WQ0033455_Engineering Report Specs and Cals_20081023

THE CLIFFS AT HIGH CAROLINA
BUNCOMBE COUNTYNORTH CAROLINA
WASTEWATER IRRIOATIOPIF
SySTEM ENOINEER"S REPORT
SPEC IFICA TIO NE
AND CALCULATIONS
PREPARED FOR*
THE CLIFFS COMMUNITIES
MR. DON NICKELL
301 BEAVER DAM ROAD
TRAVELER'S REST, SOUTH CAROLINA 29690
ORIGINAL: OCTO I BER 21, 213OW
BROOKS ENESINEERING ASSOCIATES
.PROJECT No. 30 78D8
17 Arlington Street
Asheville, NC 28801
828232.4700
RECEIVED I BEHR I DWQ
01FER PROTECTION SECTION
OCTI 3 2008

THE CLIFFS AT HIGH CAROLINA
BUNCOMBE COUNTY' NORTH CAROLINA
WASTEWATER IRRILYAT113N SYSTEM
PREPARED FOR:
THE CLIFFS AT HIGH CAROLINA, LLC
3598 HIGHWAY 1 1
TRAVELERS REST, SC 29690
FINAL DESIGN - NOT RELEASED FOR CONSTRUCTION
`,`Sttlfil8►plp/p�
RECEIVED I BENRI DWQ
AQUIFER PROTECTION SECTION
OCT -2'3 2008
ORIGINAL: OCTOBER 22, 2008
BROOKS ENGINEERING ASSOCIATES PROJECT NO.: 307808

1.0 System Summary & Project Information
1
Summary & Design Parameters
1
Contacts
4
4
Scope & Qualifiers
5
2.0 Wastewater Treatment System Components
2.1 Location of Sanitary Sewage Systems
6
2.2 Waste Water Treatment Plant
6
2.2.1 Description
6
6
2.2.2 Patented Process
6
2.2.3 Description of Proposed Process
2.3 General Consideration
7
10
2.4 Exclusions
11
2.5 Initial Design Parameters
11
2.6 Materials
11
2.6.1 Aeration and Equalization Tankage
2.6.2 Piping
12
12
2.6.3 Valves
12
2.6.4 Grating
12
2.6.5 Handrails/Toe Plates
2.6.6 Concrete
12
13
2.6.7 Reinforcing Steel
2.6.8 Manufacturer
13
2.6.9 Base Slab Installation
13
2.7 Field Service
13
13
2.8 Air Blowers and Accessories
2.8.1 Description
13
14
2.8.2 General
14
2.8.3 Exclusions
14
2.11.4 Materials and Equipment
2.9 Low Equalization Tank
18
2.9.1 Design
18
18
2.9.2 Influent Bar Screen
2.9.3 Submersible Pumps
18
2.9.4 Flow Control Box
18
2.9.5 Control Panel
19
2.10 Primary Setting Tank
19
2.11 Aerobic Towers (Three)
19
2.11.1 Plastic Media Specifications
20
2.11.2 Recycle& Forward Flow Pumps
20
2.12 Fixed Media Denitrification Reactors & Clarification Basins
21
2.12.1 Design
21
2.12.2 Hatches and Grating
22
2.13 Sand Filter
22
22
2.13.1 Scope - Self Cleaning Sand Filters
2.13.2 Design Details - Mechanical
23
2.13.3 Design Details - Process
23
2.13.4 Performance
24
2.13.5 Materials of Construction
24
2.13.6 Sparging air Supply (Parkson Package4D)
24

3.0 Wastewater Irrigation Disposal System
2.13.7 Dessicant Air Dryer Model TZM24
26
2.14
Phosphorous Removal
30
2.15
Alkalinity Control
30
2.16
Air and Gas Management
30
2.17
Building Construction
30
2.18
Ultraviolet Disinfection Equipment
31
Irrigation Distribution System
2.18.1 Design Requirements
31
3.3.1 Supply Line Force Mains
2.18.2 Ultraviolet Modules
32
3.3.2 Distribution & Return Lines
2.18.3 Monitoring System
32
3.3.3 Manifold & Valving
2.18.4 UV Lamps
32
3.3.4 Drip Lines
2.18.5 UV Lamp Sleeves
33
Wet Weather Storage Pond
2.18.6 Ultraviolet Channel
33
2.19
Sludge Holding & Thickening Chambers
33
2.20
Flow Meter
34
2.21
Telephone Service
35
2.22
Wiring Code
35
2.23
Electrical Service & Emergency Power
35
2.24
Water Service
36
2.25
Training, Operating Manuals and Electrical Drawings
37
2.26
Plant Safety
37
2.27
Autodialer
37
3.0 Wastewater Irrigation Disposal System
39
3.1
Design Criteria
39
3.2
Irrigation Dosing & Control System
39
5.3.1 Start -Up Procedures
3.2.1 Dosing Tank
39
55
3.2.2 Float Switches
39
3.2.3 WSI Pumping & Monitoring Skid
40
3.3
Irrigation Distribution System
41
3.3.1 Supply Line Force Mains
45
3.3.2 Distribution & Return Lines
47
3.3.3 Manifold & Valving
47
3.3.4 Drip Lines
49
3.4
Wet Weather Storage Pond
49
3.4.1 Design
49
3.4.2 Wet Weather Monitoring
50
3.4.3 Transfer to/from Pond
50
3.4.4 Pond Liner
50
4.0 Site Preparation
50
4.1
Clearing & Grubbing
50
4.2
Seeding & Mulching
50
4.2.1 Jute, Excelsior or Mulching
52
4.2.2 Maintenance of Seed & Mulching
52
4.2.3 Erosion Control
52
5.0 Inspection And Monitoring Proceedings
54
5.1 Pre -Construction Meeting
54
5.2 Intermediate Inspection of the System
54
5.3 Final Inspection & Start -Up
54
5.3.1 Start -Up Procedures
54
5.3.2 Pumps & Controls
55
5.3.3 Pressure Distribution
55

6.0 Calculations
6.1 Design Flow Table & Phasing Summary
6.2 WWTP Head Calculations and Process Calculations & Supporting Charts
6.3 Pump curve for irrigation dose pumps and pump curve for pumps in series
6.4 Pump Curve and TDH calculations for return pumps &tanks
6.5 Return pump tank sizing calculations
6.6 Irrigation zone pressure & flow analysis
6.7 Irrigation schedule spreadsheet
6.8 Rainfall data analysis for short term wet weather storage requirements
7.0 Attachments
Attachment A - Aqueonics Plant Cut -Sheets for: concrete mix design, railing, chemical
feed pumps, Parkson sand filter and air compressor, DuraPac trickling filter media,
Trojan UV, level controller & tranduscers, chemical feed pumps & pressure relief
valves.
Attachment B - Cut -Sheets & Pump Curves for WWTP Pumps:forward flow/recycle
pumps, sand filter flow pumps, equalization tank grinder pumps, sludge tank decanting
pump.
Attachment C - Cut -Sheets for WWTP Blowers
Attachment D - Cut -sheets and pump curve for Irrigation Dosing/Flushing Pump
Attachment E - Cut -sheets for flushing return pumps
Attachment F - Cut sheets for alternate pond liner
Attachment G - WSI PC Controller Electrical Schematics
Attachment H - Cut -sheets for drip system valving
Attachment I - Cut -sheets for Flow Meter
Attachment J - Cut -Sheets for Disc Filtration System
Attachment K -Cut-Sheets for Rainbird Rain Gauge
Attachment L - Drip Line Cut Sheets

1.1 Summary & Design Parameters
These specifications and accompanying plans are for a wastewater treatment and surface
drip irrigation disposal system to serve The Cliffs at High Carolina. The Cliffs at High
Carolina is an upscale golf course community featuring Tiger Woods first U.S. golf course
design. The project is to be developed in phases, and the permit application allows for
phasing of the wastewater treatment and disposal system. The proposed system is to be
permitted under NCAC Title 15A Subchapter 2T.0500 Wastewater Irrigation System
requirements. The proposed wastewater treatment meets reclaimed water effluent
standards and uses setbacks outlined in 15A NCAC 02T.0900. The treated effluent will
ultimately be utilized as a supplemental source of golf course irrigation water. However
the timing of the construction requires that an independent irrigation system be permitted
initially with the golf course irrigation being permitted at a later date as a conjunctive use
system.
As the site construction plans for the development are still in preliminary design, the
collection system served by the wastewater irrigation system will be permitted as a
separate system under NCAC 15A.0300 regulations by the NCDENR DWQ PERCS Unit.
The project is to be developed in phases with village community concept. The permit
application is for 200,000 gallons per day (gpd) with construction phasing in to two
100,000 gpd systems. Eight different residential "villages" are to be developed along six
different amenity sites/villages for a total of fourteen separate sites. The residential
component includes 175 units with a mix of single family and multi -family units with varying
numbers of bedrooms. The commercial buildings and amenities include: an Inn,
Clubhouse, Banquet Hall, Spa, Pool, two Wellness Facilities, golf maintenance facility, a
restaurant and small market. A breakdown of the units and the calculated design flow is
provided in Section 5.1.
The collection system will deliver raw wastewater to the proposed Aqueonics, Inc. multi-
stage aerobic/anaerobic fixed media trickling filter wastewater treatment process (Model
K -100-3/K-200-3). The Aqueonics plant utilizes a three stage aerobic/anaerobic fixed
media, fixed biofilm, trickling filter process to facilitate biological degradation of organics,
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 1 The Cliffs at High Carolina

nitrification and denitrification. The system operations are highly flexible with multiple
junctures to regulate recirculation of treated effluent and biomass. Treated effluent is
disinfected by a dual ultra -violet disinfection system. The 200,000 gpd treatment system is
to be constructed in two phases of 100,000 gpd each. All of the tankage and infrastructure
for the 200,000 gpd system is to be constructed in the initial phase of development. Media
filters, pumps, valving and other appurtenances will be installed for the second 200,000
gpd when phased in.
After disinfection the treated effluent is discharged to the dosing tank. A wet weather
monitoring system can delay the irrigation cycle during precipitation events and flows will
be diverted to a nine -day wet weather storage pond should levels in the dosing tank rise
sufficiently to trigger a dosing event to the storage pond. The disposal system consists of
the dosing system and dual zone dosing distribution and irrigation system.. The dual zone
irrigation system doses two zones simultaneously and flushes one to keep similar
hydraulic regimes during both dosing and flushing events. The irrigation system is broken
in to six (6) primary zones for dosing with twelve (12) subzones for flushing. These are
located in 32 irrigations areas as defined in soils report, The effective soil loading rate,
1.94 in/wk (0.173 gpd/ft2), is utilized for all irrigation areas. The soils report and
hydrogeological report identify an allowable irrigation rate of at least 2.0 inches/week. The
zones are constructed in two phases with each phase capable of disposing of 100,000
gpd. This zones and corresponding phase are depicted in the Construction Drawings
(CDs). The dosing of the irrigation fields is monitored and sequenced by a Wastewater
Systems, Inc. PC control system, which can detect leaks or clogs in the system with the
flow monitoring. Should a dosing flow for a particular zone be outside of the tolerances
established, the zone is eliminated from the irrigation schedule and the operator notified of
the condition. The dosing system is a 30,000 gallon below ground prestressed concrete
tank provided and constructed by Aqueonics to the same specifications as the treatment
plant tankage. The pumps and controls are a skid mounted centrifugal pump/filtration/flow
monitoring and control system manufactured by Wastewater Systems, Inc.. The drip
irrigation fields consist of a top -feed manifold system, pressure and flow regulating valving,
and NetafimT"" 20 mm drip tubing with 0.62 gph pressure compensating emitters installed
on two foot centers
r ti Brooks Engineering Associates, PA
Project No. 307308 2
Wastewater Irrigation System Specifications & Calculations
The Cliffs at High Carolina

This wastewater irrigation system is designed in accordance with requirements set forth in
15A NCAC 02T .0500. The treatment standards for this system are as follows:
1. Monthly average BODS of less than or equal to 10 mg/I.
2. Monthly average TSS of less than or equal to 5 mg/I.
3. Monthly average NH3 of less than or equal to 4 mg/I.
4. Monthly average geometric mean fecal coliform of less than or equal to 14
cfu/100 ml
5. Maximum turbidity of 10 NTU.
System calculations and accompanying pump curves are provided in Section 5.
Manufacturer product specification sheets (cut -sheets) for each of the products specified
are provided in Section 6.
All specifications are subject to North Carolina Laws and Rules for Waste Not Discharged
to Surface Waters 15A NCAC 2T.0500 and North Carolina State Plumbing Code and
North Carolina State Electrical Code, where applicable. Any use of "equivalent products"
shall first be approved by the Project Engineer prior to installation.
Brooks Engineering Associates, PA
Project No. 307308
3
Wastewater Irrigation System Specifications & Calculations
The Cliffs at High Carolina

1.2 Contacts
Engineer— Mark Brooks, PE, Brooks Engineering Associates [phone]
Soil Scientist — John Allison, LSS, Brooks Engineering Associates [phone]
Owner Contact — Don Nickell [phone]
Aqueonics Representative — Jerry Traynham [phone]
Wastewater Systems, Inc. — Brian Britain, [phone]
1.3 Scope & Quaftiers
This specifications manual is intended only for the use of permitting and construction of
the intended wastewater treatment facility. Any changes to these plans and specifications
shall be approved by the Project Engineer. Any changes in layout of equipment not
approved shall release the Engineer of any potential liability associated with the system.
The maintenance and operation of the system are to be in accordance with the Operation
& Maintenance Plan provided as a separate document. Monitoring requirements and
discharge limitations are detailed in the NCDENR Non -discharge Permit.
Notify Engineer in sufficient time to permit inspection of underground work before
backfilling is initiated. A final inspection shall be required with the Owner, Engineer,
NCDENR representative, and Contractor. Only the set of engineering plans with revision
labeled "RELEASED FOR CONSTRUCTION" shall be utilized for construction.
All construction lines shall conform to the latest Henderson County and State of North
Carolina specifications as defined by Standards and Specifications and the North Carolina
Building Code. Where two (2) standards conflict, the more stringent shall apply.
i Brooks Engineering Associates, PA wastewater Irrigation System Specifications & Calculations
Project No. 307308 4 The Cliffs at High Carolina

2.0 WASTEWATER TREATMENT SYSTEM COMPONENTS
2.1 Location Of Sanitary Sewage Systems
Rule 15A NCAC 02T.0506 states that effluent meeting secondary treatment standards
(30/30/15 monthly average) contained in 15A NCAC 02T.0506 /.0912, the setbacks for
wastewater drip irrigation sites are as follows:
Any residence or p lace of public assembly under separate ownership
100
residence or place of public assembly owned by the permittee
15
-Any
private or public water supply source
100
-Any
Surface Waters (not SA)
25
Groundwater lowering ditch
100
Surface water diversions
25
Well
100
Property Line
0
0
Top of slope with 2 ft cut
15
Water line from disposal system
10
Groundwater lowering drainage system
100
Swimming pool
100
Public Right of Way
50
Nitrification field
20
Building Foundation or basement
15
The setbacks for treatment and storage units shall be as follows:
An residence or place of public assembly under separate ownership 100
Any private or public water supply source 100
Surface Waters 50
Well 100
Property Line 50
These setbacks are depicted on the Engineering Plans and shall be maintained in
construction.
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 5 The Cliffs at High Carolina

Waste Water Treatment Plant
2.2.1 Description
The contractor shall furnish all labor, materials, tools and equipment required to
construct and complete the proposed sewage treatment plant including: Aqueonics
Inc. Model K -100-3/K-200-3 as manufactured by Aqueonics Inc., Parkson® Model
DSF-19 DynaSand filter, aerated sludge holding, ultraviolet disinfection, and all
piping and valves as shown on the drawings or specified herein except as noted
otherwise.
2.2.2 Patented Process
The treatment process is covered by United States Patent 4279753 -- Method and
apparatus for the treatment of industrial or municipal wastewater including multiple
series of alternating aerobic -anaerobic bioreactors in series. Each of such pairs
includes fill supporting fixed film microorganisms. The wastewater from primary
treatment flows into a first aeration bioreactor and downwardly through the fill where
it is contacted by the microorganisms. The effluent is passed to the bottom of an
anaerobic bioreactor for passage upwardly past submerged microorganisms affixed
to the fill walls. Part of the nutrients in the wastewater is consumed in this first
aerobic -anaerobic stage. The wastewater is then passed to a second and third
aerobic -anaerobic bioreactor stage. Incremental consumption of organic nutrients,
nitrification and denitrification occurs in each stage. Thereafter, it is subjected to
tertiary treatment.
2.2.3 Description of Proposed Process
The treatment processes includes the unit operations:
• Bar Screen
• Flow Equalization, Aerated -- 4 float control system
• Duplex Grinder lift pumps to Constant Head Tank
• Primary Sedimentation
• Alternating Aerobic/Anaerobic Treatment Reactors - Three Stages
• Alum injection & Flocculation
• Alkalinity Addition
• Tertiary Sand Filtration
• UV Disinfection
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 6 The Cliffs at High Carolina

• Holding Tank for Dosing
• Dosing Pumps & Final Filtration for land application
• Aerobic Sludge Holding and Digestion
• Odor Control and Positive Treatment of all Process Gases
2.3 General Considerations
The basic process proposed to treat domestic wastewater and remove nitrogen at this facility is
a combined Caron Oxidation — Nitrification — Denitrification system using endogenous carbon
and sequential aerobic/anaerobic (anoxic) conditions (with recycle of nitrified wastewater for
BOD enrichment) for denitrification using fixed -film reactors.
The specific process design selected is a biological process, which makes use of
concepts that have generally been known for more than 25 years Pilot systems
using this process were first installed in the mid -1970's, with full scale installations
occurring in 1979.
Typical average nitrogen content of domestic wastewater averages 40 mg/I as N. It
is assumed that the influent nitrogen concentration at this site will be in the range of
60 mg/I as nitrogen, which is to be reduced to a maximum of 5 mg/I of Total
Nitrogen with a maximum of 3 mg/I being nitrate nitrogen with the balance
comprising ammonia and nitrite.
Organic nitrogen is both soluble and particulate with the soluble organic nitrogen
mainly in the form of urea and amino acids. Primary sedimentation acts to remove
a portion of the particulate organic matter. This generally will amount to 20% or
less of the total nitrogen entering the plant. Soluble organic nitrogen is partially
transformed to ammonium by microorganisms, but concentrations of 1 to 3 mg/I are
usually found in biological treatment effluents.
The proposed plant uses the carbon oxidation -nitrification -denitrification processes
are combined into a coherent operational plan. The advantage of such processes
for effective nitrogen removal include: (1) reduction in the volume of air in
suspended solids reactors (or pumping energy to a trickling filter) to achieve
nitrification and BODS removal; (2) elimination of the supplemental organic carbon
sources (e.g., methanol) required to complete denitrification; (3) stability of
operations over long time periods.
Brooks Engineering Associates, PA
Project No. 307308
7
Wastewater Irrigation System Specifications & Calculations
The Cliffs at High Carolina

In these combined processes, either the endogenous decay of the organisms or the
carbon in the wastewater is used to achieve denitrification. In addition to the
Aqueonics process, other examples are oxidation ditches where rotor oxygenation
levels are controlled as in the "Bardenpho" process. These processes are reviewed
in the 1975 USEPA Process Design Manual for Nitrogen Control Section 5.5 where
combined Carbon Oxidation — Nitrification — Denitrification System using
endogenous carbon and Sequential Operations developments are reviewed and
commented upon. Most of these processes, however, utilize suspended growth
rather than fixed -film growth, which are more difficult to maintain a stable operating
condtion in smaller facilities such as this one.
As early as 1975 a Danish plant of 5,678 m3/day (1.5 million gallons per day (mgd))
using the "alternating contact" process was able to achieve nitrate levels of 2.0 to
5.0 mg/I. The "Bardenpho" process of South African development was also able to
achieve 5 to 7 mg/I of total nitrogen under long term performance at 98.42 M3 /day
(26,000 gpd).
Operation of suspended growth reactors in the alternating aerobic/anaerobic
(anoxic) mode requires an F/M ration sufficiently low to permit the development of a
mixed culture of organisms for carbon oxidation, nitrification, and denitrification; and
severe filamentous bulking conditions are also developed sometimes in the sludge
as a result of this low F/M ratio. Maintenance of this proper ration is a sophisticated
operational problem Fixed -film reactors by their inherent nature require no F/M
ration, since fixed bacteria automatically adjust their growth rate to the food source,
and there is, of course, no suspended sludge to bulk. Fixed -film designs, therefore
avoids these problems, give greater stability to the process, and greatly reduce the
risk of sludge loading of the subsurface distribution beds.
The Blue Plains work did serve to establish several benchmarks with respect to
criteria used in the design of alternating systems. They are as tollows: (1) 10
evaluate nitrification limitations on a system, both nitrogen loads and nitrification
rates must be taken into account, and, (2) there is general agreement that the
design of the combined carbon oxidation — nitrification functions of the aerobic
phase(s) can be separated from the anoxic phases(s). Therefore, the carbon
oxidation and nitrification calculations for the aerobic periods can be virtually
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 8 The Cliffs at High Carolina

identical to those advanced from ordinary carbon oxidation — nitrification processes
(See same USEPA document Section 4.4.1).
The Blue Plains work also supports a rational approach to sizing of the
denitrification steps and presents measured denitrification rates in systems using
wastewater as the organic carbon source. The relatively modern concept of the
coupling of an anoxic residence period with an aerobic residence period in these
systems is based on the recognition that dissimilatory denitrification is
accomplished by facultative bacteria using biochemical pathways that are almost
identical to aerobic biochemical pathways. These facultative bacteria can shift
readily from using nitrate to using oxygen and vice versa. In the aerobic towers, the
carbon and ammonia are oxidized and nitrogen gas stripped from solution so that
nitrogen gas bubbles will not form in the next packed -reactor or in the sedimentation
process.
Aqueonics' use of fixed -film reactors with stable operational characteristics are a
considerable advancement over other aerobic/anaerobic (anoxic) processes, and
provides a more easily operated, more reliable, less maintenance intensive, and
less costly system to operate than denitrification processes using either methanol -
based systems or suspended growth alternating systems.
The work of Van de Graaf, et al (Applied and Environmental Microbiology
61(4):1246 (1995) Microbiology 142:2187 (1996), and Microbiology 143:2415
(1997)) has identified an autotrophic anaerobic biological pathway for simultaneous
removal of both ammonium and nitrate which has been found to operate in long-
term fixed film systems such as are formed in subsurface distribution systems.
(Woods, et al Proceedings of 72nd Water Environmental Federation Annual
Conference 10/9-13/99). Observations indicate that stable environments for growth
of such colonies require stable fixed media reactors to achieve the reaction: CO2 +
10NH4 + 6NO3 anaerobic/autotrophs 8N2 + 2OH2O = C. Also require as sufficient
alkalinity to neutralize the increase in acidity and to provide about 1 mg of carbon
per mg of nitrate -nitrogen removed. This carbon source can be from organic
carbon in the influent, or from inorganic carbon alkalinity in the form of CO2 resulting
from the respiration of heterotrophic consumption of organic carbon, as shown
above, or added soda ash.
Brooks Engineering Associates, PA Wastewater irrigation System Specifications & Calculations
The Cliffs at High Carolina
Project No. 307308 9

In addition to alternating aerobic/anoxic fixed -film reactors, this system also
incorporates a primary clarifier to take advantage of its large removal rate of
particulate organic nitrogen and BOD. The design integrates hydraulic loading,
recycle capability, sludge handling and solids separation to provide a plant with
proper balance and flexibility in operation.
Aqueonics has conducted extensive full scale testing at Castlewood, California to
verify kinetic design parameters for this process. Aqueonics has further developed
this concept in New Jersey at the Oaks of Weymouth facility and other installations
and the results of those operations are incorporated in this design.
The system provided is the Aqueonics K -Series design. The process provides
screening and maceration of solids, flow equalization, primary sedimentation, and a
series of three alternating aerobic and anaerobic (anoxic) reactors which are
designed for carbon oxidation — nitrification and denitrification using influent sewage
as a carbon source for denitrification, and is followed by self-cleaning sand filtration,
and UV disinfection. The in ground tankage consist of a reinforced cast in place
concrete base slab constructed with attachement slots and connections for pre -cast
reinforced concrete panels. The above grade aerobic towers are constructed with
water tight fiberglass walls and fixed -film PVC media. The installation including the
towers are totally enclosed within an insulated building resembling a two story
single family residence or small commercial/institutional facility where the concrete
tankage provides the foundation.
A flow through forced air system provides process air for the aerobic towers and a
means to purging of gases from the anoxic reactors All process air is chemically
scrubbed by a potassium permanganate and activated carbon filter system before
being exhausted from the facility. In addition to silencers, all machinery and
equipment are located inside the insulated building to minimize external sound
levels.
2.4 Exclusions
The electrical contractor shall perform all inter -connecting electrical work between the
treatment plant and other structures or buildings. The General Contractor shall perform all
poured in place concrete with or without reinforcing steel, all structures and buildings other
than the treatment plant, and all painting.
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 10 The Cliffs at High Carolina

2.5 initial Design Parameters
The wastewater treatment plant shall be designed using the following criteria:
Plant capacity shall equal 200,000 gallons per day average daily hydraulic flow split in to
two phases of 100,000 gpd each. The predicted influent raw sewage characteristics
utilized in design and calculations are:
Biochemical Oxygen Demand 5 da BOD
350 m /I
Total Suspended Solids (SS)
250 m /I
Total Nitrogen as N
60 m /I
Total Phosphorus as PO4
20 m /I
Temperature (deg. C Min.
13 de .0
The wastewater treatment plant shall be designed to provide an effluent quality that has a
maximum 30 -day average concentration of:
Biochemical Oxygen Demand (5 da) (BOD)
10.0 m /I
Total Suspended Solids SS
5.0 m /I
Total Nitrogen (3 m /I NO3, 1 m /I NO2, 1 m /I Ammonia)
5.0 m /I
Turbidity
<10 NTU
Phosphorus (as P)
4 m /I
Fecal Coliform —(daily max
25 NTU / 100 mg/1
Fecal Coliform — (monthly averse)
14 NTU / 100 m /I
2.6 Materials
The materials used in construction of the wastewater treatment plant described herein
shall conform to the following:
2.6.1 Aeration and Equalization Tankage
The plant shall be constructed in the "slab" method where a base concrete slab
supports precast side and interior walls. All slabs and chambers, and fabricated units
shall be constructed of reinforced, precast concrete with 4,500 pounds per square
inch, 28 -day compressive strength. Minimum wall thickness shall be eight (8) -inch
unless otherwise noted. Walls shall be structurally sized by others and reinforced to
adequately function for their intended uses and shall withstand all required internal and
external loading. Wall panel surfaces shall be smooth and free of air hole and
honeycomb pockets unless otherwise specified. "Waffle wall' type wall panel will not
be acceptable as tanks with this type of surface finish can be adversely affected by
frost heave on external wall surfaces. All walls and joints shall be watertight. All
reinforcing steel furnished under this item shall meet the requirements in this
specification.
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & caicuianons
Project No. 307308 11 The Cliffs at High Carolina

2.6.2 Piping
All water / sewage piping shall be Sch.40 PVC pipe with standard weight PVC fittings.
Pump Connections — Sch. 40 galvanized steel threaded with standard weight
galvanized fittings.
Air piping — Above Floor shall be Sch. 40 galvanized steel or Sch. 80 PVC pipe. Below
Floor shall be Sch. 40 Stainless Steel. All piping shall be adequately supported
throughout its length.
2.6.3 Valves
Process control valves shall be wafer -type, rubber seats, polymer body butterfly, or full
port, polymer body ball valves. Operators and extension shafts shall be provided for
under floor locations. Crane or Nibco — engineer approved.
2.6.4 Grating
All grading shall be of fiberglass construction unless otherwise noted. The strength of
the grating shall be provided as required to meet OSHA safety, building codes or other
regulatory requirements for guarding tanks and open pits and walkways not otherwise
protected by handrails with toe plates.
2.6.5 Handrails/Toe Plates
When not protected by hatches, handrails shall be installed around all tank openings.
Handrails shall be of 1 -1/2 -inch diameter anodized aluminum pipe construction that
meets all OSHA requirements for lateral loads and impacts.
2.6.6 Concrete
Cement shall be Type II, Chemical Resistant, Portland Cement using up to 20% Type -
F Fly Ash for warm weather use or Type -C Fly Ash for cold weather use. Coarse
aggregate shall consist of either high-grade limestone or "gravelite" material where
necessary. Fine aggregate shall consist of organic -free, well -graded sand. Use of
super Plasticizers and water -reducing agents shall be allowed in order to enhance
workability and retain strength and acceptable water/concrete ratio. Manufacturers
shall be required to submit concrete mix designs for the engineer's approval along with
manufacturing and technical paperwork covering additives and dosage rates.
Engineer may at his discretion make a plant visitation to inspect the manufacturer's
facilities, testing area, and quality control program.
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 12 The Cliffs at High Carolina

2.6.7 Reinforcing Steel
Steel rebar shall be of equal quality or exceed ASTM 671, Grade 60 standards. All
welded -wire fabric mesh shall conform to ASTM C 185.
2.6.8 Manufacturer
The manufacturer of the concrete elements of this plant shall have precast concrete
aeration treatment plants of this type and size in successful operation in the field for
a minimum of five years.
2.6.9 Base Slab Installation
The General Contractor shall install the base slab in accordance with detail design
drawings to be furnished by the precast plant supplier. The precast concrete
aeration treatment plant shall be installed in accordance with the manufacturer's
recommendations and at the locations shown on the drawing.
2.7 Field Service
A competent factory representative shall be provided for the purpose of final inspection,
start-up, and adjustment of the precast concrete aeration treatment plant provided under
this item. In addition, this same representative shall spend at least two seven -hour days
solely training and instructing the operator(s) in the operation and maintenance of this
plant.
The manufacturer shall be required to supply the engineer with a complete set of as -built
drawings and operation and maintenance materials after equipment has been installed.
Any changes or modifications shall be reflected in the as -built drawings.
2.8 Air Blowers and Accessories
2.8.1 Description
The specifications provided herein are specific for Phase I of the treatment plant
installation. Individual blowers will be replaced with the implementation of Phase II
with blowers of the same quality but with approximately double the air flow.
Under this item, the contractor shall furnish all labor, materials, tools and equipment
required to complete all air blowers and accessories as shown on the drawings or
specified herein.
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 13 The Cliffs at High Carolina

capacity. This blower shall be provided with controls that automatically shutdown the
blower when backpressure falls below three (3) feet of water (1.3 psi).
Blower Specifications
All plant blowers shall be manufactured by the same manufacturer to facilitate
maintenance, repair, service and spare parts. The blower casings shall be gray cast
iron. The impeller shafts shall be constructed from a common ductile iron casting.
Impellers are to be straight, two -lobe, involute type, operating without rubbing or
liquid seals or lubrication, and shall be positively timed. The timing gears shall be
machined, heat-treated alloy steel. The spur tooth gears shall be mounted on the
impeller shafts on a tapered fit, secured by lock nuts. The impellers/shafts are to be
supported on single row ball bearings. A positive lip -type seal shall be provided at
each bearing, designed to prevent leakage of lubricant into the air streams. The
impeller sides of the lip -type seals shall be vented to atmosphere to eliminate carry-
over into the air streams.
Mountings
The air blowers units shall be completely factory assembled. Each air blowers and
motors unit shall be mounted on common heavy steel base plates along with related
equipment such as couplings and belt guards. The steel base plates shall be
provided with flanges suitable for installation with stainless steel anchor bolts. Air
blowers without base plates shall not be acceptable. The blower openings shall be
sealed after rust -inhibiting powder is injected and prior to shipment. The drive
between the motor and blower shall be guarded (belt guard) in accordance with all
applicable safety and OSHA regulations. The blowers and common base plates shall
be factory primed with a corrosion resistant coating prior to shipment. The
motor/blower set shall be installed inside the plant.
Accessories
Each of the motor/blower units will be equipped with no less than one additional set of
sheaves and pulleys to operate the blowers at mid-range of their maximum air
requirements to facilitate winter and summer, start-up and full operating conditions. An
extra drive belt shall be supplied with each Motor/Blower unit. The discharge of each
motor/blower shall be supplied with a weighted pressure relief valve and
Technocheck® check valve and equipped with high temperature and pressure
switches to control their operation in the event of failure to start, pressure loss, or
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 16 The Cliffs at Nigh Carolina

high temperature operation. Each blower shall be individually controlled using 15
minute increments, 24/7 timers to control the amount of air (oxygen) delivered to the
system.
Silencers
Each blower shall be equipped with an individual inlet filter, inlet silencer and outlet
silencers. Each unit shall be sized according to the manufacturer's recommendation
for the speed of the blower, air volume and airflow. The equipment shall be installed
to fully support the weight and vibration of the equipment.
Air Inlet Filter
For each intake shall be a Universal CC -F Series in MPT or Flange 125/150# Pattern
sized for the discharge port of the blower. Each filter shall be equipped with a
differential pressure gauge and paper filter element. The units shall have a corrosion
resistant epoxy coated or galvanized housings.
Inlet Silencer
For each intake shall be Universal rotary blower silencers, Series RISY chamber
absorption type inlet silencers. The silencers shall be sized according to
manufacturer recommendations to effectively reduce the noise and low frequency
pulsations that can be detrimental to surrounding equipment and personnel, as well
as neighbors.
Outlet Silencer
Outlet silencers shall be Universal rotary blower silencers, Series RISY chamber
absorption type discharge silencers. The silencers shall be sized according to
manufacturer recommendations to effectively reduce the noise and low frequency
pulsations that can be detrimental to surrounding equipment and personnel, as well
as neighbors.
Equipment Control Panel
A NEMA 4X, or equivalent, control panel for control of all air blowers shall be timing
relays provided. This control panel shall include breakers, starters, timers
hand/off/auto switches that are required to operate three blowers.
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 17 The Cliffs at High Carolina

2.9 Lowe Equalization Tank
2.9.1 Design
Two flow equalization basins shall be rectangular in cross section and have an
effective minimum capacity of 43,350 gallons each for a combined total tankage with
Phase II implementation of 87,120 gallons of equalization, which well exceeds the
20% requirement. The EQ pumps specified herein are for Phase I. The pumps are
to be replaced with the implementation of Phase II with pumps of a similar
specification but the double the flow capacity (at the same head conditions).
Dimensions shall be as shown on the drawings. A pumping system and a flow
control box shall be provided capable of delivering wastewater to the plant at the
maximum design flow and head. An air diffusion system shall be supplied with all
necessary piping and control valves. See air flow equalization blower shown above.
2.9.2 Influent Bar Screen
A bar screen shall be fabricated of hot dipped carbon steel with 2" o bars on 2"
centers inclined at 450. One shall be installed in each EQ basin with the
implementation of each Phase. The size of the screen shall be such that the
velocities — at 200,000 gpd have an approach velocity no more than 1.25 feet per
second.
2.9.3 Submersible Pumps
For Phase I, duplex grinder pumps shall be Hydromatic Model HPGF, 1750 RPM,
60Hz, 3 HP, 230/460 volt, 3 phases, 60 cycles, 70 gpm @ 25 feet TDH. The pumps
shall have a 2 -inch diameter vertical discharge and designed to reduce domestic and
institutional sewage to a finely ground slurry. These pumps shall be rail mounted
using a quick disconnect lift out system that does not require entry into the basin and
equipped with a stainless steel lifting to aid in pump removal. Overload protection
shall be mounted in the control panel.
2.9.4 Flow Control Box
The flow control box installed in Phase I provides sufficient flexibility in the adjustable
weir arrangements to suit the flow ranges in Phase I and II. An aluminum and
fiberglass flow control box shall be provided to equalize the flow of sewage into the
plant aeration basins. See drawings for design. Flow rates into the plant will be
controlled by the rectangular weirs in the flow control box to return excess flow to the
flow equalization basin. Two adjustable V -notch weirs control forward flow to the
plant and a future addition. The control box design flow shall be 140 gallons per
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Project No. 307308 18 The Cliffs at High Carolina

minutes with provisions to operate two trains of a daily flow of 70 gallons per minute.
The internal weirs shall be adjustable downward to a daily flow rate of less than
30,000 gallons per day.
2.9.5 Control Panel
A NEMA 4X, or equivalent, control panel shall be provided which shall automatically
alternate the lead pump for subsequent pumping cycles. The panel shall contain
required breakers, contactors, hand/off/auto switches, run lights, and all necessary
controls required for automatic operation. A red, high water alarm light and auto -
dialer alarm connection shall be provided to indicate high water in the flow
equalization basin for pump control and alarm activation.
2.10 Primary Settling Tank
Two primary settling tanks are provided each with a sufficient capacity for 100,000 gpd.
Upon implementation of Phase II both tanks will be combined (via internal hatches) to act
as a singular settling tank. The supplier shall provide two primary settling tanks following
the flow equalization tank with the following specifications.
• 6.5'x19.5'x12'SWD.
• Effective settling area 113 sq. ft.
• Surface overflow rate 885 gpd per sq. ft.
• 60 -degree slope hoppers.
• Two 3" o airlift pumps for sludge removal.
• Inlets and baffles shall be designed to dissipate the inlet velocity, to distribute the
flow equally both horizontally and vertically and to prevent short-circuiting.
• Weir troughs shall be designed to prevent submergence.
• Scum Removal shall be by airlift skimmer 4' dia.
2.11 Aerobic Towers (Three)
Supplier shall provide three towers with fixed media. Each tower shall be 12' x 12' x 20'
and contains 2,880 cubic feet of media for each phase. Tower I shall contain plastic
media with a surface area of 30 ft2/ft3. Towers II and III shall contain plastic media with
a surface area of 68 ft2/ft3. Sufficient room is to be constructed in Phase I for the
insertion of three Phase 11 towers.
2.11.1 Plastic Media Specifications
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Project No. 307308 19 The Cliffs at High Carolina

The media shall be fabricated from rigid PVC sheets completely corrugated forming a
cross -corrugated pattern with adjacent sheets to permit continuous norozoniai
redistribution of both the air and wastewater throughout the depth of the media. The PVC
roll stock sheets shall be of uniform thickness with no sections less than ± 0.002 -inch
manufacturing tolerance. The media shall be specifically designed for use in the
biological oxidation of municipal and industrial wastewater.
The polyvinyl chloride used in the media shall be resistant to degradation from ultraviolet
radiation, rot, fungi, bacteria and other forms of microorganisms. The media shall be
chemically resistant to concentrations of common inorganic mineral acids or alkalies and
organic solvents or compounds normally experienced in sewage.
Each module shall consist of several PVC sheets, bonded together to form a structurally
self-supporting block measuring 24" wide x 24" high x 48" or 72" long. The modules shall
be designed with a minimum specific surface area of 30 and 68 square feet per cubic
foot with a minimum 95% void volume ratio. Each module shall be capable of
withstanding a minimum load of 35 pounds per square foot per foot of media depth.
Maximum allowable deflection shall be limited to 2%.
The manufacturer shall submit test reports for the mil thicknesses to be supplied. Test
reports shall comply with the requirements of paragraph C. If there are no test reports or
if there are any alterations to the media in respect to materials or design, the
manufacturer shall test the modules in accordance with paragraph C.
Individual sheets used in the manufacture of the media shall conform to commercial
standards ANSI/ASTMD1784-78:12454C with the following physical properties when
tested in accordance with the method indicated
2.11.2 Recycle & Forward Flow Pumps.
For each phase, the supplier shall provide three pumps and one spare pump for the
three towers. Transfer flow shall be sufficient for 101% recirculation of the 70 gpd
influent flow. Flow at 144 gpm shall be lifted to the top of each tower using a Size:
30MMP Hydromatic Self Prime Model 30MMP, 3 hp, 3 -inch discharge, 144 gpm, @ 30'
TDH, 230 volt, 3 phases, 60 cycles. One stand-by pump shall be provided. Provide
each tower with one Aqueonics flow dividing split to divide the flow to (8) spray nozzles
to wet the media. Hydraulic loading of the media shall be a nominal 1 gpm per square
foot, or 144 gpm.
Brooks Engineering Associates, PA wastewater Irrigation System Specifications & Calculations
Project No. 307308 20 The Cliffs at High Carolina

2.12 Fixed Media Anaerobic Reactors & Clarification Basins — ('Three)
The three "anaerobic" reactors shall be designed to achieve three functions: First, as a
tube settler for solids removal, second, to create an anoxic environment to accomplish
denitrification utilizing sewage as the organic carbon source and, thirdly, to achieve partial
"anaerobic" digestion of biomass.
Each of the "anaerobic" reactors shall contain plastic media having a surface area of 30
ft2/ft3 placed atop precast concrete hoppers on fiberglass beams within the tankage.
Influent shall enter each "anaerobic" unit from beneath the media and flows in a serpentine
manner through the media. A hydraulic retention time of 2 hours shall be maintained for
media contact to accomplish the anoxic denitrification reaction. The surface overflow rate
shall be 879 gpd/ft2 or less and presence of the media makes these reactors extremely
efficient clarifiers in addition to their primary function in biological denitrification.
Denitrification conversion efficiency is limited only by minimal concentration of the nitrate
substrate with which the colonies of facultative anaerobe denitrifiers can be maintained.
An effluent consistently less than 3 mg/I nitrate -nitrogen has been achieved in similar
facilities
The process of anoxic denitrification is confirmed by EPA design data. (Process Design
Manual for Nitrogen Control. U.S. EPA Technology Transfer. October, 1975.)
2.12.1 Design
The media will be installed in three percast concrete tanks located below the
aeration towers. These tanks shall be constructed with a 4,500 -pound per square
inch, 28 day compressive strength. Minimum wall thickness shall be 4 -inches unless
otherwise noted on the drawings. "Waffle wall" type wall panel will not be acceptable
as tanks with this type of surface finish can be adversely affected by frost heave on
external wall surfaces. All walls and joints shall be watertight.
Each basin has a hydraulic capacity of approximately 8,400 gallons (12'0" x 12'0" - 8`
SWD above the hopper bottom) for a detention time of 120 minutes.
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The fixed media shall meet the specifications show above for the aerobic tower. The
media shall be self-supporting block measuring 24" wide x 24" high x 43" or 72" long.
The modules shall be designed with a minimum specific surface area of 30 square
feet per cubic foot with a minimum 95% void volume ratio. Each module shall be
capable of withstanding a minimum load of 35 pounds per square foot per foot of
media depth. Maximum allowable deflection shall be limited to 2%. The media shall
be supported on fiberglass structural member adequate to support the load of wet
media when the chamber is emptied.
Provide duplex lift pumps between the discharge side of reactor III and the sandfilter.
Provide two Hydromatic Model SP -40, 70 gpm @ 15' TDH, 0.4 hp. Lift is
approximate 4 feet.
2.12.2 Hatches and Grating
Each tank opening shall be covered by a locking aluminum hatch flush with the floor
designed for a 300 Ib/sq. foot load. If fiberglass grating is used, Fibergrate® or
engineer approved equal. The strength of the grating shall be provided as required
to meet OSHA safety, building codes or other regulatory requirements for guarding
tanks and open pits and walkways not otherwise protected by handrails with toe
plates.
2.13 Sand Filter
2.13.1 Scope - Self Cleaning Sand Filters
With each Phase, a DynaSand Filter Model DSF19-DBTF, manufactured by
Parkson Corporation will be installed. Each sand filter shall be provided with a
Ingersoll-Rand, Duplex, lubricated, air-cooled, reciprocating compressor, Type 30,
Model 2-2475E5.
The filters shall consist of a cylindrical tank with a conical hopper, feed inlet
manifold, feed distribution radials; filtrate weir and flume; airlift pipe, internal sand
washer, sand distribution cone(s), reject compartment with weir and flume and a
compressed air control system.
The filter shall operate in manner such that the total cross-sectional area of each
filter shall be in a continuous filtration and a continuous backwash mode. There
shall be no interruption of the filtration process by shutting down a part of a whole
filter for backwashing.
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2.13.2 Design Details — Mechanical
• The filter shall be a continuous backwash, upflow, deep bed single media filter.
Mixed or multiple media shall not be allowed.
• The filter shall operate countercurrent. The feed shall be upflow with sand
moving downward.
• Each filter shall provide a minimum of 19 ft2 of filtration area.
• Each filter tank shall be 15.67 ft. in height and have an internal diameter of 5
feet.
• Each tank shall come complete with 1501b drilled flanged connections including
a 6" G feed connection, 3" 0 reject connection 6" 0 filtrate connection, and a
VO drain connection.
• Each tank shall have a wall thickness of 11 GA.
• The filter shall be designed for a bed depth of 80".
• The filter shall not contain any moving parts.
• The filter shall not contain any screens, wedgewires, grids, etc., to retain the
media in place.
• The air supply system shall consist of a separate panel including an air filter,
control valve, air flow meter, pressure regulator, and pressure gauge.
• The unit shall come complete with access ladders and platform.
• The filter shall be designed for Seismic Zone 0 installation.
2.13.3 Design Details — Process
The units shall be designed to filter out of suspended solids from a peak flow of
69.44 gallons per minute of municipal biological -following clarification feed stream
containing approximately 20 ppm of TSS. Based on 19 ft2 of total filtration area,
the loading rate shall be 3.65 gpm/ft2.
The filter shall produce a continuous filtrate stream and a continuous reject stream
and shall not be shut down for any backwash cycles. No backwash valves, pumps,
instrumentation shall be required for backwashing.
The sand bed shall be continuously backwashed internally and redistributed on top
of the san bed an average of 4 to 8 times per 24 hours.
Brooks Engineering Associates, PA
Project No. 307308
Wastewater Irrigation System Specifications & Calculations
23 The Cliffs at High Carolina

s
Continuous sand cleaning shall be accomplished within the filter using filtered
water. Filter influent (feed) shall not be used for sand cleaning. External sand
movement or washing is not allowed.
r
The headloss through the filter shall not exceed 48".
The backwash surface loading rate shall exceed 50 to 100 gpm/ft2 to ascertain a
superior scouring and cleaning of the sand.
The air scouring of the sand shall exceed 100 to 150 SCFM/ft2. This shall be
accomplished by supply 1.6 SCFM of air per unit at 15 to 25 psi. (Air supply
specifications shown below in these specifications).
2.13.4 Performance
The units shall have a record of at least 5 U.S. installations and operation of not
less than 2 years.
2.13.5 Materials of Construction
1. Tank
2. Feed Pipe
3. Feed Radials
4. Filtrate Weir & Flume
5. Reject Weir
6. Reject Flume
7. Central Compartment
8. Airlift pipe
9. Sand Washer Housing
10. Sand Cone
11. Ladder
12. Platform
13. Cover
14. Air Panel
304 SS
304 SS
304 SS
304 SS
Polypropylene
Reinforced Fiberglass
Reinforced Fiberglass
304 SS
Reinforced Fiberglass
304 SS
EPCS
EPCS
Reinforced Fiberglass
4X One per unit FRP
2.13.6 Sparging Air Supply (Parkson Package 4D)
Ingersoll-Rand, Duplex, lubricated, air-cooled, reciprocating compressor, Type 30,
Model 2-2475E5 equipped as follows:
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Two (2) Model 2475 Bare Air Compressors, lubricated, air-cooled, two-stage,
single acting reciprocating type, each featuring two (2) cast iron cylinders in a V -
configuration:
• First stage cylinder bore size: 4"
• Second stage second cylinder bore size: 2.5"
• All strokes size: 2.75"
• Heavy duty cast iron frame
• Dry type inlet filter silencer
• Stainless steel finger valves
• Non adjustable, single piece connecting rods
• Oil splash lubrication system
• Heavy duty modular iron crankshaft
• Protective, replaceable crankshaft bushing
• Balanced four -ring piston with rings
• Heavy duty, non adjustable long life, ball bearings
• Built-in air-cooled inter -cooler, featuring finned copper tubes to remove the
inter -stage heat of compression and inter -cooler safety valve
• Oil fill cap
• Low Oil Level Switch in a NEMA 4 enclosure
• Air cooled after -cooler, built-in, Model BG -50 sized for a 25° F approach
temperature
Drive system including the following components:
• Cast iron compressor flywheel that transmits power acts as a cooling fan,
• and smoothes out pulses
• V -belt drive complete including belt drive adjustment arrangement
• Motor (s) 5 horsepower, 460 Volts, 3 Phase, 60 Hertz, 1750 RPM, 184T
frame
• Totally Enclosed Fan Cooled, motor Class F insulation, motor efficiency of
85.5% and a 1.15 Service Factor.
• All wiring is NEMA 4 watertight
• Totally enclosed belt guard
• Heavy steel baseplate
All above components are mounted on a heavy steel frame which hangs a 120
gallon capacity, horizontal type Air Receiver, A.S.M.E. coded and labeled, National
Board approved rated for a maximum working pressure of 200 psi and tested to
300 psi.
This receiver shall be equipped with:
■ Pressure gauge
■ Safety valve
■ Automatic drain valve, programmable solenoid type (EDV2000)
■ Service valve
■ Sturdy receiver feet
■ Suitable interconnecting and control piping
The compressor controls operate in:
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• Automatic start/stop control. AS & S utilizes a pressure switch to start and
stop the motor over and adjustable pressure range. Usually 35 psi. The
pressure switch is in a NEMA 4 enclosure
• Ingersoll-Rand synthetic lubricant in the crankcase T-30 Select All Season
• Installation, operations, and parts manuals
• Non asbestos gasketing
NEMA 4 Combination Alternator Panel
• Fusible disconnects switches with fuses
• Alternating relay
• Starters with third leg overload protection and one each NO and NC contact
• Control Terminal Board
• Manual reset buttons
• Hour -meters
• HOA switches (hand/on/off/auto)
• Control voltage transformer
• Grounding lugs
• Pump "Running Lights"
Ingersoll-Rand Type 30 Model 2-2475E5 Performance
Horsepower
5 HP
(each motor)
Speed
1040
RPM
Piston displacement
20.8
CFM (each pump)
Minimum operating air pressure
50
PSIG
Normal operating air pressure
125
PSIG
Maximum operating air pressure
200
PSIG
Actual delivery
17.1
(each pump)
Brake -horsepower
4.8
(each pump)
Full Load Amps @ 460 volts
7.6
(each motor)
Note: 1. This Package is suitable for Indoor Installation
2. System allowable operating temperature
401 to 110° F
3. The above brake horsepower
-and performance figures include all
belt losses. Actual
delivery is
referred to 14.7 psia and inlet
temperature at the
compressor
intake and includes packaging
losses.
2.13.7 Dessicant Air Dryer Model TZM24
Compressed Air Flow
100% saturated compressed air enters the dryer via inlet 5/2 control valve V1
and is directed up through one of the snow storm filled desiccant columns
(depending on where in the cycle the cam timer is, this will be either Column A
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or Column B). During its flow, water vapor is adsorbed from the air. The
adsorption is based on the affinity of the desiccant material towards the water
vapor in the air. One of the outlet check valves V2 will be open and the other
closed (again depending on the cam timer position). This normally will be open
for 120 seconds and then closed for 120 seconds (continuous operation). This
continuous cycling is controlled by an electric cam timer.
Regeneration Air Flow
Simultaneously to drying the compressed air in one chamber, a limited amount
of dried air is passed from the dryer outlet and expanded to atmospheric
pressure through purge regulator V3. This regeneration air flows downwards
through the saturated desiccant of the other chamber. The expanded dry air
flows down through the chamber and regenerates the desiccant. The expanded
regeneration air containing the adsorbed moisture and is discharged through
5/2 control valve V1 and the exhaust valve silencer V4. After 90 seconds
exhaust valve V4 closes, the left chamber is pressurized through one of the
purge air regulators V3 and 30 seconds later (a total of 120 seconds) exhaust
valve V4 opens. The pressure in the right chamber is vented and 5/2 control
valve V1 is switched via a signal from the cam timer. V2 outlet check valve
switches as a result of the pressure difference between the two chambers. The
fully regenerated left chamber will now dry the saturated compressed air while
the right chamber is being regenerated.
TZM24 Air Drver Technical
Capacity: 24 CFM
Maximum Pressure: 150 PSIG
Voltage: 115 volt, 1 phase, 60 Hz
Compressor Horsepower: N/A
Running Current: .5 Amps
Pressure Dew Point: Class H -40F (based on 100 F inlet, 100 F ambient)
Sound Level: N/A
Inlet & Outlet Conn: 1/2"
Ingersoll Rand Pre -filter MODEL GP123
The general purpose coalescing filter is designed to remove liquids and solids
from compressed air and a flow rate of 123 cfm. The filter removes particles
down to 1 micron -liquids down to 0.5 mg/m3 W at 21° C. The initial dry
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
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pressure drop at rated flow will not exceed 1 psig, where as the initial wet
pressure drop will not exceed 3 psig.
The GP series is especially suited for applications such as protecting
instrumentation systems and gauging equipment, air bearings, advanced
pneumatics and in sophisticated process and electronic plants. The filter
utilizes the coalescing method for removing contaminants. The filter
elements are long lasting and easy to install. They are constructed of
multi -layered borosilicate microfibre media; lass filled Nylon end caps
and perforated stainless steel inner and outer support cores.
The housing is constructed of pressure die-cast aluminum. The filter has an
automatic drainage system for constant removal of contaminants. It also has a
differential pressure indicator visible from both sided for ease of installation.
The lift and twist mechanism made for easy element exchange. The durable
stainless steel element inner and outer cores withstand sudden pressure
surges of up to 100 psig. The element top end cap has an over molded seal
and patented tapered location that ensure a perfect seal.
Ingersoll Rand After -Filter MODEL HE123
The high efficiency filter is designed to remove liquids and solids from
compressed air. The filter removes particles down to 0.01 micron -liquids down
to 0.01 mg/m3 W at 21° C (0.01 PPM W at 70° F). The initial dry pressure drop
at rated inlet air pressure and rated flow will not exceed 1 psig, where as the
initial wet pressure drop will not exceed 3 psig.
The HE series is especially suited for applications such as protecting
instrumentation systems and gauging equipment, air bearings, advanced
pneumatics and in sophisticated process and electronic plants. The filter
utilizes the coalescing method for removing contaminants. The filter elements
are long lasting and easy to install. They are constructed of multi -layered
borosilicate micro fiber media; glass filled nylon end caps, and perforated
stainless steel inner and outer support cores.
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The housing is constructed of pressure die-cast aluminum. The filter has an
automatic drainage system for constant removal of contaminants. It also has a
differential pressure indicator visible from both sides for ease of installation.
The lift and twist mechanism makes for easy element exchange. The durable
stainless steel element inner and outer cores will withstand sudden pressure
surges of up to 100 psig. The element top end cap has an over molded seal
and patented tapered location that ensures a perfect seal.
All internal wiring and piping for the entire package is completed requiring only
customer air hookup, condensate discharge hookup and electrical in
connection. Bypasses are included on the dryer and the filter.
System Transformer
The package is complete with an externally mounted control voltage
transformer. The purpose of the transformer is to provide secondary power to
operate the dryer and condensate system. The transformer shall be NEMA 4
rated, dry type transformer with a primary voltage of 460 volts and a secondary
of 120 volts. The transformer shall be factory mounted and wired to the control
panel with watertight conduit. The transformer shall be a Micron Industries, 2
KVA rated.
System Piping
The complete package is pre -piped, the dryer and filter and by-pass system are
piped using high pressure, anodized aluminum, corrosion resistant air piping.
The fittings are high pressure, nickel plated, Parker fittings, both dryer and filter
are equipped with a 3 -valve by-pass, allowing the system to service with
shutting down the dryer and filter.
Centralized Condensate System
The package is complete with a pre -piped and pre -wired condensate system,
the drain lines form the dryer, filter and tank are all piping to one common area.
All lines are complete with a check valve to prevent moisture from back feeding
into the other components. The drain system is complete with a NEMA 4
programmable drain valve Model EDV2000. This drain valve is pre -mounted on
the system and factory set, it is fully adjustable for on time and drain intervals.
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Project No. 307308 29 The Cliffs at High Carolina

• One Alum Feed Pump Wallace & Tiernan Encore@ 700 metering pump solution
feed pump.
• 100 gallon fiberglass or plastic solution tank.
• Flocculation mixers — fine -bubble diffuser is provided in the influent chamber to
Anaerobic III. Provide 3 Model 375, Snap -Cap Plus 5 diffusers as manufactured
by Enviroquip® International, Inc. on 6 -inch center -to -center spacing on a 1-1/4
inch, Schedule 40 Stainless Steel header.
• Mixer and low solution level alarm.
2.15 Alkalinity Control
• One Soda Ash Feed Wallace & Tiernan Encore@ 700 metering pump solution feed
pump.
• 100 -gallon fiberglass or plastic solution tank.
• Mixer. and low solution level alarm.
2.16 Air and Gas Management
• Provide one Exhaust fan located above trickling filter III. (25 cfm exhaust, 0.5 hp,
120 volts.
• Provide one Aqueonic's brand Potassium Permanganate and activated carbon air
filter located above trickling filter III to use for air cleaning and odor removal in
exhaust gases.
• Provide one feed pump for KMnO4
• 100 -gallon fiberglass or plastic solution tank.
2.17 Building Construction
• Lumber - Pressure treated (0.4 lbs retention CCA) lumber.
• Fasteners — Galvanized fasteners approved for pressure -treated wood.
• Framing - "balloon" construction.
• Siding — Alcoa vinyl — color per Owners selection.
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Project No. 307308 30 The Cliffs at High Carolina

® Roofing — 225 lbs asphalt shingle.
• Insulation — insulate all exterior walls using fiberglass insulation 6 inches thick.
• Aerobic Towers — 0.50 inch thick reinforced Fiberglass interior wall lining for the
aerobic towers.
2.18 Ultraviolet Disinfection Equipment
For Phase I the supplier shall provide Trojan Technologies Inc. Model 3000PTP 3300K
in series (1 duty, 1 redundant), complete with UV modules, support rack, level control
weir, one monitoring system per bank, power distribution receptacles, one maintenance
rack, one operators kit, spare parts (3 lamps, 2 sleeves, 2 lamp holders), stainless steel
channel and transition boxes which is sufficient for both phases (200,000 gpd) of
treatment.
2.18.1 Design Requirements
The unit shall have dual channels, each capable of disinfecting an effluent with the
following limits:
A. Max Flow:
B. Total Suspended Solids:
C. Ultraviolet Transmittance at 253.7 nm
D. Annual Effluent Temperature Range:
E. Effluent Standards to be achieved:
100,000 GPD
5 mg/I
65%
36 to 86 ° F (2 to 30°C)
25 CFU /100ml one day max.
14 CFU / 100 ml monthly avg.
Fecal Coliforms, based as a monthly geometric mean of daily samples.
The manufacturer shall supply a description of the UV disinfection system complete
with number of lamps in each UV lamp module, number of UV lamp modules and
number of UV banks along with a submersible UV intensity sensor with display. The
UV units shall be fabricated in a stainless steel channel as shown on the plans.
The installed UV system (2 units) shall be able to continue providing disinfection while
cleaning or replacing UV lamps, quartz sleeves and ballasts.
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Project No. 307308 31 The Cliffs at High Carolina

Design- The ultraviolet disinfection system will be installed in per -cast concrete tanks
following the fixed media anaerobic reactors. These tanks shall be constructed with
4,500 -pounds per square inch, 28 -day compressive strength, Minimum wall thickness
shall be 4 -inches unless otherwise noted on the drawings.
The ultraviolet disinfection system shall be installed inside a fabricated stainless steel
type 304, 14 -gauge effluent channels (68 -inches long by 2.8 -inches wide by 14 inches
high).
All material in contact with effluent or UV light shall be stainless steel, quartz 214, or
Teflon. All wiring exposed to UV light shall be Teflon coated.
2.18.2 Ultraviolet Modules
Each module will consist of two UV lamps with their corresponding electronic ballast
in an aluminum enclosure mounted on a stainless steel type 316 frame. The
electrical wire connecting the lamps and ballasts will be enclosed in the stainless
steel frame and not exposed to the effluent. Each UV module shall be equipped with
a weatherproof cable and standard 120 -volt plug. Lamp status will be displayed on
top of each UV module by watertight LED indicator lights.
2.18.3 Monitoring System
Two submersible UV sensor will sense the UV intensity produced in each bank of UV
lamp modules. The UV intensity will be displayed in units of MW/CMA 2 on a
minimum 3 character display. Time elapsed will be displayed in hours on a minimum
4 character display. Both displays must be visible above the precast concrete tank.
The monitoring system shall display the lamp status, run time and UV output and is
enclosed in a fiberglass type 4X wall -mounted panel or approved equal.
2.18.4 UV Lamps
The lamps will be placed parallel to the effluent flow and evenly spaced in both
horizontal and vertical directions. The UV lamps shall be low-pressure mercury
slimlineTM lamps of the hot cathode, instant start design. The arc current will heat
the coiled filamentary cathodes. The lamps shall emit essentially monochromatic
light at a wavelength of 253.7nm to 273.7 nm. Each UV lamp sleeve shall be type
214 clear fused quartz circular tubing as manufactured by General Electric or
approved equal. Each lamp shall be guaranteed an operation life of 12,000 -hours or
more. Each lamp shall have an operating temperature between 95 to 122°F.
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2.18.5 UV Lamp Sleeves
The sleeves shall be circular tubing, with a nominal wall thickness of 1.0 to 2.0
millimeters, clear fused type 214 quartz or equal.
2.18.6 Ultraviolet Channel
The channel shall be equipped with a bottom drain and be stainless steel 304, 14 -
gauge or approved equal.
Each module shall be supported on a rack system. The outside dimensions of the
effluent channel shall not exceed 96 -inches in length or 18 -inches in width. Weirs
shall be installed to control the level of the effluent.
2.19 Sludge Holding & Thickening Chambers
Sludge Holding and sludge thickening are provided in separate process chambers.
Each phase shall provide one aerated sludge holding chamber having a capacity of
21,2563 gallons to received sludge from the primary clarifier and anaerobic reactor
units by means of timed airlift pumps. A single 20,225 -gallon sludge thickening
chamber for decanting supernatant from the conditioned sludge prior to off-site
disposal is provided to serve both phases.
Included in the sludge holding chamber is air for mixing and digestion at a rate
sufficient to keep the solids in suspension and maintain dissolved oxygen between one
and two mg/I. For minimum mixing and oxygen requirements, an air supply of 30 cfm
per 1,000 cubic feet of tank volume or 86 cfm. Provided to the sludge thickening is air
at the rate of 10 cfm @ 7 psi also provided by Blower Two.
As part of the air supply in the sludge processing are diffusers which shall be "Wide
Band" Stainless Steel diffusers in 304L stainless steel. The diffuser is made with cast
end caps welded all around. Deflectors shall be supplied with each diffuser but can be
removed. The coarse bubble diffuser is intended to be a clog -free design, with oxygen
transfer rates of 0.5 to 0.8% per foot of submergence (1.7 to 2.5% SOTS/m).
Suspend on 1-1/4 inch, Schedule 40 header. Design Flow: 10-40 SCFM (17-67
Nm3/hr) Flow Range: 0-50 SCFM (0-85 Nm3/hr).
The diffusers piping shall be mounted on a 1-1/4 inch Schedule 40 Stainless Steel
header. The diffuser assembly shall be suspended on a 1-1/4 inch, schedule 40
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & uaicuiations
Project No. 307308 33 The Cliffs at High Carolina

stainless steel supply pipe drops. Each supply pipe drop shall have an easily
accessible ball valve and unions to facilitate diffuser drop removal for maintenance and
service of the diffuser assembly and manually regulate the air supply to the diffusers.
Also provided on supernatant liquid decanting pump (Hydromatic Model SK50,
submersible, non -clog, 124 gpm @ 24' TDH, 1750 RPM, 0.5 horsepower pumps or
approved equal). Pump electrical characteristics shall be 115 volt, single phase. Also
provided is one Davit Crane, Portable Type, Capacity 500 Lb, manual pump lift.
2.20 Flow Meter
An ultrasonic microprocessor -based flow meter and recording chart shall be installed on
an interior wall of the Mechanical Building located adjacent to the plant in accordance
with the manufacturer's recommendation. A flume shall be installed in the ultraviolet
basin in accordance with the drawing.
The ultrasonic sensor will be mounted as shown in the drawings on the ceiling of the tank
using stainless steel fasteners to secure the sensor and cables. All cabling between the
sensor and flow meter shall be installed in non -corroding conduit. The rate of flow is
determined by reading the elevation of the discharge through the V -notch weir in the weir
box mounted at the outlet end of the tank. The box containing a flume shall be located at
least 6 inches above the invert of the effluent pipe to insure that the discharge side of the
flume is never flooded.
• Siemens Miltronics HydroRanger Model Ultrasonic open -channel flow meter similar or
engineer approved equal. Power —100/240 VAC, 50/60 HZ.,
• Siemens Miltronics Echomax Model XRS-5 Transducer or engineer approved equal.
• Recording Chart — Chessell Model 392 paper chart recorder with 4 universal inputs or
engineer approved equal.
• Power — 80/240 VAC, 50/60 HZ.
• Outputs — 4-20mA isolated into 1000 ohm, monitored to detect open circuits, with
RFI and gas discharge surge protection and two fuses.
• Data Logger — There shall be a data logger integral to the electronics and an
external paper logger. The data logger shall have a non-volatile flash memory with
storage capacity of least 32,000 records. Software shall be supplied for
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Project No. 307308
Wastewater Irrigation System Specifications & Calculations
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downloading the data. The logged data shall have the capability to be displayed
on the backlit in graphing from for daily minimum, maximum, average and total low
units for the past 16 days.
2.21 Telephone Service
Telephone service by other to the Sewage Treatment Plant shall be,six pair of twisted copper
wire, underground telephone service connected to a service panel in the office area of the
Building. Service shall be connected to the control panel of the Supervisory Monitoring
system and contain additional phone jackets to allow operators to connection regular
telephones for their use. Telephone outlet jacks shall be provided throughout the buildings
as shown on the drawings.
2.22 Wiring Code
Interior wiring of the Sewage Treatment Plant control panels shall be completely wired at the
factory and UL stamped. All wiring in the station shall meet the requirements of the local
electric utility, local code and the National Electric Code, and be marked and color -coded as
indicated on the wiring diagram. All wiring outside the panel shall be in conduit, except for the
120 -volt single-phase accessory items that are provided with connecting insulated service
cord. Power wiring outside the service -building install underground shall have conductors,
within the project limits, installed in conduit and covered with a minimum earth cover of 24
inches. A warning tape "Electric Line Buried Below" will be used above all electrical lines. All
wiring and connections in the basins and tanks of the plant shall be explosion proof
construction design. All exterior junction boxes shall be of NEMA 4X construction. All
electrical receptacles shall be protected with Ground Fault Interrupter devises.
2.23 Electrical Service
The service to the station is 120/240 volts, 4 -wire, 3 Phase power. Power will be supplied
underground to the building control center.
Provide one NEMA Class I control panel installed within the control enclosure of the plant.
This control panel shall include breakers and starters that are required to operate all
electrical equipment supplied by Aqueonics. Flexibility of operation will be provided by
PLC. In normal operation the status display will show which devices are on. If there is a
malfunction in the plant, the red alarm light will come on, the alarm will be transmitted on
the phone line, and the alarm signal in question will be indicated on the status display.
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2.25 Training, Operating Manuals and Electrical Drawings
The owner and operators shall be furnished complete and accurate operating instructions,
original equipment manufacturer operating manuals, and vendor drawings of approved
equipment and controls including control circuits and electrical ladder drawings.
Training in operation of the grinder, pump controls, motor/blowers, competent factory
representative shall provide pumps and emergency generator during final station plant
checkout, start-up and adjustments required for proper operation of the motors.
2.26 Plant Safety
Plant equipment and processes located outside the Plant Building shall be secured by a
fence consisting of a 7 -foot chain link fence topped with three strands of barbed wire. The
plant building shall be secured locking doors, and dusk to dawn lights located on the sides of
the building. Fence gates shall be provided hasps and padlocks. The Contractor shall
provide padlocks with common keys.
All rotating equipment will be provided guards meeting OSHA standards. The equipment
supplier will provide for local lockout on motor controls. Tank openings such as the flow
equalization tank shall be secured with aluminum hatches, or provided with both aluminum
handrails with kick plates, or fiberglass grating. All closures shall be rated at 300 lbs/sq. ft..
Grating shall be Fibergrate® unless otherwise specified on the drawings
2.27 Autodialer
The plant shall have a supervisory monitoring system and a local alarm system consisting of
a strobe light and bell. The automatic telephone dialer, alarm bell and red flashing strobe
signal shall be the means of detection when operation of the plant is in alarm conditions. The
major items in the supervisory monitoring unit include the following elements to support the
station:
Sensaphone Express II or engineer approved equal. Provide Part No. FGD -6700
(Sensaphone Express II), No. FGD -0035 (Input Card No. 2 which adds inputs 9 through
16), and all mounting and cabling.
The inputs to the Sensaphone shall be:
• Public Utility Electric Power failure
• Failure of Pumps or Blowers to start or operate
• High water levels in Flow Equalization Basin
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• Un -authorized entrance into Mechanical Building
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3.1 Design Criteria
The wastewater disposal system primary components consist of:
o dosing tank storing treated effluent.
o the irrigation system dosing pumps and irrigation controls and monitoring system
o piping system to and from the irrigation zones.
o manifolds and valving distributing irrigation effluent to the zones from the main
piping system.
o drip irrigation lines and emitters.
o Wet weather storage pond.
The system primary design parameters include:
o A maximum pump run time of 18 hrs/day for Phase II implementation, resulting in a
average dosing rate of each zone of approximately185 gpm or less.
o Minimum pipe flow velocities of 2 feet/second.
o Minimum field flushing of drip laterals of 2 feet/second.
o Pressure range at any given drip lateral/emitter of between 7 to 70 psi.
o Wet weather storage requirement of 9 days.
3.2 Irrigation Dosing & Control System
3.2.1 Dosing Tank
The dosing tank is a 30,000 gallon prestressed concrete tank supplied by the
treatment plant manufacturer and built to the same specifications as other below
ground treatment plant tankage. The tank shall meet or exceed the construction
specifications for pump tanks outlined in 15A NCAC 18A .1954.
3.2.2 Float Switches
Floats are to be set at the levels specified in the engineering plans prior to the final
inspection. Sealed mercury control floats or similar devices designed for detecting
liquid levels in pump tank effluent shall be provided to control pump cycles. A
separate level sensing device is provided to activate the high-water alarm. Float
switches are for high level alarm and low level shut-off only as dosing is based upon
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Project No. 307308
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a time -dose system. Pump -off level is set to keep the pump suction foot valves
submerged at all times or in accordance with the manufacturer's specifications. A
minimum of 18 inches of effluent is maintained in the bottom of the pump tank.
Switches are set to allow for varying irrigation cycles. If the tank level is in the Drip
Enable Zone, a dose/rest cycle will be implemented based upon the average daily
flow
3.2.3 WSI Pumping & Monitoring Skid
The pump & monitoring skid shall consist of the system controller (1), the filtration
package (2), the pumps (3), the flow meter (4) the pump master control valve (5) and
a quick -reacting pop-off pressure relief valve (6). All of the components listed shall
be pre -assembled on a skid for package installation and shall be pre -wired,
programmed and tested upon delivery.
The pump & monitoring skid unit shall be as supplied by Wastewater Systems Inc.
Model W130PC.
3.2.3.1 Pumps
A duplex skid mounted centrifugal pump system will dose the Phase I irrigation
system. A second duplex centrifugal booster pump station will be installed during the
Phase II addition to provide the additional TDH conditions required to dose the
Phase II irrigation system. The configuration of the skid, piping and controls shall be
provided to accommodate the addition of any required equipment for the future
Phase II addition.
The Phase I pumps are Paco Type LC Model 20953 (9.54" impellers) end suction
centrifugal with 40 HP close coupled motor drives. The design pump rate and TDH
conditions are established by the drip zone with the highest flow and head
conditions. Other zones have pressure regulating valves to maintain pressures
between 7 and 70 psi at all of the drip field emitters to allow for pressure
compensated flow. The pump system is designed to meet the discharge rate and
total dynamic head requirements of the Phase I effluent distribution system, with a
minimum required operational point of 200 gpm at 325' TDH. See the calculations in
Section 5.
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Project No. 307308
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The Phase II pumps are Berkeley Model B2TPMS (6-3/16" impellers) end suction
centrifugal with 10 HP close coupled motor drives. The design pump rate and TDH
conditions are established by the drip zone with the highest flow and head
conditions. Other zones have pressure regulating valves to maintain pressures
between 7 and 70 psi at all of the drip field emitters to allow for pressure
compensated flow. The pump system is designed to meet the discharge rate and
total dynamic head requirements of the Phase I and Phase II effluent distribution
system, with a minimum required operational point of 200 gpm at 452' TDH. See the
calculations in Section 5.
The pump system has been designed in accordance with 15A NCAC 18A .1952(c).
Pumps shall be listed by the Underwriters Laboratory or equivalent third party
electrical testing and listing agency. The suction lines shall have check valves to
keep the lines full.
3.2.3.2 Controls
The programmable controlling (PC) system of the irrigation system is by Waste
Water Systems, Inc. and incorporates numerous safety features and control
mechanisms and is designed to allow the irrigation zones to be dosed according to
the irrigation schedule. The controller actuates the pumping system and remote
zone valves in accordance to the dose/rest cycle presented. Features include:
♦ The ability for the operator to field modify the dose/rest cycle
parameters.
♦ The ability to monitor dose flow to the irrigation fields and detect a
minimum (+/-) 5% variance in the established flow rate of each
independent irrigation zone. If dose flow is outside of the
established tolerance, that zone shall be eliminated from the
irrigation schedule and the operator shall be notified of the
condition.
♦ The ability to delay the dose schedule in the event of rainfall, with an
input from the rain gauge.
♦ The ability to "dose" the wet weather storage pond in a high water
F-1 level event in the storage tank.
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Project No. 307308
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Wastewater Irrigation System Specifications & Calculations
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The PC operations are provided in the Operations & Maintenance Manual.
The PC system features an industrial flat touch color screen panel with the
following features. The controller is an OPTO22 configuration. The input/output
(1/0) cards and all the electrical control components shall be located in a NEMA -4X
enclosure. Pump and control circuits shall be provided with manual circuit
disconnects within a watertight, corrosion -resistant, enclosure (NEMA 4X or
equivalent) adjacent to the pump skid, securely mounted at least 12 inches above
the finished grade. The control panel must be in a watertight, corrosion -resistant
enclosure (NEMA 4X or equivalent) unless installed within a weather -tight building.
The panel shall be protected from intense solar heating. The pump(s) is/are
manually operable without requiring the use of special tools or entrance into the
tank for testing purposes. Conductors shall be conveyed to the disconnect
enclosure through waterproof, gas -proof, and corrosion -resistant conduits, with no
splices or junction boxes provided inside the tank or riser. Wire grips, duct seal, or
other suitable material is used to seal around wire and wire conduit openings inside
the pump tank and disconnect enclosure.
3.2.3.3 Disc Filtration
Automatic Filter Assembly
1. The automatic filter shall be a package assembly filter battery
consisting of inlet and outlet manifold headers, three (3) disc filter
bodies, automatic back flush valves and controls on a pre -
assembled header and frame. The inlet and outlet manifolds shall
be Schedule 40 stainless steel 316 with flanged connections. The
filter bodies shall be aluminum. The filter back -wash valves shall be
4 -inch cast iron valves, epoxy coated with "high pressure" NC
solenoid bodies.
2. Filters shall be hydraulically operated by pressure and electrically
actuated by the computer controller. The filter assembly shall be
equipped with fifteen (15) two-inch, 140 mesh disc filter elements
and shall be capable of filtering 200 GPM at a maximum operating
pressure of 200 psi.
3. Filter battery shall have the following features:
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & caicutauons
The Cliffs at High Carolina
Project No. 307308 41

a.
f
inlet/outlet diameter
4 inch
b.
end connections
3" flanged
C.
minimum pressure
40 PSI
d.
maximum pressure
200 PSI
e.
maximum recommended flow rate
375 GPM
h.
minimum backflushing flow rate
175 GPM
fl h'
220 Gallons
L amount of water used a us sng
j. filter rings 140 mesh -100 micron
k. head loss 1.0 PSI at 200 GPM
3.2.3.4 Flow Monitoring
The effluent flow meter shall be a velocity propeller type, magnetic drive, sealed
housing, flanged tube meter rated for 300 psi working pressure. It shall comply with
the applicable provisions of AWWA C704. The meter shall be a 4 -inch flanged meter
with a sealed indicator having a range of 50 to 500 and shall be equipped with a six
digit Indicator -Totalizer -Transmitter reading in units of U.S. gallons and shall be
accurate within +/- 2% of true flow. The meter shall have a GPM indicator hand and
a sweep test hand. The transmitter shall utilize a durable magnetically actuated reed
switch with an output pulse rate of 150 contacts per minute at the maximum flow
rate. A two -lead shielded cable must be furnished with the transmitter. The meter
shall be as supplied by Waste Water Systems.
3.2.3.5 Master Control Valve
The pump master control valve shall be a double -chambered, diaphragm actuated
hydraulic globe valve with a removable integral actuator. The valve shall be a
standard oblique (Y) pattern and equipped with electrical actuation from the
computer control system. The valve body and cover shall be ductile iron EN 1563
meeting ASTM A-536 with a fusion bonded epoxy coating. The valve shall be 4 -inch,
flanged (ANSI B-16.42), Class 150 having a 250 psi working pressure. The valve
shall be as supplied by Waste Water Systems.
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3.2.3.6 Pressure Relief Valve
The pump station skid shall be equipped with a pressure relief valve to protect the
pump station components and piping system from over pressurization. The valve
shall be a quick -reacting, direct -sealing diaphragm valve activated by line pressure
and controlled by an adjustable pilot. When the network pressure exceeds the pilot
set point of the valve, the valve shall instantly become fully open and shall slowly
close when the network pressure decreases below the set point. The valve shall be
a bronze angle valve and pilot. The pilot spring range shall be 115 — 360 psi. The
relief valve shall be as supplied by Waste Water Systems.
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Project No. 307308
Wastewater Irrigation System Specifications 6, caicutations
43 The Cliffs at High Carolina

3.3 Irrigation Distribution System
The irrigation distribution consists of the supply piping, manifolds, valving distribution lines,
drip tubing, return lines, return manifolds and return mains.
3.3.1 Supply Line Force Mains
Pipe and fittings must be of a size.and material as depicted on the engineering
drawings. All lines 3" in diameter or greater must have mechanical mechanically
fastened joints (MegalugTM or equivalent) capable of withsanding pressures in
excess of 225 psi. Lines less than 3" in diameter may have glued joints.
3.3.1.1 Installation
Bedding and installation shall be consistent with ASTM Standard D 2774. Three (3)
feet minimum cover shall be provided for all force mains unless ferrous material pipe
is specified. Ferrous material pipe, or other pipe with proper bedding to develop
design supporting strength, shall be provided where sewers are subject to traffic
bearing loads. Additional protection shall be provided for sewers that cannot be
placed at a depth sufficient to prevent damage.
3.3.1.2 Steep Slope Installation:
Sewers on 20 percent slopes or greater shall be anchored securely with concrete, or
equal, with the anchors spaced as follows:
a. Not greater than 36 feet center to center on grades 21 % to 35%;
b. Not greater than 24 feet center to center on grades 35% to 50%; and
c. Not greater than 16 feet center to center on grades 50% and over.
No anchors are required on lines less than 2 inches in diameter.
Thrust blocks shall be utilized on all force main fittings where the design velocities in
the pipe are projected to be greater than 15 feet per second. The location and sizing
of the thrust blocks are shown on the engineering drawings.
3.3.1.3 Testing
All pressure lines shall be either hydrostatically or pneumatically tested. No testing
shall be performed until at least two days after all pipe connections have been made.
Pneumatic testing shall be in accordance with ASTM C828.
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For hydraulic testing, the testing system shall have the ability to pressurize and seal
the line on both ends and have pressure readings on both ends of the installed
system. Testing procedures shall consist of pressurizing the distribution system with
water with pressure equivalent to the capacity of the specified pump. Once the line
has been sealed and the pressure equilibrated, the system shall be inspected for
leaks. The pressure shall be maintained for two hours with a pressure drop of less
than 2 psig.
3.3.1.4 Trenching
Trench excavation shall conform to the line, depth and dimensions shown on the
plans or as directed by the Designer. The trench shall be properly braced and
shored so that workmen may work safely and efficiently. If unstable conditions are
encountered, the Designer shall be notified in order that proper bedding materials
may be selected. Trench excavation or excavation for pipelines shall consist of
excavation necessary for the construction of sewers, conduits and other pipelines
and all appurtenant facilities thereof, pipe embedment materials, and pipe protection,
insulating and sleeving in ductile iron pipe, as called for on the plans. It shall include
site preparation, backfilling and tamping of pipe trenches and around tanks and the
disposal of waste materials, all of which shall conform to the applicable provisions of
these specifications. When MUCK, gUICKSana, soli clay, Swampy ui uti iCi 11IoLVI iai
unsuitable for foundations or subgrade are encountered which extend beyond the
limits of the excavation, such material shall be removed and replaced with pipe
foundation material as specified in the engineering drawings. Surface drainage shall
not be allowed to enter excavated areas
3.3.1.5 Rock in Pipe Trenches
Rock encountered in trench excavation shall be removed for the overall width of
trench which shall be as shown on the plans. It shall be removed to a minimum depth
of three (3) inches below the bottom of the pipe. Clean compacted backfill shall
replace the excavated rock.
3.3.1,6 Pipe Installation
The pipe material listed above shall be installed in accordance with the
manufacturer's recommendations and the requirements of these specifications. All
sewer lines shall be laid to the line and grade shown on the plans. No deviations
from line and grade shall be made, unless they have been approved by the
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Project No. 307308
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Wastewater Irrigation System Specifications & calculations
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Designer. The pipe interior shall be kept clean before and after laying by means
approved by the Engineer. Pipe ends shall be plugged at the end of each work day
or when work is temporarily stopped. The plugs shall be watertight so that water and
debris will not enter the pipe.
3.3.1.7 Backfilling
(a) All backfilling shall be done in such manner as will not disturb or injure the pipe or
structure over or against which it is being placed. Any pipe or structure injured,
damaged or moved from its proper line or grade during backfilling operations shall be
opened up and repaired and then re -backfilled as herein specified.
(b) The Contractor shall replace all surface materials and shall restore paving,
curbing, sidewalks, gutters, shrubbery, fences, sod, and other surfaces disturbed, to
a condition equal to that before the work began, furnishing all labor and materials
incidental thereto as provided elsewhere in these specifications. The backfilling of
the trench after the pipe installation and testing shall be in accordance with the
standard detail.
3.3.2 Distribution & Return Lines
The distribution and return lines are the lines connecting the top -feed manifolds to
the drip tubing. The lines are design to drain after each dose event, so burial depth
can be shallower than typical force mains. An approximate 6" to 12 " burial depth is
sufficient. The lines are constructed of schedule 40 flex PVC tubing sized as shown
on the engineering plans, with Perc-rite connections to the drip tubing as supplied by
the drip tubing manufacturer. Piping shall be supplied by Wastewater Systems, Inc.
3.3.3 Manifold & Valving
Top -feed supply and return manifolds are utilized as depicted in the engineering
plans. Supply & return manifolds are specified in the plans and shall be constructed
of the pipe type and size as shown on the engineering drawings and per details
provided. Manifolds may be buried or surface mounted. The manifold must be
installed with sufficient elevation as to allow for drainage to the distribution lines and
drip tubing upon depressurization.
Brooks Engineering Associates, PA
Project No. 307308 46
Wastewater Irrigation System Specifications & caicuianons
The Cliffs at High Carolina

All valves shall be properly sized to meet flow and friction loss specifications.
Control valves shall be a double -chambered, diaphragm actuated hydraulic globe
valve with a removable integral actuator and equipped with electrical actuation from
the computer control system. The valve shall be a standard oblique (Y) pattern. The
valve body shall be brass with plastic actuator. The valve shall be threaded (NPT)
having a working pressure range of 10 —150 psi. Valves shall prevent backflow
while offering full flow performance with a minimum of turbulence or pressure loss
and must be rated for 150 psi W.O.G. (working pressure non -shock). The Check
Valves shall be as supplied by Waste Water Systems.
Pressure regulating valves shall be installed at locations as specified in the contract
documents and drawings. The valve body shall be brass with NPT inlet and outlet
and shall provide instant response to variations in pressure and ensure the outlet
pressure remain constant regardless of the inlet pressure. Regulating units shall be
plastic body with EDPM diaphragms and stainless steel springs. Valve sizing and
pressure set points shall be in accordance with the Contract Documents. Valves
shall be as supplied by Waste Water Systems, Inc.
Air and vacuum relief valves shall be installed at the high -points of irrigation header
lines, where shown on the drawings or as required. Valves shall be 2" diameter
combined air release valve which operates to release or admit air from or into the
lines. Valves shall be high strength plastic with operating parts of non corrosive
materials and be suitable for working pressure in the lines. The Air and Vacuum
Relief Valves shall be Guardian as supplied by Waste Water Systems.
All electrical wiring from the computer/controller to the automatic solenoid valves
shall be furnished by the system supplier. The electrical cables shall be U.L. listed
suitable for direct burial.
Brooks Engineering Associates, PA
Project No. 307308
47
Wastewater Irrigation System Specifications & Calculations
The Cliffs at High Carolina

3.3.4 Drip Lines
All dripper line shall be 0.75 -inch diameter nominal O.D. polyethylene tubing with a
pressure compensating mechanism allowing a constant discharge rate from each
dripper opening. Inside diameter shall not be less than 0.69 -inch. Dripper line
discharge rate per opening shall be 0.62 gallons per hour. Dripper line emitter
spacing shall be 24 -inch on center. Dripper compensating mechanism shall be
activated at 7 psi and maintain a uniform flow rate over a pressure range of 7 — 70
psi. Dripper diaphragm shall be constructed of synthetic elastomer to withstand the
effects of chemicals and acids (to pH of 2). Diaphragm shall have a self-cleaning
feature which continuously measures the actual flow rate, particles that could clog
the drippers create back pressure and push back the diaphragm to continuously
clean and flush particles from the regulating chamber of the diaphragm. Drip tubing
shall be installed where indicated on the drawings and should be installed and
connected according to manufacturers requirements with approved water tight
connectors.
The dripper line shall be BioLine® as supplied by Waste Water Systems, Inc.
3.4 Wet Weather Storage Pond
3.4.1 Design
The water balance conducted in accordance with NCAC 2T .0504(k) predicted that
no long term storage (30 days or more) is required with the specified irrigation rate.
However, short term storage must be provided to store influent wastewater during
wet weather and/or freezing events. The number of days of storage needed is
calculated based upon 37 years historical rainfall and freezing weather data. The
data is provided in Section 6.2. Daily rainfall and sign temperatures were
researched and analyzed; every day with over 1/2" of rainfall and a high temperature
of less than 32° F, it is assumed that the entire daily design flow is held in storage.
That stored volume is then integrated into the irrigation cycle the next day, as long as
weather conditions allow, creating a cycle of stored/relieved water volumes. The
cumulative effect of this cycle is that 6 days of storage is needed. BEA has applied a
safety factor of 1.5 and provided 9 days of storage, or 1.8 million gallons of effective
storage. The pond is to be graded according to the engineering plans to insure
sufficient effective volume.
Brooks Engineering Associates, PA
Project No. 307308
Wastewater Irrigation System Specifications 6, Galcuiations
48 The Cliffs at High Carolina

3.4.2 Wet Weather Monitoring
Wet weather monitoring is to by a Rainbird TMRanifall and Wind Speed Sensor. The
tipping bucket identifies rainfall events and disrupts the dosing cycle of the irrigation
fields. Treated effluent is allowed to store in the dose tank during this interruption
period. Should the water level in the dose tank reach a high level condition, WSI PC
monitoring system doses the storage pond until high level switch is deactivated.
Water can also be transferred to the storage pond by operating the pump and control
valving in hand mode.
3.4.3 Transfer to/from Pond
The stored, treated effluent is re -directed from the irrigation dose tank into the
storage pond via the normal irrigation distribution system. The pond is integrated in
the same fashion as an irrigation zone off of the distribution system, but not included
in the regular irrigation schedule. Flow to the pond is controlled by actuating a
remote zone valve of the same specification as any irrigation zone.
The return of stored effluent is via the drip zone flushing return line. As there is
adequate elevation head to pressurize the return line, a remote zone valve of the
same specifications as utilized on the manifolds is actuated to relieve the stored
effluent from the pond. The flow must be restricted manually at the treatment plant
via a mechanical valve located outside of the plant prior to a wye connection in to the
collection system main prior to entry in to the equalization basin.
3.4.4 Pond Liner
The Hydrogeological Report states that an inhibitive liner with a conductivity of 10"6
cm/s is required to prohibit the mounding and mixing of groundwater with stored
effluent. A clay soil material with >50% clay material and conductivity of less than
10"6 cm/sec can be installed in a one foot thick layer. Sampling and testing of the
clay material should be conducted every 50 cu.yds, to insure the material is to
specification. An alternative to a natural soil liner type of liner is an ESS -13
application. ESS -13 is a non-toxic polymer emulsion that provides a pond seal by
reducing the hydraulic conductivity of soils beyond their natural capability by filling
voids in the soil and by chemically and electrically modifying the alignment of the clay
platelets in the soil. It can.be applied by mixing into the liner material prior to filling or
by applying to the surface of pond after it has been filled. Cut -sheets are provided in
Attachment F.
Brooks Engineering Associates, PA
Project No. 307308
Wastewater irrigation System Specifications & uaicuianons
49 The Cliffs at High Carolina

4. 0 SITE PREPARA TIOJ
4.1 Clearing & Grubbing
The irrigation areas are to be as undisturbed as possible during all demolition and site
clearing activities. Minor clearing and grubbing is allowed for access during site and soil
investigations. It is preferable that clearing and grubbing be performed by hand and not
heavy machinery. It is desirable to leave soil compaction in a natural state. During
clearing and grubbing, no more than an inch of topsoil may be removed. Minimize root
excavation. No fill dirt maybe placed on top of drainfield or repair areas, unless specified
in the permit.
4.2 Seeding & Mulching
Fertilizing, seeding, and mulching of disturbed areas shall be completed within ten (10)
working days following completion of system installation and final inspection of the system
by the project engineer or designer. This may require that a temporary seeding mixture be
used during given dates of the year when permanent seeding would not be allowed. Said
temporary seeding for compliance shall be replaced by permanent seeding during allowed
seeding dates. Mulching shall be straw as specified herein.
Typical Seed Application Rates
Species: Rate (Ib/acre)
Falcon Fescue: 175
Rebel Fescue: 175
Jaguar Fescue: 175
Biltmore Mix: 100
Apply 4,000 - 5,000 Ib/acre grain straw or equivalent cover of another suitable
mulching material.
Brooks Engineering Associates, PA
Project No, 307308
Wastewater Irrigation System Specifications & Calculations
80 The Cliffs at High Carolina

IF—
4.2.1 Jute, Excelsior or Mulching
All seeded areas shall be mulched. Grain straw may be used as mulch at any time
of the year. If permission to use material other than grain straw is requested by the
Contractor and the use of such material is approved by the Engineer, the seasonal
limitations, the methods and rates of application, the type of binding material, or
other conditions governing the use of such material will be established by the
Engineer at the time of approval.
Applying Mulch
(1) Mulch shall be applied within 24 hours after completion of seeding unless
otherwise permitted by the Engineer. Care shall be exercised to prevent
displacement of soil or seed or other damage to the seeded area during the
mulching operations.
(2) Mulch shall be uniformly spread by hand or by approved mechanical spreaders
or blowers which will provide an acceptable application. An acceptable application
will be that which will allow some sunlight to penetrate and air to circulate but also
partially shade the ground, reduce erosion, and conserve soil moisture.
(3) Straw mulch shall be applied at the rate of not less than 2 tons per acre.
4.2.2 Maintenance of Seed and Mulching
Areas where seeding and mulching have been performed shall be maintained in a
satisfactory condition until final acceptance of the project.
4.2.3 Erosion Control
(a) During the construction of the project, the Contractor shall be required to take
the necessary steps to minimize soil erosion and siltation of rivers, streams, lakes
and property. The Contractor shall comply with the applicable regulations of the
appropriate governmental agencies in regard to soil erosion control and
sedimentation prevention.
(b) The Owner will limit the area over which clearing and grubbing and excavation
operations are performed.
(c) Prior to the end of each work day, on the project, the Contractor shall take the
necessary measures to protect the construction area from erosion.
(d) Temporary and permanent erosion control measures shall be accomplished at
the earliest practicable time. Temporary erosion control measures shall be
Brooks Engineering Associates, PA wastewater Irrigation System Specifications & Calculations
Project No. 307308 51 The Cliffs at High Carolina

coordinated with permanent measures to ii
continuous erosion control during the life c
(e) Temporary erosion control measures s
use of temporary berms, dams, dikes, drai
vegetation, mulches, mats, netting or any
necessary.
(f) Erosion control measures installed by
maintained by the Contractor, until the si
(g) Where excavation is adjacent to stre,
Contractor shall not place excavated ma
re economical effective and
the project.
all include, but are not be limited to the
age ditches, silt ditches, silt fences,
:her methods or devices that are
e Contractor shall be suitably
is fully stabilized.
s, lakes or other surface waters, the
-ials between the excavation and the
surface waters.
(h) Where live streams are crossed by theproject, the Contractor shall exercise
particular care to minimize siltation of the stream. Temporary erosion control
measures shall be constructed. These mai include but not be limited to use of
coffer dam in the stream, dikes, diversion ditches and/or temporary sediment traps
at the top of the banks, and silt fences on all creek banks. All temporary erosion
control measures shall be acceptably mai ntained until permanent erosion control
measures are established.
(i) Where runoff on natural ground may cause erosion of the trench or erosion of
the backfill in the trench, the Contractors all construct temporary erosion control
measures. These may include but not be limited to diversion ditches, check dams
and silt basins or other suitable erosion control measures.
(j) Permanent seeding of disturbed areas shall be accomplished at the earliest
practicable time.
(k) Gravel construction entrances shall bE installed at all locations used regularly
as ingress and egress to the project site.
(1) Stream and River Crossings
Diversion ditches shall be constructed at r near the top of each river bank at river
crossings. Localized stormwater runoff shall be diverted by way of the diversion
ditches away from the disturbed stream bank. Other specified erosion control
material shall be used in ditches and sw les.
F
IJ
Brooks Engineering Associates, PA
Project No. 307308
_J
Wastewater Irrigation System Specifications a Caicuianons
52 The Cliffs at High Carolina

5.0 • ' AND MONITORING
5.1 Pre -Construction Meeting
A pre -construction meeting shall be scheduled which shall include the contractor, the
NCDENR DWQ representative, the engineer or his representative, the system(s)
manufacturer representative and the certified operator. Scheduling this meeting shall be
the responsibility of the installation contractor and all parties shall receive a minimum of
one week's notice prior to the meeting date scheduled. Any changes to the plans
requested by the contractor or DWQ representative will be discussed at this meeting and
responded to within 3 working days by the engineer.
5.2 Intermediate Inspection of the System During Construction
The contractor shall notify the engineer in time to inspect the site and insure proper
installation of the system components prior to backfilling.
5.3 Final Inspection & System Start -Up
A copy of the engineer's Inspection Form shall be provided at the pre -construction
meeting. This document shall be utilized during final system inspection and start-up.
5.3.1 Start-up Procedures
Start-up testing shall be required for all electrical and pressurized components of the
on-site wastewater system. Testing of all components to insure operation in
accordance with intended function shall be checked and recorded. Potable water
shall be utilized for all system testing.
Brooks Engineering Associates, PA
Project No. 307308
Wastewater Irrigation System Specifications & uaicuianons
53 The Cliffs at High Carolina

5.3.2 Pumps and Controls
Potable water shall be introduced into the pump tank sufficient to activate (either by
float switches or time -dose) the pumping system for 2 on/off dosing cycles. The
dosing volume shall be estimated by checking tank levels before and after each
dose cycle. Pump run-times and estimated dose volumes shall be recorded for
review by the project engineer. If alternating drainfields are utilized, pump
sequencing should be checked. Electrical system components shall be approved
by the local building inspector.
5.3.3 Pressure Distribution
Dynamic pressure shall be checked at manifolds and (if present) pressure
distribution laterals. Pressures shall meet specified engineering requirements. See
the attached project calculations for the particular requirements for this project.
Pressure testing devices shall be installed as shown on the engineering drawings.
Brooks Engineering Associates, PA Wastewater Irrigation System Specifications & Calculations
Project No. 307308 54 The Cliffs at High Carolina

BEA Project # 307808
The Cliffs at High Carolina
Design Flow Calculations
Phase I Design Flow: 95,910
Phase II Design Flow: 103,780
Total Design Flow: 199,690 gpd
Phase I Buildings Floors I units/floor I br/unit flow/br
81 31 5 2 120 28,800 gpd
Site 2Buildings
Phase 1
10
Floors units1floor I br/unit I flow/br
2 5 2
120
24,000
gpd
Site 3
Phase 1 Inn bedrooms flow/br
48 120 5,760
I Restaurant seats flow/seat120
VgpdPhase
40 4,800Phase
1 Market Area (sq. ft gal/ 1000 sq. ft
9000 100 900
Phase I Banquet seats flow/seat
60 301 1,800 g d
Phase 1 S a Square Ft Flow/ 100 sq. ft
10,000 50 5,000 gpd
Site 5
Phase I Village Wellness and Pool I Sq. Ft Flow/ 100 sq. ft
8,0001 50 4,000 gpd
Site 7
Phase I Clubhouse Sq. Ft I
Flow/ 100 sq. ft
15,0001
50
7,500
g d
Site 9
Phase 1
I Strauss Lake SF units br/unit
flow/br
16 31
1201
5,760
gpd
Site 10
Phase l
Practice Golf SF1
units
br/unit
flow/br
8 4 120 3,840 gpd
Phase I
Golf Maintenance
ISgr Ft
Flow/ 100 sq. ft
7,5001
501
1 3,750
1 gpd
Site 4
Phase H Village Wellness and Pool
Sq. Ft
5,000
Flow/ 100 sq. ft
50
2,500
gpd
6
Site site bass
Phase 11 Buildings I units/bldg br/unit flow/br
141
8
Site Site 81
Phase 11
units br/unit
421 41
flow/br
1201 20,160
gpd
Site 11
Phase 11 Clubhouse Cottage SF
I
units
br/unit
I flow/br
241
41 1201
11,520
gpd
1:m
12
Phase 11 SFe Lots SF
units I br/unit
40
flow/br
4 120
19,200 gpd
Site 14
Phase 1l I Village Lake OverlookBuildings units
br/unit flow/br
,qnl en nen 1 —4
Prepared by: Matthew Rice Brooks Engineering Associates, PA 10/21/2008

6.2 WWTP Head Calculations and Process Calculations
Supporting Charts
--,
�_J

II. WWTP PROCESS CALCULATIONS
A.— Sludge Processing
Influent = 100,000 gpd @ 350 mg/l BOD, = 2921bs/day of BOD.
Process Sludge Production
0 0.15 lb/lb x 292 lb/day = 44 lbs/day at 4-1/2% solids.
o Gallons per day = 44 lbs/day/(8.34 lb/gal x.045) = 115 gallons/day.
Primary Tank Sludge Production
o Suspended solids = 210 lbs/day.
0 60% removed in primary clarification as primary sludge.
o Primary Sludge = 0.60 x 210 lb/day = 126 lbs/day at 2.5%
o Sludge volume = 126 lb/day/(8.34 gal/lb x.025) = 606 gallons per day of primary sludge.
Total sludge Production
o Daily sludge production= 606 gal. + 115 gal.= 721 gpd
Aerobic Sludge Processing
o Sludge stabilized under aeration = 15 days,
o Concentrated in the sludge conditioning chamber yield = 7-1/2% solids
o Production of sludge for off-site disposal = 350 gallons per day
o Sludge Storage Days Available = 21,263 gallons/350 gpd = 60 days.
Air Requirements
Mixing Air Required = 3 cfm/If x 261f of chamber = 78 cfm
Aerobic Digestion = Oxygen requirements, = 30 cfm per 1,000 cubic feet of tank. 21,263
gallons /7.48 gal/cu.ft. = 2,843 cu.ft.
2,843/1000 = 2.843 thousand cu. ft. of tank
2.84 x 30 cfm = 86 cfm-
Aw
SPECIFIC BLOWER REQUIREMENTS
!" Blower No 1 – Flow Equalization & Intermittent Airlift
Flow Equalization = 78 cfm @ max 7 psi
Airlift Pumps (2 max at a time) = 30 cfm @ 7 psi
Required = 108 cfm @ max 7 psi
Provided = 112 cftn @ 7 psi
p. 3

FIGURE 4-7
EFFECT OF ORGANIC LOAD ON NITRIFICATION- EFFICIENCY
u
cs
rt
EFFECT OF ORGANICIOAD ON NITRIFICATION-EFFICIEWY
OF ROCK TRIMLING IqVrW
0 . PO 30 40 50
RODS LOAD L811000 CU FTIDAY
E -M

VC — 5.0-477-1 BFGoodrich Information Bulletin
OFGoadrich
General Products Division
DESIGN CALCULATION RESULTS
TREATABILITY FACTOR K20 =0 07
influent Waste Temperature - 4000
INFORMATION
BULLETIN
wo spoirl Main Slfc-o
Akron Ghia 44318
DePcOmeml 0414, WHB•3
VINYL CORE'.
influOnt Waste Temperature -13° C
% BOD Removect
Media Depth
Raw F
w Expressed =F —GPM? of Surface Area
Feet0.8
Feet
U
().,5
0.-6
OJ
0-6
0.9
-Tower
1
1,2
13
1.4
1.b
............
12
766
57
54,
61
49
47,
--
45 43
—4-7
42
41
40
39
I . 14 —
— 72.
63
.59
-
56
64
52
50 48
60
46
44
43
16
67
80 72
84 75
(64:.
68.
72
61
69
59
57
135,
55- 53
63 61,
52
60 .--
50
54
58
49
53
57
48
52
56
18
20
66-
6�8
63
rb -
62
-6 5
61 --
6T
59
63
70
68
6b 65
63
62
60
59
7B
89
91
81 ..........
B4
1
76 9
76
72
74
70 6,8
774 2 71
66
69
65
68
63
65
62
65
24
—26
8
—g-2-86
75
74
81
79
77
75 73
72
--84 -
86
84
82
30
93
--83
86
85
83
81
79
W 77 76
'M
f—�
72
70
—3294
85
89
87
85
83
81
36
7
75
74
73
—
34
95
91
89—
87—
85
83
81 80
79
77
76
7 5
91
—
89
88
87
85
4.83
84
82
80
79
78
77
36
95
92
go
88
86
�8 5
133
93
91
go
88
86
85 83
82
81
80
79
8895
8B
86 85
84
82
81
80
influOnt Waste Temperature -13° C
% BOD Removed
Media Depth
Raw F12,w Expresser inCPM/ft, cif
Tower Surface Area
Feet0.8
4, 03
U
016
UJ
0.9
jo,
1.1
1,2
1.3
1.4
1.5
—
12
0
75
61
57
55
52
So
56
46
47
45
44
49
43
—4 8
42
47
14
— -- ----
-
84
75
68
72
65
63
67
60
59,
63
67
61
55
0
6 -
54
58
--
62
57
51
55
18
8779
89-82
76
79
73
76
—6,5
71
74—
B9
72
67
70.
66-
6�8
63
rb -
62
-6 5
61 --
6T
59
63
20
22
24
91
85
�j-79
8
a2
—77--7—.5,
7B
76
72-
74
70
73
696_7--'-66
_
71
70
69
26
28
94
89
86
X80
8,2
80
--
7g---.---77.-
75
74
73
72
§5
4(0) 88
--84 -
86
84
82
81
79
1
78
80
76
797
75
74
32
34
95
:JT
93
91
89
88
86
85
63
q�
78
36
95
94
rat
91
89
88
89
86
88
85
86
84
85
82
84
81
80
B2
40
95
95
94 23
91
go
89
88
87
85
4.83
84
83
—

FIGURE 5-12 VOLUME DENITRIFICATION RATE
9 W
FIGURE, 5-13
VOLUME DENITRIFICATION RATE FOR StIVERGED
lflr,H POROSITY FINE MEDIA COLUMNS (REFERENCE 39)
160C
120(
out
lu TO f- v
TEMPERATURE, C
40
out
lu TO f- v
TEMPERATURE, C

2.3 Pump curve for irrigation dose pumps and pump curve for
pumps

Berkeley 10 HP
Flow (gpm, Head (FT)
1
154
100
153
125
151
150
149
175
145
200
140
225
134
250
124
Paco 40 HP
Flow (gpm, Head (FT)
1
360
100
360
125
358
150
356
175
354
200
350
225
345
250
340
Both Pumps in Series
Flow (gpm, Head (FT)
1
514
100
513
125
509
150
505
175
499
200
490
225
479
250
464

YANC

'9/16/2008 12:21pm
WS1 7702766535 #439 Page 11/12
Oft AM Aft
ir"Cull,
RUMPS
LC - 20953 Configured Curve
_.._.i..._. .....
By, TGJ
Date: 10/9/2008
Rev. 4
jProject: Waste Water Systems
Tag A P-1 P-2
P.O.
'Location:
Model: 20953
Cust ReN
,Contractor:
Qty: 2
LentlRep; SPE
jEnginoer.
Service....
1000 #
o so
40,
20
A
0 so 100 150 200 250 300 350 400 450 500 550 600 650 700
Capacity - usgpnl
Q An in Maxi
L
_.._.i..._. .....
... ... ...... ....... .... .. .......
... ................ ..
FEE
. ......... . ............
Fluid: Water
-------------
Efficiency
19,54 In
...... ....
. . .... . ......
Dls. Press,
.... ....... ....... .... .
........ --------
................ .. . ..... ....
Diff. Press,
NPSHr!
--- - ---------
. ............
. .... ... ... . ..........
0 so 100 150 200 250 300 350 400 450 500 550 600 650 700
Capacity - usgpnl
Q An in Maxi
L
. ....
...... . ........
.......... .... I.....
J. ............ ...... ......
T
. ......... . ............
Fluid: Water
-------------
Efficiency
19,54 In
...... ....
. . .... . ......
Dls. Press,
.... ....... ....... .... .
........ --------
S.C.: 0.998
Diff. Press,
NPSHr!
7.04 ft
. ............
BHP: 30-3 hp
I ip. Dia.:
- -------
. ...... .... .....
...
1gra Of Stages,
1
JBEP: 426 USgprn
P.
... ... ....
Voltage: 208-2301460
17.00 in
in
Phase: Three phase
F.: 1.15
S.
1 i.. ...... . .
35nn
60
1 Encl.: ODP
--------- - -
........... . ....
+ .........
I UU
-90
.80
70
60
-50
-40
30
20
10
0
V
0 so 100 150 200 250 300 350 400 450 500 S50 Soo 650 700
Capacity - usgpm
40-
20
fJ
0 50 100 150 ?00 250 300 350 400 450 500 550 Soo 650 700
capaefty - usgpm
P-5
J I PSHr I
J. ............ ...... ......
T
200 USqpm
fJ
0 50 100 150 ?00 250 300 350 400 450 500 550 Soo 650 700
capaefty - usgpm
P-5
Desll�n Data..:.
190w;
200 USqpm
Fluid: Water
Suct. Press: 0.00 pqLa
DH:
350 ft
Temp: 68.06 deg F
Dls. Press,
15kutoff Head:
363 ft
S.C.: 0.998
Diff. Press,
NPSHr!
7.04 ft
-
'Visc.; 1.00 op
BHP: 30-3 hp
I ip. Dia.:
9.54 In
Pump Eff.: 68A6
1gra Of Stages,
1
JBEP: 426 USgprn
P.
40
Voltage: 208-2301460
Eff;
�,6minal RPM.
3500
Phase: Three phase
F.: 1.15
S.
pp".
35nn
60
1 Encl.: ODP

'0/1,6/2008 12:21pm WWSI 7702766535
BERKELEY
MOTOR DRIVE
#439 Page 12/12
B2 TPMS
Nominal RPM 3600 Eased on I-resNr,wctercl-eq , F
I'rnpelrer Diu rnetc r; 6-3f TLS" f TPr Hf'}
57
155
150
145
LJ 14.0
w
.W. 1 38
¢ 130
W
= 125
J
120
O '
~ 115
110
105
n 25 50 75 100 125 150 175 200 22.5 250 275 "3C
B, E. C. 4,5
CAPACITY IN IJ.S•. (4,A1,1014C, PER MINUTE
7-5-
70
ZZ Uz
w
U�
65 ��
W
60
cc
w
10.0 ,_s
erC)
7,5. i w
00
5'er­ 11-G
SELECTIO14 CC3`N TTTdTttS
Flow:
MOTOR DRIVE
#439 Page 12/12
B2 TPMS
Nominal RPM 3600 Eased on I-resNr,wctercl-eq , F
I'rnpelrer Diu rnetc r; 6-3f TLS" f TPr Hf'}
57
155
150
145
LJ 14.0
w
.W. 1 38
¢ 130
W
= 125
J
120
O '
~ 115
110
105
n 25 50 75 100 125 150 175 200 22.5 250 275 "3C
B, E. C. 4,5
CAPACITY IN IJ.S•. (4,A1,1014C, PER MINUTE
7-5-
70
ZZ Uz
w
U�
65 ��
W
60
cc
w
10.0 ,_s
erC)
7,5. i w
00
5'er­ 11-G
C. u0TF;I) BY -
TAS
t DOTED Ta.
brooks job Cliff$
SELECTIO14 CC3`N TTTdTttS
Flow:
200.0 GPM
Priming Type:
Stondard,
Total Dynamic Head:
140.0 feet
M-ot-or Loading:
Stand"ard,
PUMP DESCRIPTION
Pump Model:
62TPMS
Pri(ring Type:
Standard
Impeller Diameter:
6.1aa in.
irrl•p•el-ler Material:
Iron
Suction:
2Yz"NPT
Discharge:
2"NPT•
Shaft Seal:
Mechanicar
PUMP PERFOR24ANCE
Flow:
200.0 GPM
Power_
a-7 E3N•P
Total Dynamic Head:
140.6 feet
Efficie-ncy:
73.47c,
'1.4.•2
Nominal Speed:
3600 RPM
NPSHR:
feet
Shut—Off Head:
154.5 feet
Max Power:
T T-6 ETHF
Sect Eff; 73.7 @' 214.Or GFM
MOTOR
Size:
10 FNP
Encloevre:
TEFL
o /,§
Voltage; Cor1sulL Catclog/Factary
Fiz/Phase:
—
PRICE/ORDER
INFORMATION
C:ataln,) No.:
Factory
Wcigh ;
200 lbs.
C. u0TF;I) BY -
TAS
t DOTED Ta.
brooks job Cliff$

6.4PumpCurveand TDH calculationsfor returnpumps
r-

BUNCOMBE COUNTY, NC THE CLIFFS AT HIGH CAROLINA PROJECT #307808
TDH = DH + hm
where:
AH = elevation head
hm = major pipe losses, utilize Hazen Williams equation with equivalent lengths for fittings
hm = (4.727 L/ d4 S7) (Q/C)1.85 where: Q in cfs, L in feet, d in ft.
D no user input
user input req'd
ON MEM
Piping:
Diameter= ��� �mches (nominal) equals 2.047 inches (ID)
0.1705833 ft.
Q (gpm)
A
hm (feet)
TDH1�O::
I
Velocity
5
173.00
0.34
173.0
0.5110
173.00
1.24
174.4
1.0215
173.00
2.63.0
1.5320
173.00
4.48
177..8
2.0422
173.00
5:35
178..2
22525
173.00
6.78
179..8
2.5530
173.00
9.50
182.0
3.0735
173.00
12.64
185.4
3.5840
173.00
16.19
189.9
4.0945
173.00
20.14
193.6
4.6050
173.00
24.47
197.5
5.11
Brooks Engineering Associates, PA P. 1 of 1 10/21/2008

�r
120
112
10.1
96
88
0 80
s 72
U
64
z
56
0 48
40
32
24
t6
8
0
GALLONS
LITERS
0 8 16 24 32 40 48 56 64
FLOW PER MINUTE
_ P PERFORMANCE
DISCHARGE10 GPM
015413
Part Number
H P
Voltage
Phase Amps
Stages
Height
5030-0005
1/2
115
1 12.0
6
22-3/8"
5030-0006
1/2
230
1 6.0
6
22-318"
5030-0007
112
115
1 12.0
8
015413
Part Number
H P
Voltage
Phase Amps
Stages
Height
5030-0005
1/2
115
1 12.0
6
22-3/8"
5030-0006
1/2
230
1 6.0
6
22-318"
5030-0007
112
115
1 12.0
8
24-118"
5030-0008
112
230
1 6.0
8
24-118"
5030-0009
3/4
230
1 8.0
12
28-718"
2 GPM Models ?&,7al�t,
PUMP PERFORMANCE CURVE k
27 GPM
1 1/4" NPT DISCHARGE t �" °' 1n
320 f
3fi - _ 1 1112 HP- QSTAGE
',��■
wmwaa ' mm
5 ib 15 10 25 3b 35 40
GA1.LaqS
UTERS 6 10 d0 66 80 100 1k 140
FLONPERMINUTE 015045
5 10 15 20 25 31
GALLONS
LITERS
0 20 40 60 80 100
FLOW PER MINUTE
015414
Part Number
HP
Voltage
Phase Amps
Stages
Height
5031-0005
112
115
1 12.0
4
21-118"
6031-0006
1/2
230
1 6.0
4
21-1/8"
E5032-0007
314
230
1 8.0
6
24-5116"
1
230
1 9.8
7
26-7/16°
230
1-1/2
230
1 13.1
10
31-7/8°
5 10 15 20 25 31
GALLONS
LITERS
0 20 40 60 80 100
FLOW PER MINUTE
015414
Part Number
H P
19 GPM Models
Phase Amps
Stages
Height
5031-0005
LL
PUMP PERFORMANCE CURVE
1 12.0
5
19 GPM
6031-0006
1/2
1^/4" NPT DISCHARGE
1 6.0
280
21-15116"
314
80
1 8.0
72
240
1
230
1 9.8
9
28-118"
230
1
64
4
24-15115'
5033-0009
1-1/2
230
200
13.1
5
29-15116"
0 56-
48-
160
U
a 40
t20
NH
32
2a
so
16
40
0
5 10 15 20 25 31
GALLONS
LITERS
0 20 40 60 80 100
FLOW PER MINUTE
015414
Part Number
H P
Vdtage
Phase Amps
Stages
Height
5031-0005
112
115
1 12.0
5
T-15116-
6031-0006
1/2
230
1 6.0
5
21-15116"
5031-0007
314
230
1 8.0
7
25-1116'
5031-0008
1
230
1 9.8
9
28-118"
35 GPM Models
w PUMP PERFORMANCE CURVE
35 GPM
2" NPT DISCHARGE
56 180
1-V2 HP- 5 STAGE
48 160-
140- 1HP-4STAGE
40
� 120
x
-11
314HP-3STAGE
�¢ 32 100
r
24 So-
so-
is-
40-
20-
All
0 112HP-2STAGE
0
so
16
40
8 20
0 l
10 20 30 40 50 60
GALLONS
LITERS 0 40 60 120 160 200
FLOW PER MINUTE 015044
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5033-0005
112
115
1
120
2
19=/116"
5033-0006
112
230
1
6.0
2
19-7/16°
5033-0007
314
230
1
8.0
3
22-3/16"
5033-0008
1
230
1
9.8
4
24-15115'
5033-0009
1-1/2
230
1
13.1
5
29-15116"
© Copyright 2007 Zoeller Co. All rights reserved.

BUNCOMBE COUNTY, NC THE CLIFFS AT HIGH CAROLINA PROJECT #307808
TDH = OH + hn,
where:
AH = elevation head
hrr, = major pipe losses, utilize Hazen Williams equation with equivalent lengths for fittings
hm = (4.727 L/ d'-") (Q/C)l.85 where: Q in cfs, L in feet, d in ft.
nsH
no user input
TDHffl27
user input req'd
5
175.00
Piping: "'d
177.10
Diameter =��IN inches (nominal) equals
2.047 inches (ID)
175.00
7.59
0.1705833 ft.
NODE: u
15
175.00
INPUTS Elevation Head Loss
Mayor Losses
Equiv Length lburn
No. inputs Fittings Details Initial Elev Final Elev.
L ' C"
(FT) Eq Length
s 6 $0 X905 2505.`
1
Q (gpm)
nsH
hm (feet)
TDHffl27
5
175.00
2.10
177.10
10
175.00
7.59
182.59
X245
15
175.00
16.09
191.09
20
175.00
27.41
202.41
24
175.00
38.42
213.42
92.4
25
175.00
41.44
216.44
93.7
2.55
30
175.00
58.09
233.09it
3.07
35
175.00
77.28
252.283.58
40
175.00
98.96
273.964.09
45
175.00
123.08
298.084.60
50
175.00
149.60
324.605.11
Brooks Engineering Associates, PA P. 1 of 1 10/21/2008

10 GPM Models
PUMP PERFORMANCE CURVE
10 GPM
1 114' NPT DISCHARGE
120 400
112 314 HR 12 STAB
360
104
96 320-
88
20
88 280-
q
8a
0 80 112 HP- 8 STAGE
i 72 240
U
64
200-
3
00
66 112 HP- 6 STAGE
0 48 i60
40
20
32
24 80
16
40
s
0
2 4
GALLONS
LITERS 0 8 1
6
le'
FLOW PER MINUTE 015413
Part Number
I
27 GPM Models
PUMP PERFORMANCE CURVE Pump
27 GPM
11/4" NPT DISCHARGE :.
36 320 7 1/2 HP -10 STAGE m9�
300 g
72 2d0
—ITp
Voltage
Phase
Amps
Stages
Height
5030-0005
112
115
1
12.0
6
22-318"
5030-0006
1l2
230
1
6.0
6
22-318"
5030-0007
1/2
115
1
12.0
8
24-118"
5030-0008
112
230
1
6.0
8
24-1/8"
5030-0009
3/4
230
1
8.0
12
28-7/8"
I
27 GPM Models
PUMP PERFORMANCE CURVE Pump
27 GPM
11/4" NPT DISCHARGE :.
36 320 7 1/2 HP -10 STAGE m9�
300 g
72 2d0
H P
Vdtage
Phase
1 HP- 7 STAGE
p 't
220
5032-0005
P.
200
3/4 TA
6STAGE
(
,•p�} @ /��' // ! p
d A
56 180
21-1/8"
5032-0006
b 48 160
J
230
1
740
4
21-118°
40
if2 HP -d STAGE
230
120
8.0
6
32 100
5032-0008
1
24 80
60
16
1
9.8
d0
26-7116°
5032-0009
8 20
230
1 1
0
S 1b is 20 2s 6 9s
40
GALLONS
TER
20 40 6 80 700 1 0 140
FLOW PER Al NUTE
015045
Part Number
H P
Vdtage
Phase
Amps
Stages
Height
5032-0005
112
115
1
12.0
4
21-1/8"
5032-0006
112
230
1
6.0
4
21-118°
5032-0007
314
230
1
8.0
6
24-5116"
5032-0008
1
230
1
9.8
7
26-7116°
5032-0009
1-112 1
230
1 1
1 13.1
10
31-718°
19 GPM Models
LL PUMP PERFORMANCE CURVE
19 GPM
1Y<" NPT DISCHARGE
f24
80 9 STAGE
72
64
0
56
w
= 4S
U
¢ 40
0 32
O24H-
16810 15 20 25
GAL
LITERS 0 20 40 60 80 10
FLOW PER MINUTE
015414
Part Number
H P
Vdtage
Phase Amps
Stages
Height
5031-0005
112
115
1 12.0
5
21-15116"
5031-0006
1/2
230
1 6.0
5
21-15116"
5031-0007
314
230
1 8.0
7
25-1/16"
5031-0008
1
230
1 9.8
9
28-18"
35 GPM Models
PUMP PERFORMANCE CURVE
LL 35 GPM
2" NPT DISCHARGE
56 180
1-112 HP- 5 STAGE
48 160-
140- 1 HP-4STAGE
40
120-
314
20
S
3/4 HP-3STAGE
a 32 100
0
a24 SO 1/2 HP-2STAGE
~ 60
16
40
9
20
0
10 20 30 40 50 60
GALLONS
LITERS 0 40 80 120 160 200
FLOW PER MINUTE 015044
Part Number
HIS
Voltage
Phase Amps
Stages
Height
5033-0005
1/2
115
1 12.0
2
19-7116°
5033-0006
112
230
1 6.0
2
19-7/16°
5033-0007
3/4
230
1 8.0
3
22-3116"
5033-0008
1
230
1 9.8
4
24-15116"
5033-0009
1-1/2
230
1 13.1
5
29-15116"
© Copyright 2007 Zoeller Co. All rights reserved.

III! I III 1 111
• �'

TANK SIZING CALCULATIONS
Return Flush Pump Tank
1850 gallon Pump Tank Selected
Minimum dose (gal)
Total Height
Storage (gal/ft)
Storage (gal/in)
min pump submergence
min dose volume
space lost due to float spacing
emergency storage
Emergency Storage (gal)
BEA Project #
307808
700
63 inches
355.51
29.63
26 inches
23.6 inches
8 inches
5.4 inches
159.14
Net On/Off
PT -298 Length (ft) Width (ft) Height (ft) Gal/ft Volume (gal) Setting (inches)
Pump Tank 1 9.83 4.83 5.25 355.51 1866.4 23.63
t n/ft.
29.63
Brooks Engineering Associates, PA
P.1 of 1
10/21/2008

6.6 Irrigation zone pressure & flow analysis

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Enaineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 fUs is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curare.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d487) (Q!C)f•ss
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush Rate lus the Dose Flow Rate
IA-
NO.ls:
7
(in)
0.79
h :
"m):
0.62
acin ft
2
age:
3616
ow (g m):
18.68
Application Flow (pm):
' ,�.
Min. Design Scour Vel. (ft/s)
Tubing ID (in)
a2.3O
Residual Flow for Scour (g m)6
Req'd Flush Rate (gpm)B:
Supply Manifold Elev.
' ,�.
1A-SM2
Return Manifold Elev.
1A-RM2
Run
Dose
Lateral
Lateral
Min. Flush
Run
Lateral Run Elev.
Len th
# Emitters Flow (gpm)'
Length (ft)
Dose L9 _PM)
Flow (gpm)s
1 1
30
0.3
602
3.033
11
5.41
2
35
0.4
3
43
0.4
4
48
0.5
5
62
0.6
6
83
0.9
2 7
114
1.2
474
2.4
4.7
8
123
1.3
3 9
129
1.3
522
2.7
5.0
10
132
1.4
4 11
131
1.4
492
2.5
4.8
12
115
1.2
5 13
73
0.8
594
3.1
5.4
14
71
0.7
15
71
0.7
16
82
0.8
6 17
76
0.8
584
3.0
5.3
18
74
0.8
19
72
0.7
20
70
0.7
7 21
65
0.7
348
1.8
4.1
22
51
0.5
P3
32
0.3
24
26
0.3
4ann
1R 7
18.7
34.8
Brooks Engineering Associates, PA p•
1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Total Headloss at Min. Flush Rate at Return Manifold
203.5
88.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
296.5
128.4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
412.8
178.7
Flush Pressure at backwash tank for Min. Flush Rate
452.4
195.8
55.0
16.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
PRV NEEDED? YES
Flush Pressure at WWTF far Min. Flush Rate
113.3
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
274.2
468.5
PSI
51.2
117.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
PRV setting utilized
127.1
39.1
55.0
16.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at WWTF far Min. Flush Rate
113.3
49.0
63.4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
146.4
1
Brooks Engineering Associates, PA p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d4'87) (Q/C)' 85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush Rate Plus the Dose Flow Rate
1A•2ls:
35.7
15
(in)
0.79h
:
"(gpm):
0.62acin
ft
2age:
Run
6908ow
(gpm):
35.69
Supply Manifold Elev.
35.7
1A-SM1
2.0
Return Manifold Elev.
_
1A -RM 1
2.30
Req'd Flush Rate (gpm)':
Run
Run
Lateral Run
Elev.
Len th # Emitter:
4.8
1.2
121
2{afl
1.2
472
121
2 3
1.2
120
4
1.2
466
119
3 5
1.2
118
6
1.2
462
118
4 7
1.2
117
8
1.2
458
116
5 9
1.2
116
10
1.2
448
115
6 11
1.1
115
12
1.1
434
114
7 13
1.1
113
14
1.1
442
111
8 15
1.1
108
16
1.2
462
109
9 17
1.2
110
18
1.2
480
111
10 19
1.3
114
20
1.3
490
117
11 21
1.3
119
22
1.3
488
121
12 23
1.3
123
24
1.1
418
122
13 25
1.1
122
26
1.1
426
122
14 27
1.1
104
28
35.7
105
15 29
106
30
°_
114
107
6908
3454
Ap lication Flow (gpm):
35.7
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Req'd Flush Rate (gpm)':
70.2
Dose
N (gpm)7
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (gpm)
1.3
484
2.5
4.8
1.3
1.2
478
2.5
4.8
1.2
1.2
472
2.4
4.7
1.2
1.2
466
2.4
4.7
1.2
1.2
462
2.4
4.7
1.2
1.2
458
2.4
4.7
1.2
1.2
448
2.3
4.6
1.1
1.1
434
2.2
4.5
1.1
1.1
442
2.3
4.6
1.1
1.2
462
2.4
4.7
1.2
1.2
480
2.5
4.8
1.3
1.3
490
2.5
4.8
1.3
1.3
488
2.5
4.8
1.3
1.1
418
2.2
4.5
1.1
1.1
426
2.2
4.5
1.1
35.7
35.7
70.2
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1A-2
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE Inputs 11 Dose Flow (a) Flush Flow (b)
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
Line length (ft) from P.T. to H.U' -
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
0.016 0.014
12.016 12.014
10/20/2008
Brooks Engineering Associates, PA
p.2 of 3
LJ
H.U. to J1
Segment Flow Rate (gpm)
,
'
Line Length (ft)-
Line Size ID (in)'
i�
3.058
2.778
_i
4 Friction Headloss (ft)
278
Minor Losses (ft)
2.27
2'27
2
2'18
.16
Line Velocity (ft/s)
ii
J1 to J2
Segment Flow Rate (gpm)
Line Length (ft)
ME
Line Size ID (in)5
0.434
0.902
5 Friction Headloss (ft)
090
Minor Losses (ft)
1.16
1.16
.73
1.73
1
Line Velocity (ft/s)
J2 to 1A-SM1,�
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
1.078
3.426
6 Friction Headloss (ft)
343
Minor Losses (ft)
1.92
1.92
3 .58
3.58
Line Velocity (ft/s)
Supply Force Main Elevation Delta
82
7 Elevation (ft) from H.U. to Manifold
'
Drip System Headloss Results
s °
a
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
Feed Manifold to Bottom Lateral
_.
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Lateral'
50
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.933
3.504
9 Total Segment Headloss (ft) = Friction + Elev.
-42.067
-46.496
Return Force Main Friction Losses
1A-RM1 toJ21,yr��
�„;-
Segment Flow Rate (gpm)
Line Length (ft)
606
Line Size ID (in.)
Minor Losses from Check Valve
0.438
Friction Headloss (ft)
1.50
Line Velocity (ft/s)
J2 to J1
Segment Flow Rate (gpm)"
Line Length (ft)
490
Line Size ID (in.)
Minor Losses (ft)
,,.
1.853
Friction Headloss (ft)
3.66
Line Velocity (ft/s)
11 to WWTF
Segment Flow Rate (gpm)r
Line Length (ft)
1000
�"
Line Size ID (in.)
REP l-%-
Minor Losses (ft)
3.782
Friction Headloss (ft)
2.03
Line Velocity (ft/s)
Return Line Elevation Delta
+NWTF
_J
Elevation (ft) from Return Manifold to
10/20/2008
Brooks Engineering Associates, PA
p.2 of 3
LJ

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 1A-2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
181.1
78.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
318.9
138.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
429.0
185.7
Flush Pressure at backwash tank for Min. Flush Rate
476.4
206.2
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
290.4
51.2
Pressure at manifold before PRV
469.0
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
37.0
45.0
16.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at WWTF for Min. Flush Rate
112.9
48.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
139.0
60.2
Brooks Engineering Associates, PA
p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: ht = (4.727 U d"'87) (Q/C)165
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Supply Manifold Elev. 1A-SM1
Return Manifold Elev. 1A-RM1
Run Run
Lateral Run Elev. Length
1 1I"
2
3
4
5
6
7
8
9
10
11
12
13
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
72
74
78
79
70
73
82
81
68
68
76
153
150
155
150
153
149
148
145
148
147
147
144
148
150
150
150
149
148
146
Application Flow (gpm):
zone: 1A-3
No. Latera=Lft)2
Tubing: ID
Emitters
Emitter Spacing
Total FootDesign
Flo
Req'd Flush Rate (gpm)':
Supply Manifold Elev. 1A-SM1
Return Manifold Elev. 1A-RM1
Run Run
Lateral Run Elev. Length
1 1I"
2
3
4
5
6
7
8
9
10
11
12
13
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
72
74
78
79
70
73
82
81
68
68
76
153
150
155
150
153
149
148
145
148
147
147
144
148
150
150
150
149
148
146
Application Flow (gpm):
40.0
Min. Design Scour Vel. (fUs)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)'
2.30
Req'd Flush Rate (gpm)':
69.9
Dose
Flow (gpm
0.8
0.7
0.8
0.8
0.8
0.7
0.8
0.8
0.8
0.7
0.7
0.8
1.6
1.6
1.6
1.6
1.6
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.6
1.6
1.6
1.5
1.5
1.5
1.5
40.0
Lateral Lateral Min. Flush
-th rfh nose lnom) Flow (gpm)
608
3.1
5.4
586
3.0
5.3
606
3.1
5.4
610
3.2
5.5
604
3.1
5.4
586
3.0
5.3
590
3.0
5.3
582
3.0
5.3
596
3.1
5.4
600
3.1
5.4
594
3.1
5.4
580
3.0
5.3
Brooks Engineering Associates, PA
p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1A-3
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE Inputs Dose Flow (a) Flush Flow (b)
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 .5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2.778
2 Total Segment Headloss (ft) = Friction + Elev.
0.278
Hydraulic Unit
2.16
H.U. Elev
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
3 Headloss from H.0 (ft.)s
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Supply Force Main Friction Losses
0.902
H.U. to J1
0.090
Segment Flow Rate (gpm)
Line Length (ft)
1.73
Line Size ID (In)5
4 Friction Headloss (ft)
0.254
Minor losses (ft)
0.025
Line Velocity (ft/$)
0.88
J1 to J2
SegmE:nt Flow Rate (gpm)
Line Length (ft)
1A-RM1 to J2
Line Size ID (in)"
5 Friction Headloss (ft)
Minor Losses (ft)
Line Length (ft)
Line Velocity (ft/s)
317
J2 to 1A-SM1
Line Size ID (in.)
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
Minor Losses from Check Valve
6 Friction Headloss (ft)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
1.30
0.016 0.014
12.016 12.014
3.058
2.778
0.306
0.278
2.27
2.16
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
0.434
0.902
0.043
0.090
1.16
1.73
0.081
0.254
0.008
0.025
0.47
0.88
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
82
Drip System Headloss Results
° 4
t A"
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
1.801
5.166
9 Total Segment Headloss (ft) = Friction + Elev,
-43.199
-46.834
Return Force Main Friction Losses
1A-RM1 to J2
Segment Flow Rate (gpm)
Line Length (ft)
317
Line Size ID (in.)
Minor Losses from Check Valve
0.229
Friction Headloss (ft)
1.30
Line Velocity (ft1s)
J2 to J1
EM `
Segment Flow Rafe (gpm)
Line Length (ft)
490
Line Size ID (in.)
M
Minor Losses (ft)
3
Friction Headloss (ft)
2.03
2.0
Line Velocity (ft/s)
J1 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
Minor Losses (ft) 3.782
Friction Headloss (ft) 2.03
Line Velocity (ft/s)
rte?
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF FT,, `'
r-� 10/20!2008
Brooks Engineering Associates, PA p.2 of 3
j

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 1A-3
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
200.9
87.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
299.1
129.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
431.3
186.7
Flush Pressure at backwash tank for Min. Flush Rate
456.8
197.8
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
292.7
470.1
PSI
51.2
117.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
14.0
45.0
6.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
90.1
39.0
Flush Pressure at W WTF for Min. Flush Rate
140.1
60.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d"'87) (Q/C)' 85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 E uals the Re uired Flush Rate lus the Dose Flow Rate
Supply Manifold Elev.
1 B-5ls:
IB -SMI
15
(in 0.79h
: 0.62acin
"(gPm):39.95
ft 2age:
7732w
(gpm): 39.95
Run
Supply Manifold Elev.
39.9
IB -SMI
2.0
Return Manifold Elev.
76; _
18-RM1
2.30
Req'd Flush Rate (92m) 8 :
Run
Run
Lateral Run
Elev.
Len th # Emitter:
1 1
0.7
P< 1
27
2
0.8
602
53
3
0.7
55
4
0.7
70
---' 2 5
0.8
78
6
1.1
438
71
7
1.2
71
8
1.2
492
81
3 9
1.3
106
j 10
1.4
538
113
4 11
1.4
120
12
1.4
556
126
r ' 5 13
1A
133
14
1.5
574
136
6 15
1.5
138
_
16
1.5
584
140
7 17
1.5
143
18
1.5
592
144
8 19
1.5
145
20
1.5
576
147
9 21
1.5
149
22
1.4
524
147
--i 10 23
1.3
1
145
24
1.1
396
143
11 25
0.9
135
26
0.9
594
127
12 27
0.8
107
28
0.7
91
13 29
0.7
84
30
0.7
440
75
a 31
0.6
70
_ 32
14 33
0.5
68
63
"1 34
0.5
58
35
36
0.4
416
52
47
15 37
0.4
42
38::
1 39
0.3
35
312
40
0.3
5
41
J
0.2
23
` 42
43�
0.2
21
17
_.I 44
! 37 r$
14
7732
386
Ap lication Flow (gpm):
39.9
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (g m)s
2.30
Req'd Flush Rate (92m) 8 :
74.7
Dose Lateral Lateral Min. Flush
Flow (gpm)7
Length (ft)
Dose (gpm)
Flow (gpm)
0.3
410
2.1
4.4
0.5
0.6
0.7
0.8
602
3.1
5.4
0.7
0.7
0.8
1.1
438
1.9
4.2
1.2
1.2
492
2.4
4.7
1.3
1.4
538
2.8
5.1
1.4
1.4
556
2.9
5.2
1A
1.5
574
3.0
5.3
1.5
1.5
584
3.0
5.3
1.5
1.5
592
3.1
5.4
1.5
1.5
576
3.0
5.3
1.5
1.4
524
2.7
5.0
1.3
1.1
396
2.0
4.3
0.9
0.9
594
3.1
5.4
0.8
0.7
0.7
0.7
440
2.5
4.8
0.6
0.5
0.5
0.4
416
2.6
4.9
0.4
0.3
0.3
0.2
0.2
0.2
0.1
cn2
74.7
Brooks Engineering Associates, PA
p.1 of 3 10!2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1 B-5
ID
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
I Dose Flow (all Flush Flow (b)
LINE
_Inputs
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.016
0.014
2 Total Segment Headloss (ft) = Friction + Elev.
12.016
12.014
Hydraulic Unit
H.U. Elev %
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J1
r
i
Segment Flow Rate (gpm)
00-021
� a�
m
Line Length (ft)
Line Size ID (in)'
3.058
2.778
4 Friction Headloss (ft)
0.306
0.278
Minor Losses (ft)
2.27
2.16
Line Velocity (ft/s)
J1 to J3
�-
Segment Flow Rate (gpm)'
Line Length (ft)
WON
Line Size ID 00'
0.081
0.278
5 Friction Headloss (ft)
028
Minor Losses (ft)
1.11
1.11
.16
2.16
2
Line Velocity (ftls)
J3 to1B-SMI
itis,
Segment Flow Rate (gpm)
za
Line Length (ft)
s
.,
Lme S¢e (m)
6 Friction Headloss (ft) 1.415 4.454
0.142 0.445
Minor Losses (ft) 1.75 3.24
Line Velocity (ft/$)
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 70
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
4'•I"
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold'
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
-- Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2 1.491 4.759
9 Total Segment Headloss (ft) = Friction + Elev. -49.509 -53.241
_a
Return Force Main Friction Losses
1 B -RMI to J3 34.5
Segment Flow Rate (gpm)
Line Length (ft) 360
Line Size ID (in.) _
Minor Losses from Check Valve 3.072
Friction -0.38
on Headloss (ft)
-0.38
Line Velocity (ft/s)
J3 to J15<
,,a Segment Flow Rate (gpm) 100
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft) ".
0.419
Friction Headloss (ft) 2.15
Line Velocity (ft/s)
J1 to WWTF
Segment Flow Rate (gpm) 1000
Line Length (ft)
Line Size ID (in.)( _
Minor Losses (ft) 0
.92
Friction Headloss (ft) 2.15
Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF Y4 '
p.2 of 3 10/20!2008
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE IB -5
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
190.5
82.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
309.5
134.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
448.5
194.1
Flush Pressure at backwash tank for Min. Flush Rate
445.5
192.9
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
309.9
469.0
51.2
117.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
PRV setting utilized
104.0
16.0
45.0
6.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
82.3
35.6
Flush Pressure at WVVTF for Min. Flush Rate
146.5
63.4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Brooks Engineering Associates, PA
p.3 of 3 10/20!2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d") (Q/C)' as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush Rate plus the Dose Flow Rate
1 B-6ls:
25.8
10
(in)
0.79h
:
"(gPm):
0.62acin
ft
2age:
48.9
5022w
(gpm):
25.95
A plication Flow (g m):
25.8
Min. Design Scour Vel.(ft/s)
2.0
Tubing ID in
0.787
Residual Flow for Scour (gpm)s
2.30
R "d Flush Rate (g m)-:
48.9
Supply Manifold Elev.
1 B-SM2
Return Manifold Elev
H
1B-RM2
Dose
Lateral
Lateral
Min. Flush
Run
Lateral Run Elev.
Run
Len th # Emitters Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)
1 1
11
0.1
532
2.7
5.0
2
15
0.2
3
19
0.2
4
24
0.2
5
31
0.3
6
49
0.5
7
55
0.6
8
62
0.6
2 9
62
0.6
582
3.0
5.3
10
69
0.7
11
79
0.8
12
13
81
102
0.8
1.1
420
2.2
4.5
3
14
15
108
113
1.1
1.2
462
2.4
4.7
4
16
118
123
1.2
1.3
504
2.6
4.9
5 17
18
129
131
1.3
1.4
528
2.7
5.0
6 19
PO
133
136
1.4
1.4
548
2.8
5.1
7 21
22
138
140
1.4
1.4
566
2.9
52
8 23
24
143
1.5
9 25
145
1.5
582
3.0
5.3
28
146
83
1.5
0.9
298
1.5
3.8
10 27
28
5022
66
0.7
2511
25.9
25.9
48.9
10/20/2008
Brooks Engineering Associates, PA
P.1 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1 B- 6
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs
Dose Flow (a)
Flush Flow (b)
LINE.,
1 Operating Head from Pump Curve'
9 x
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.014
2 Total Segment Headloss (ft) = Friction + Elev.
122.01.01 6
12.014
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (fQ3
Supply Force Main Friction Losses
H.U. to J10
-R.
Segment Flow Rate (gpm)
i Line Length (ft)
-
Line Size ID (in)5
3.058
2.778
4 Friction Headloss (ft)
Minor Losses (ft)
2.27
2.27
2 .16
2.16
Line Velocity (ft/s)
J1 to J4
Segment Flow Rate (gpm)
i Line Length (ft)
Line Size ID (in)5
0.597
2.042
5 Friction Headloss (ft)
i Minor Losses (ft)
1.11
1.11
2
2.16
.16
Line Velocity (ft/s)
J4 to 1 B-SM2
25,g
48.9
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
0.324
1.047
6 Friction Headloss (ft)
0,0320.105
Minor Losses (ft)
.i
1.13
1.13
2.13
2.13
Line Velocity (ft/s)
r, Supply Force Main Elevation Delta
82
7 Elevation (ft) from H.U. to Manifold
J Drip System Headloss Results a -
in drip system from supply manifold to return manifold r
N
8 Total Headloss (ft.)
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
- Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.519
9 Total Segment Headloss (ft) = Friction + Elev.
224.724.72 0
30.481
Return Force Main Friction Losses
- 1 B-RM2 to J4
23.0
Segment Flow Rate (gpm)
Line Length (ft)
185
-! Line Size ID (in.)
Minor Losses from Check Valve
5.983
Friction Headloss (ft)
3.63
Line Velocity (ft/s)
J4 to J1
�
J Segment Flow Rate (gpm)
Line Length (ft)
735
Line Size ID (in.)�
Minor Losses (ft)
1.178
Friction Headloss (ft)
1.28
_g Line Velocity (ft/s)
J1 to WWTF'.
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
Minor Losses (ft)
4.192
Friction Headloss (ft)
2.15
2.15
Line Velocity (ft/s)
-1
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
�----
u
^I, p.2 of 3 10/20/2008
'_ J
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 1B-6
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
195.9
84.8
131.7
Manifold
Low Pressure Check: P at Min. Flush Flow at Return Manifold
412.3
178.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
464.3
201.0
Flush Pressure at backwash tank for Min. Flush Rate
133.2
57*7
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
273.7
469.6
51.2
117.7
Pressure at manifold before PRV
calculated (pressure at manifold -pressure loss required)
154.3115.5
66.5
PRV setting
setting utilized
32.5
50.0
14.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
111.1
48.1
,PRV
Flush Pressure at WWTF for Min. Flush Rate
133.2
57*7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4'a') (Q/C)''$$
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
R Equals the Re uired Flush Rate Plus the Dose Flow Rate
.5
ls:
16
(in
0.79
h :
".43.08
0.62
acin ft
2
age:
8338
ow (gpm):
43.08
Appin.lication Flow gpm):
43.1
MDesign Scour Vel. (fus)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Re 'd Flush Rate (gpm;?
79.9
'
Supply Manifold Elev.
3A-SM1
Return Manifold Elev.
Run
3A-RM1
Run
Dose
Lateral
Lateral
Min. Flush
_.i
Lateral Run
Elev.
Len th # Emitters
Flow (gpm)7
Length (ft)
Dose (g m)
Flow (gpm)
1 1
23
0.2
554
2.9
5.2
2
33
0.3
3
42
0.4
_ j
4
50
0.5
5
58
0.6
71
0.7
r r
2 7
90
0.9
378
2.0
4.3
8
99
1.0
3 9
108
1.1
432
2.2
4.5
_)
10
108
1.1
4 11
111
1.1
448
2.3
4.6
r-
12
113
115
1.2
1.2
462
2.4
4.7
5 13
14
15
116
118
1.2
1.2
476
2.5
4.8
6
16
17
120
121
1.2
1.3
494
2.6
4.9
7
18
126
1.3
8 19
134
1.4
540
2.8
5.1
I-
20
9 21
136
138
1.4
1.4
552
2.9
5.2
24
23
138
139
1.4
1.4
558
2.9
5.2
10
24
140
1.4
11 25
140
1.4
564
2.9
5.2
26
27
142
144
1.5
1.5
580
3.0
5.3
r"
12
28
146
146
1.5
1.5
588
3.0
5.3
_s
13 29
30
148
148
1.5
1.5
594
3.1
5.4
14 31-r
32
149
1.5
`3
15 33
86
0.9
592
3.1
5.4
34
78
64
0.8
0.7
35
3636)
16 37
G•.
-� ;
68
58
0.7
0.6
526
2.7
5.0
-�
38
r
�n
50
0.5
39
4.5
0.5
40a
41
0.4
41
36
0.4
42��
6'
33
0 3
43 1
79
8338
4169
43.9
' ?
Brooks Engineering Associates, PA
p.1 of 3
1 0/2012 00 8

i
'i
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
li
ZONE 3A-7
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs I Dose Flow a)
Flush Flow (b)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 .5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 5
0.005
0.016
2 Total Segment Headloss (ft) = Friction + Elev.
12.005
12.016
Hydraulic Unit
--,
H.U. Elev
(ft.)'
3 Headloss from H.0 (ft.
Supply Force Main Friction Losses
H.U. to J1
-
-i
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
0.959
3.178
4 Friction Headloss (ft)
318
Minor Losses (ft)
1'21
1.21
2.32
2 .32
- -,
Line Velocity (ft/s)
J1 to J6.'
o- ` "
Segment Flow Rate (gpm)
`�`�`�'
�'
-�
Line Length (ft)
Line Size ID (in)5
1.017
3.369
5 Friction Headloss (ft)
0.102
0.337
Minor Losses (ft)
1.21
2.32
Line Velocity (ft/s)
_
J6 to 3A-SM1
Segment Flow Rate (gpm)`
Line Length (ft)
1
Line Size ID (in)'
0.816
2.653
6 Friction Headloss (ft)
265
-
Minor Losses (ft)
1.63
1.63
3
3.08
.08
Line Velocity (ft/s)
Supply Force Main Elevation Delta
96
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
Total Headloss (ft.) in drip system from supply manifold to return manifold
°
r-�
8
Feed Manifold to Bottom Lateral
--
Headloss (ft) in manifold°
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
- -1
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral?
'
1.453
4.518
9 Total Segment Headloss (ft) = Friction + Elev.
-33.547
-37.482
--
Return Force Main Friction Losses
3A-SM1 to J6
Segment Flow Rate (gpm)
-A
Line Length (ft)
325
Line Size ID (in.)
AIWIN
Minor tosses from Check Valve
2.478
Friction Headloss (ft)
1.60
Line Velocity (ft/s)
J6 to J1
e�
Segment Flow Rate (gpm)
1060
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
°�`
- -
Friction Headloss (ft)
2.26
2.26
Line Velocity (ft/s)
J1 to WWTF�;8�"'
Segment Flow Rate (gpm)
1000
Line Length (ft)
-
Line Size ID (in.)
0�
Minor Losses (ft)
4.621
Friction Headloss (ft)
2.26
Line Velocity (ft/s)
Return Line Elevation Delta
9 M
Elevation (ft) from Return Manifold to WWF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3A-7
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
211.2
91.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
287.8
124.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
407.5
176.4
Flush Pressure at backwash tank for Min. Flush Rate
470.1
203.5
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi) 489.9 117.7
Pressure at manifold before PRV 154.3 66.5
PRV setting calculated (pressure at manifold - pressure loss required) 115.5 50.0
PRV setting utilized 5 14.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold 34. 34.5 52.6
Flush Pressure at WWTF for Min. Flush Rate 142.0 61.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow.
i
-'a
i
J
j
l
i7
_i
Brooks Engineering Associates, PA p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: ht = (4.727 L/ d4 a') (Q/C)t 85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush Rate lus the Dose Flow Rate
3A-8
ls:
8
(in)
0.79
h :
"(gPm�):
0.62
acin ft
2
age:
4148
ow (gpm):
21.43
Supply Manifold Elev. 3A-SM1
Return Manifold Elev. 3A-RM1
Run Run
I af.-I Run Elev. Length #
2
3
4
5
6
7
8
2
21.4
Min. Design Scour Vel. (ft/s)
17
3
0.787
Residual Flow for Scour (gpm)'
19
4
39.8
2.6
21
5
2.5
4.8
24
6
4.6
588
26
7
29
8
31
g
34
10
39
11
41
12
45
13
100
14
113
15
127
16
129
17
128
18
126
19
124
20
123
21
122
22
122
23
120
24
105
25
87
26
79
27
60
28
(
68
4148
207,
Application Flow (g m):
21.4
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)'
2.30
Req'd Flush Rate (gpm)':
39.8
Dose
0.2
0.2
0.2
0.2
0.3
0.3
0.3
0.4
0.4
0.4
0.5
1.0
1.2
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.2
1.1
0.9
0.8
0.6
0.7
21.�
Lateral Lateral Min. Flush
enoth (ft) Dose (gpm) Flow (gpm)
598
3.1
5.4
512
2.6
4.9
508
2.6
4.9
494
2.6
4.9
488
2.5
4.8
450
2.3
4.6
588
3.0
5.3
Brooks Engineering Associates, PA
P.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 3A-8
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT Inputs Dose Flow (a) Flush Flow (h)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
0.005 0.016
12.005 12.016
10/20/2008
H.U. to J1
—-
Segment Flow Rate (gpm)°
Line Length (ft)
Line Size ID (in)5
0.959
3.178
4 Friction Headloss (ft)
Minor Losses (ft)
1'21
121
.32
2.32
2
_
Line Velocity (ft/s)
J1 to J6
Segment Flow Rate (gpm)
—
Line Length (ft)`
Line Size ID (in)5
1.017
3.369
5 Friction Headloss (ft)
37
Minor Losses (ft)
1
1.21
2.
2.32
Line Velocity (ft/s)
.21
—�
J6 to 3A -SMI
Segment Flow Rate (gpm)
_3
Line Length (ft)
Line Size ID (in)5..
0.816
2.653
6 Friction Headloss (ft)
265
..
Minor Losses (ft)
1.63
1.63
3 .08
3.08
Line Velocity (ft/s)
Supply Force Main Elevation Delta
96
7 Elevation (ft) from H.U. to Manifold
_ j
Drip System Headloss Results
Total Headloss (ft.) in drip system from supply manifold to return manifold"
�71W$ry8
8
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
_
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
1.786
5.066
j
9 Total Segment Headloss (ft) = Friction + Elev.
-26.214
-29.934
Return Force Main Friction Losses
3A-SM1 to J650
t` 731
Segment Flow Rate (gpm)
—
Line Length (ft)
325
Line Size ID (in.)
Minor Losses from Check Valve
2.478
'
Friction Headloss (ft)
0.80
0.80
Line Velocity (ft/s)
J6 t0 J i
Segment Flow Rate (gpm)
Line Length (ft)
1060
"A',02 .....
�l
Line Size ID (in.)
Minor Losses (ft)
4.898
Friction Headloss (ft)
2.26
Line Velocity (ft/s)
Ji to WWTF�
�����;
"I
Segment Flow Rate (gpm)
Line Length (ft)
1000
4i}2t
Line Size ID (in.)
Minor Losses (ft)`�
4.621
Friction Headloss (ft)
2.26
r-1
Line Velocity (ft/s)
Return Line Elevation Delta
az
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3A-8
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
218.2
94.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
280.8
121.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
400.1
173.2
Flush Pressure at backwash tank for Min. Flush Rate
463.1
200.5
NEEDED? YES
Pressure loss required (high pressure - 60 psi)
469.9
117.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
50.0
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
115.5
27,5
11.9
Flush Pressure at WWTF for Min. Flush Rate
114.5
134.7
49.6
58.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Brooks Engineering Associates, PA
P.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d4'8) (Q/C)' 85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 E uals the Recuired Flush Rate plus the Dose Flow Rate
Zone: 1 B-9
No. Laterals:
3
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
1358
Design Flow (gpm):
7.02
Supply Manifold Elev. 1B-SM3
Return Manifold Elev. 1 B-RM3
Run Run
Lateral Run Elev. Length
1 1
2
3
4
2 5
g
3 7
g
g
10
Brooks Engineering Associates, PA
Application Flow (gpm):
7.0
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Req'd Flush Rate (gpm)':
13.9
P.1 of 3
10/20/2008
Dose
# Emitters Flow (gpm)'
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (gpm)'
11 0.1
398
2.1
4.4
16 0.2
89 0.9
83 0.9
82 0.8
470
2.4
4.7
153 1.6
70 0.7
490
2.5
4.8
67 0.7
58 0.5
50 0.5
1358 679 7.0
7.0
13.9
P.1 of 3
10/20/2008

6.1 Design Flow Table & Phasing Summary
6.2 WWTP Head Calculations and Process Calculations & Supporting Charts
6.3 Pump curve for irrigation dose pumps and pump curve for pumps in series
6.4 Pump Curve and TDH calculations for return pumps
6.5 Return pump tank sizing calculations
6.6 Irrigation zone pressure & flow analysis
6.7 Irrigation schedule spreadsheet
6.8 Rainfall data analysis for short term wet weather storage requirements

6.1 Summary
Design Flow Table & Phasing
r'.'1

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1B-9
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs
Dose Flow fall
Flush Flow (b)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.016
0.014
2 Total Segment Headloss (ft) = Friction + Elev.
12.016
12.014
Hydraulic Unit
H.U. Elev
1
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J3
Segment Flow Rate (gpm)
Line Length (ft)
—
Line Size ID (in)s-
3.373
3.056
4 Friction Headloss (ft)
7
6
Minor Losses (ft)
227
2
2.16
2.1
Line Velocity (ft/s)
,2
J3 to J4
M`F���
Segment Flow Pate (gpm)
Line Length (ft)
Line Size ID (in)5
9?
0.503
0.620
5 Friction Headloss (ft)
Minor Losses (ft)
1.11
1.24
1 .24
Line Velocity (ft/s)1.11
J4 to 1 B-SM3
y
of
Segment Flow Rate (gpm)
Line Length (ft)
_
Line Size ID (in)6
0.071
0.231
6 Friction Headloss (ft)
07
023
Minor Losses (ft)
1.01
1.
.91
1.91
1
Line Velocity (ft/s)
Supply Force Main Elevation Delta
46
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return
manifold" F�
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.769
2.542
9 Total Segment Headloss (ft) = Friction + Elev.
-18.231
-23.458
Return Force Main Friction Losses
1 B-RM3 to J4
�
Segment Flow Rate (gpm)
'�
Line Length (ft)
50
Line Size ID (in.)
Minor Losses from Check Valve
f 7 °`
0.394
Friction Headloss (ft)
0.66
Line Velocity (ft/s)
J4 to J1
Segment Flow Rate (gpm)
620
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
0.993
Friction Headloss (ft)
1.28
1.28
Line Velocity (ft/s)
11 to WWTF
Segment Flow Rate (gpm)
1100
Line Length (ft)
4`
Line Size ID (in.)
"
Minor Losses (ft)?'-
4.611
Friction Headloss (ft)
2.15
Line Velocity (ft/s)
Return Line Elevation Delta
5
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE iB-9
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
142.9
61.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
357.1
154.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
441.9
191.3
Flush Pressure at backwash tank for Min. Flush Rate
450.7
195.1
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
303.3
PSI
51.2
7.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.6
154.3
6 6.5
66.5
PRV setting utilized
127.1
59.1
55.0
25.6
Low Pressure Check: P at Min. Flush Flow at Return Manifold
107.1
46.3
Flush Pressure at WWTF for Min. Flush Rate
138.3
59.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow.
Brooks Engineering Associates, PA
p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d"'a') (Q/C)'•es
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush Rate lus the Dose Flow Rate
10-1 0
Supply
ls:
6
in)
0.79
h :
"(gpm):-
0.62
acin ft
2
age:
3138
ow (gpm):
16.21
Supply Manifold Elev. 1B-SM3
Return Manifold Elev. 1 B-RM3
Run Run
Lateral Run Elev. Len th
1 1 `
2
Lateral
39
3
Tubing ID (in)
49
4
Flow (gpm)
54
5
3.0
58
6
63
2 7
0.5
65
8
70
9
72
10
76
3 11
0.7
73
1E
73
13
2.9
76
14
80
4 15
0.7
74
16
72
17
73
18
604
81
5 19
0.8
96
20
97
6 21
99
Application Flow (gpm):
Lateral
Min. Design Scour Vel. ft/s)
Tubing ID (in)
E2.30
Residual Flow for Scour (gpm)e
Flow (gpm)
Req'd Flush Rate (gpm)-:
Dose
Lateral
Lateral
Min. Flush
Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)
0.3
580
3.0
5.3
0.4
0.5
0.6
0.6
0.7
0.7
566
2.9
5.2
0.7
0.7
0.8
0.8
604
3.1
5.4
0.8
0.8
0.8
0.8
600
3.1
5.4
0.7
0.8
0.8
1.0
386
2.0
4.3
1.0
1.0
402
2.1
4.4
1.1
16.2
16.2
30.0
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 18-10
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 .5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 5
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)'
Supply Force Main Friction Losses
H.U. to J3
_ Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (Irif
4 Friction Headloss (ft) 3.373 3.056
6
Minor Losses (ft) 2.2 7 2.1
"1
Line Velocity (ft/s) 2 27 2.16
J3 to J4 �' ` ;,.. v
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
_ 5 Friction Headloss (ft) 0.503 0.620
062
Minor Losses (ft) 1.11 .24
1
Line Velocity (ft/s) 1.11 1.24
J4 to 1 B-SM3 ,.
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft) 0.0.071 0.231
023
Minor Losses (ft) 1. .91
07 1.91
Line Velocity (ft/s) 1.01 1
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 46
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
Feed Manifold to Bottom Lateral
z
_ t Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
_ Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2 0.533 2.117
9 Total Segment Headloss (ft) = Friction + Elev. -10.467 -15.883
Return Force Main Friction Losses
1B-RM3 to J4 —
Segment Flow Rate (gpm) 5�
50
_j Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
0.394
Friction Headloss (ft) 1.32
Line Velocity (ft/s)
J4toA
Segment Flow Rate (gpm)
Line Length (ft) 620
Line Size ID (in.)2
Minor Losses (ft) W
0.993
Friction Headloss (ft) 1.28
Line Velocity (ft/s) 1'28
J1 to WTF� �a
r _1 WSegment Flow Rate (gpm) 1100
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
4.611
Friction Headloss (ft) 215
j Line Velocity (ft/s) 2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
Inputs Dose Flow (a) Flush Flow (b)
0.016 0.014
12.016 12.014
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 113-10
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
162.9
70.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
337.1
145.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
434.1
187.9
Flush Pressure at backwash tank for Min. Flush Rate
430.7
186.5
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
295.5
469.6
51.L
117.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
127.1
39.1
55.0
16.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
87.1
37.7
Flush Pressure at WWTF for Min. Flush Rate
130.5
56.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 2A-12
162
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs jDose
Flow (a)
Flush Flow (b)
LINE
3.70
2096
1 Operating Head from Pump Curve'r
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
8.786
2.15
Line length (ft) from P.T. to H.U'
1000
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.017
0.016
2 Total Segment Headloss (ft) = Friction + Elev.
`0
12.017
12.016
Hydraulic Unit
4.192
H.U. Elev
3 Headloss from H.0 (ft
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm)
Line Length (ft)�,
Line Size ID (in)5
3.301
3.107
4 Friction Headloss (ft)
30
311
Minor Losses (ft)
2.37
2
.29
2.29
2
Line Velocity (ft/s)
.
A to J7
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6.919
6.512
5 Friction Headloss (ft)
651
Minor Losses (ft)
2.37
2.37
2.29
2 .29
Line Velocity (ft/s)
J7 to 2A -SMI
�.
Segment Flow Rate (gpm)
Line Length (ft)
ism
Line Size ID (in)5
0
82
6 Friction Headloss (ft)
0.288
0.2
Minor Losses (ft)
.093
2.54
2.54
4.69
Line Velocity (ft/s)
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
151
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold' a "
Feed Manifold to Bottom Lateral m..
Headloss (ft) in manifold'
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
9 Total Segment Headloss (ft) = Friction + Elev.
Return Force Main Friction Losses
2A -RMI to J7
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
Line Velocity (ft/s)
J7 to JI
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
11 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
1.854 5.175
-30.146 -33.825
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008
162
2.551
3.70
2096
8.786
2.15
1000
`0
4.192
2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 2A-12
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
276.5
119.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
222.5
96.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
339.9
147.1
Flush Pressure at backwash tank for Min. Flush Rate
515.0
222.9
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
201.3
460.7
PSI
51.2
117.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
16.0
45.0
6.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
158.4
68.6
Flush Pressure at WWTF for Min. Flush Rate
127.1
55.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Brooks Engineering Associates, PA
p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Enaineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4 487 /C) (Q/C)' as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
R E uals the Re wired Flush Rate lus the Dose Flow Rate
3A-13
ls:
14
(in)
0.79h
:
"(QpM):34.0;3
0.62acin
ft
2age:
Lateral Run
6586ow
(gpm):
34.03
Supply Manifold Elev.
34.0
3A-SM2
Return Manifold Elev.
Tubing ID (in)
3A-RM2
Residual Flow for Scour gpm)'
Run
Run
Lateral Run
Elev.
Len th
1 1
147
2,
584
3.0
2 3
145
1.5
4
3 5
1.2
446
6
4.6
110
4 7
S
108
1.1
5 9
2.2
4.5
10
1.1
6 11
110
12
442
2.3
7 13
111
1.1
14
8 15
1.2
l
16
4.6
113
9 17
18
114
1.2
10 19
2.4
4.7
20
1.2
11 21
115
22
460
2.4
12 23
115
1.2
24
13 25
1.2
466
26
4.7
117
14 27
28
118
1.2
29
2.4
4.7
30
1.2
31
116
32
458
2.4
33
113
1.2
34
35'
1.1
416
36
3
99
1.0
6586
A plication Flow (gpm):
34.0
Min. Desi n Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour gpm)'
2.30
Re 'd Flush Rate (gpm)':
66.2
Dose
mitters Flow (gpm)'
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (gpm)
150
1.6
598
3.1
5.4
149
1.5
147
1.5
584
3.0
5.3
145
1.5
113
1.2
446
2.3
4.6
110
1.1
108
1.1
434
2.2
4.5
109
1.1
110
1.1
442
2.3
4.6
111
1.1
112
1.2
450
2.3
4.6
113
1.2
114
1.2
458
2.4
4.7
115
1.2
115
1.2
460
2.4
4.7
115
1.2
116
1.2
466
2.4
4.7
117
1.2
118
1.2
474
2.4
4.7
119
1.2
116
1.2
458
2.4
4.7
113
1.2
109
1.1
416
2.1
4.4
99
1.0
92
1.0
358
1.8
4.1
87
0.9
45
0.5
542
2.8
5.1
40
0.4
38
0.4
32
0.3
30
0.3
24
0.2
23
0.2
16
0.2
15
0.2
Brooks Engineering Associates, PA
P.1 of 3 10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 3A-13
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT Inputs Dose Flow (a) Flush Flow (b)
LINE
1 Operating Head from Pump Curve'
Pump Tank to N.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2 0.005 0.016
2 Total Segment Headloss (ft) = Friction + Elev. 12.005 12.016
Hydraulic Unit
--i H.U. ElevREW,
3 Headloss from H.0 (ftJ3 Ela_
' Supply Force Main Friction Losses
H.U. to J6 .:4 �." � , " 1
Segment Flow Rate (gpm) _ -
Line Length (ft)
Line Size ID (in)5
- 1.976 6.547
4 Friction Headloss (ft)
655
Minor Losses (ft) 1.21 .32
2
_ Line Velocity (ft1s) 1'21 2.32
J6 to 2A-SM1 kas,z
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
0.161 0.552
5 Friction Headloss (ft)
� 0.016 0.055
Minor Losses (ft)
0'42 0.82
Line Velocity (fUs)
— 2A-SM1 to 3A-SM2,
Segment Flow Rate (gpm)
Line Length (ft) a-
-i Line Size ID (in)s��"'
0.663 2.276
6 Friction Headloss (ft)
228
Minor Losses (ft) 1.48 .87
2
Line Velocity (ft/s) 1'48 2.87
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 109
Drip System Headloss Results 4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
,I Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Laterals 0.000 0.000
9 Total Segment Headloss (ft) = Friction + Elev. -30.000 -37.000
Return Force Main Friction Losses
3A-RM2 to 2A-RM1
Segment Flow Rate (gpm)"
Line Length (ft) 230
Line Size ID (in.)
Minor Losses from Check Valve'
0.600
Friction Headloss (ft) 11.4.40
Line Velocity (ftls)
2A -RM i to J6
Segment Flow Rate (gpm) 1200
Line Length (ft)
Line Size ID (in.) 0
Minor Losses (ft) LOS:
0.833
a Friction Headloss (ft) 0.81
Line Velocity (ft/s)
J6 to WWTF Segment Flow Rate (gpm) <•'.
2060
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft) 7.792
Friction Headloss (ft) 2.03
2.03
Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WW i F
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3A-13
Feet
PSI
Total Headloss at Min. Flush Rate at ReturnManifold
231.4
100.2
115.8
Low Pressure Check: P at Min. Flush Flow at Return Manifold
267.6
45.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
390.9
169.2
Flush Pressure at backwash tank for Min. Flush Rate
477.7
206.8
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
469.8
17.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
45.0
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
104.0
16.0
6.9
6.9
6.9
Flush Pressure at W Wl'F for Min. Flush Rate
117 7
127.0_
1.0
55.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d"'87) (Q/C)''85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
Q E uals the Required Flush Rateplus the Dose FlWFlu
Rate
Zone: 2B-14
s:9(in)
Scour Vel. (ft/s)
2.0
0.79h
:
0.62cin
ft
MEZ
2ge:
42.5
4530
gpm):
23.41
low (gpm):
_ 23.4
Scour Vel. (ft/s)
2.0
) -
0.787w
for Scour (gpm)6
2.30Rate
(gpm)6:
42.5
Supply Manifold Elev.
2B-SM1
Return Manifold Elevifi
26-RM1
Dose
Lateral
Lateral
Min. Flush
Run
Elev.
Run
Len th # Emitters Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm
Lateral Run
$
9
0.1
362
0.2
2 5
1 1
2
13
0.1
3
16
0.2
4
20
0.2
5
24
0.2
6
28
0.3
7
33
0.3
8
g
38
45
0.4
0.5
452
2.3
4.6
2
10
53
0.5
11
60
0.6
12
68
89
0.7
0.9
436
2.3
4.6
3 13
14
4 15
129
134
1.3
1.4
536
2.8
5.1
16
17
134
134
1.4
1.4
538
2.8
5.1
5
18
135
136
1.4
1.4
546
2.8
5.1
6 19
20
21
137
137
1.4
1.4
550
2.8
5.1
7
22
138
138
1.4
1.4
554
2.9
5.2
8 23
24
25
139
139
1.4
1.4
556
2.9
5.2
9
26
1
139
1.4
21.8
42.5
4530
2265
23.4
10/20/2008
Brooks Engineering Associates, PA
P.1 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 28-14
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT Inputs Dose Flow (a) Flush Flow (b)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
- Line Size ID (in) 0.017 0.016
Friction Headloss (ft) from Pump to H.U? 12.017 12.016
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev, Mew
3 Headloss from H.0 (ft.)3
Supply Force Main friction Losses
H.U. to J1
_,. Segment Flow Rate (gpm)
Line Length (ft)�
Line Size ID (in)5 3.301 3.178
-' 4 Friction Headloss (ft) 0.330 0.318
Minor Losses (ft) 2,37 2.32
i Line Velocity We)
J1 to J7
Segment Flow Rate (gpm)
Line Length (ft)`
Line Size ID (in)5 6.919 6.662
5 Friction Headloss (ft) 0.692 0.666
Minor Losses (ft) 2.37 2.32
Line Velocity (ft/s)
J7 to 28-SM1
9
Se ment Flow Rate (gpm)
Line Length (ft)
Line Size ID (1n)5 - 0.342 1.303
6 Friction Headloss (ft) 0.034 0.130
- Minor Losses (ft) 1.12 2.32
Line Velocity (ft/s)
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 179
Drip System Headloss Results'^
8 Total Headloss (ft.) in drip system from supply manifold to retum;manifold°
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateralz 1.578 4.726
-' 9 Total Segment Headloss (ft) = Friction + Elev. -22.422 -26.274
Return Force Main Friction Losses
2B-RM1 to J7 _D
Segment Flow Rate (gpm) 410
Line Length (ft) .
Line Size ID (in.)
Minor Losses from Check Valve 1.551
Friction Headloss (ft)
2.03
Line Velocity (ft/s)
J7ioJ1 .x��`
Segment Flow Rate (gpm) 2096
Line Length (ft)
Line Size ID (in.) .
Minor Losses (ft) 7.9P8
Friction Headloss (ft) 2.03
Line Velocity (ftls)
J1 to WWTF
" Segment Flow Rate (gpm) 1000
Line Length (ft)29
, y
Line Size ID (inJ
Minor Losses (ft) 3,782
Friction Headloss (ft) 2.03
Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF 1�
1 `l
Brooks Engineering Associates, PA p.2of3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 28-14
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
301.2
130.4
86.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
198.8
131.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
304.8
235.3
Flush Pressure at backwash tank for Min. Flush Rate
543.6
184.7
119.4
PRV NEEDED? YES
ZONE SUMMARY WI PRV
Pressure loss required (high pressure - 60 psi)
Feet
166.2
PSI
51.2461.4 117.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
45.0
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
104.0
18.0
7.8
Flush Pressure at WWTF for Min. Flush Rate
184.7
119.4
80.0
1 51.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4 B7) (Q/C)t es
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re c uired Flush Rate plus the Dose Flow Rate
2A-15ls:
59.7
22
in)
0.79h
:
"(gpm):
0.62acin
ft
2a
e:
11548ow
(gpm):
59.66
Supply Manifold Elev 2A -SMI
Return Manifold Elev 2A -RMI
Run Run
1 1
2
2 3
4
3 5
6
4 7
8
5 9
10
6 11
12
7 13
14
8 15
16
9 17
18
10 19
20
11 21
22
12 23
24
13 25
26
14 27
28
15 29
30
16 31
32
17 33
34
18 35
36
19 37
38
20 39
40
21
sc
F G N M
22 45
46
47
Brooks Engineering Associates, PA
Application Flow (gpm)_
59.7
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)'
2.30
Re 'd Flush Rate gpm)':
110.3
Dose
mitters Flow (gpm)'
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (gpm)'
139
1.4
556
2.9
5.2
139
1.4
139
1.4
554
2.9
5.2
138
1.4
138
1.4
550
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
138
1.4
552
2.9
5.2
138
1.4
138
1.4
554
2.9
5.2
139
1.4
139
1.4
554
2.9
5.2
138
1.4
138
1.4
552
2.9
5.2
138
1.4
138
1.4
550
2.8
5.1
137
1.4
137
1.4
546
2.8
5.1
136
1.4
134
1.4
534
2.8
5.1
133
1.4
132
1.4
528
2.7
5.0
132
131
1.4
1.4
524
2.7
5.0
131
1.4
131
1.4
490
2.5
4.8
114
110
1.2
1.1
426
2.2
4.5
103
1.1
99
1.0
392
2.0
4.3
97
1.0
87
0.9
606
3.1
5.4
73
0.8
69
0.7
74
0.8
76
0.8
340
1.8
4.1
48
0.5
27
0.3
,,fr_
11548 57j459.7 59.7
p.1 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
r`
Friction Headloss (ft) 2.15
Line Velocity (ftfs)
Return Line Elevation Delta5£i
_ Elevation (ft) from Return Manifold to WWTF
__ _J
p.2 of 3 10!2012008
Brooks Engineering Associates, PA
ZONE 2A-15
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs
Dose Flow (a)
Flush Flow (b)
LINE
t
_
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
1
Line length (ft) from P.T. to H.0 .6
Line Size ID (in)
0.017
0.016
Friction Headloss (ft) from Pump to H.U?
12.017
12.016
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
3.301
3.107
4 Friction Headloss (ft)
0.330
0.311
--
Minor Losses (ft)
2.37
2.29
Line Velocity (ft1s)
J1 to J7
yi
_
`!
Segment Flow Rate (gpm)'"
Line Length (ft)
�
__J
Line Size ID (in)'
6.919
6.512
5 Friction Headloss (ft)
0.692
0.651
Minor Losses (ft)
2.37
2.29
—`-1
Line Velocity (ft1s)
J7 to 2A-SM1
�v$
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
0.165
0.513
c-
6 Friction Headloss (ft)
0.017
0,051
Minor Losses (ft)
1.24
2.29
Line Velocity (ftls)
Supply Force Main Elevation Delta
151
7 Elevation (ft) from H.U. to Manifold
_71
J
Drip System Headloss Results
Headloss (ft.) in drip system from supply manifold to return
manifold° $s
.
e Total
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.648
3.049
9 Total Segment Headloss (ft) = Friction + Elev.
-51.352
-55.951
Return Force Main Friction Losses
2A-RM1 to J7
w 4
Segment Flow Rate (gpm)
165
Line Length (ft)
- -
Line Size ID (in.)
Minor Losses from Check Valve
0.692
-
Friction Headloss (ft)
2.15
Line Velocity (ftls)
J7 to J17�
Segment Flow Rate (gpm)
2096
Line Length (ft)
J
Line Size ID (in.)w
Minor Losses (ft)
8.786
Friction Headloss (ft)
2.15
Line Velocity (ft/s)
J1 to WWTF
Segment Flow Rate (gpm)
1000
-
Line Length (ft)
D2€i
Line Size ID (in.)
Minor Losses (ft)
4192
r`
Friction Headloss (ft) 2.15
Line Velocity (ftfs)
Return Line Elevation Delta5£i
_ Elevation (ft) from Return Manifold to WWTF
__ _J
p.2 of 3 10!2012008
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 2A-15
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
275.1
223 g
119.1
96.9
96.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
361.9
56.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
518.2
224.3
Flush Pressure at backwash tank for Min. Flush Rate
148.3
64.2
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
461.6
117.7
Pressure at manifold before PRV
calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting
PRV setting utilized
104.0
15.0
45.0
6.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
159.3
69.0
Flush Pressure at WWTF for Min. Flush Rate
148.3
64.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
10/20/2008
Brooks Engineering Associates, PA
p.3of3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
is to determine the pressures in the drip system
1. The purpose of this calculation spreadsheet
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
1
(Flush flow is for single zone and Dose flow is for dual zones.)
s5
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4.87)
(Q/C)'
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 he Re wired Flush Rate lus the Dose Flow Rate
s7 a
als:D in 0.62h
InFlow
:
2ts
acin ft
e: 13132
low m : 67.85
Supply Manifold Elev.- 2B -SMI
Return Manifold Elev. 2B-RM1
Run Run Dose Lateral Lateral
Min. Flush
Lateral Run Elev. Len th # Emitters Flow (gpm)' Length(ft) Dose ( pm Flow (g m)
1 1 89 0.9 368 1.9 4.2
2 95 1.0
2 3 95 1.0 384 2.0 4.3
4 97 1.0
3 5 100 1.0 408 2.1 4.4
6 104 1.1
4 7 110 1.1 448 2.3 4.6
8 114 1.2
5 g 116 1.2 470 2.4 4.7
10 119 1.2
6 11 122 1.3 494 2.6 4.9
12 125 1.3
7 13 128 1.3 516 2.7 5.0
14 130 1.3
--:.536 2.8 5
133 1.4 .1
8 15
16 135 1.4
9 17 139 1.4 562 2.9 52
--_ 18 142 1.5
10 19 144 1.5 582 3.0 5.3
147 1.5
l 11 201 149 1.5 600 3.1 5.4
22 151 1.6
12 23 151 1.6 606 3.1 5.4
152 1.6
24
13 25 152 1.6 608 3.1 5.4
26 152 1.6
^l 14 27 150 1.6 598 3.1 5.4
28 149 1.5
15 29 - 147 1.5 584 3.0 5.3
'�--� 30 145 1.5
16 31 143 1.5 568 2.9 5.2
32 141 1.5
-1 17 33 139 1.4 546 2.8 5.1
34's 134 1.4
is 35 132 1.4 522 2.7 5.0
s j 35 129 1.3
19 37 125 1.3 496 2.6 4.9
38 123 1.3
20 39 120 1.2 474 2.4 47
40 117 1.2
21 41 ,;. 114 1.2 452 2.3 4.8
42 112 1.2
22 43 110 1.1 434 2.2 4.5
-.4t 107 1.1
44 4.3
-� 23 45 s 102 1.1 396 2.0
96 1.0
46 'S 4.2
24 47 q - ,.�,�� 93 1.0 366 1.9
l 4890 0.9
25 �. 81 0.8 540 2.8 5.1
,1 8`.' 59 0.7
63 0.7
l 57 0.6
51 0.5 574 3.0 5.3
,1 26 54 48 0.5
55 42 0.4
56x x 38 0.4
_n uz* 6it 30 0.3
I, 58 30 0.3
89 24 0.2
60 4 ,fid a F, 24 0.2
- 13132 6566 67.8 67.8 127
i-7 10!20/2008
P.1 of 3
Brooks Engineering Associates, PA
':. J

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 2B-16
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs Dose Flow (aFlush Flow b
LINE4ygg
1 Operating Head from Pump Curve'
144
_
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 s
_
Line Size ID (in)
0.017
0.016
Friction Headloss (ft) from Pump to H.U?
12.017
12.016
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev 1REW..,
3 Headloss from H.0 (fQ3
Supply Force Main Friction Losses
H.U. to J1
-
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID 0r)s
T
3.301
3.178
4 Friction Headloss (ft)
0.330
0.318
Minor Losses (ft)
2.37
2.32
Line Velocity (fils)
Segment Flow Rate (gpm)
-
Line Length (ft)
Line Size ID 0n)s
6.919
6.662
5 Friction Headloss (ft)
0,692
0.666
Minor Losses (ft)
2.37
2.32
Line Velocity (ft/s)
J7 to 2B-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)"
0.342
1.303
6 Friction Headloss (ft)
0.034
0,130
Minor Losses (ft)
1.12
2.32
Line Velocity (1111s)
Supply Force Main Elevation Delta
179
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
Headloss (ft.) in drip system from supply manifold to return
manifold °
57SV
�.::T.>7
"�*`
8 Total
Feed Manifold to Bottom Lateral
_ . ,-
Headloss (ft) in manifold
`
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
1.708
4.940
9 Total Segment Headloss (ft) = Friction + Elev.
-53.292
-57.060
Return Force Main Friction Losses
2B-RM1 to J7
' -:c--'"
Segment Flow Rate (gpm)
410
Line Length (ft)
._,
Line Size ID (in.)
- - -
Minor Losses from Check Valve
-
1.551
Friction Headloss (ft)
2.03
Line Velocity (ft/s)
J7 to J1
1:tS
Segment Flow Rate (gpm)
2096
Line Length (ft)
-,- ,--
Line Size ID (in.)
-
Minor Losses (ft)
- "
7.928
Friction Headloss (ft)
2.03
Line Velocity (ft/s)
J1 to WWTF.'
'8
Segment Flow Rate (gpm)
1000
Line Length (ft)
Line Size ID (n.)
�.
Minor Losses (ft)
3,782
Friction Headloss (ft)
2.03
Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to W WTF
i----� 10/20/2008
p.2 of 3
Brooks Engineering Associates, PA -
__

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 213-16 Feet PSI
Total Headloss at Min. Flush Rate at Return Manifold 305.2 132.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold 194.8 84.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow 335.7 145.3
Flush Pressure at backwash tank for Min. Flush Rate 539.6 233.6
PRV NEEDED? YES
ZONE SUMMARY WI PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
197.1
461.4
51.2
17.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
66.5
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
104.0
14.0
180.7
45.0
6.0
75.2
Flush Pressure at W WTF for Min. Flush Rate
150.2
65.0
High Pressure Check: Emitter Pon Bottom Lateral at Dose Flow
p.3 of 3 10/20/2008
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4'87) (Q/C)t'a$
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush Rate lus the Dose Flow Rate
Zone: 4A-17
No. Laterals:
7
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter S acin it
2
Total Footage:
3664
Design Flow (gpm
Supply Manifold Elev. 4A-SM1
Return Manifold Elev. 4A -RMI
Run Run
i �f.-I Run Elev. Length #
2
3
4
2
3 9
10
4 11
12
5 13
14
6 15
16
7 LEM
Application Flow (gpm):
18.9
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)s
2.30
Reg'd Flush Rate (gpm)':
35.0
Dose
Hitters Flow (gpm)'
Lateral
Length (ft)
Lateral
Dose (gpm)
Min, Flush
Flow (gpm)
55
0.6
500
2.6
4.9
61
0.6
65
0.7
69
0.7
71
0.7
598
3.1
5.4
68
0.7
70
0.7
90
0.9
102
1.1
418
2.2
4.5
107
1.1
113
1.2
466
2.4
4.7
120
1.2
131
1.4
538
2.8
5.1
138
1.4
130
1.3
548
2.8
5.1
144
1.5
104
1.1
596
3.1
5.4
66
0.7
68
0.7
60
0.6
Brooks Engineering Associates, PA
p.1 of 3 10/20!2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 4A-17
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT Inputs Dose Flow (a) Flush Flow to)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
® Line Size ID (in)
Friction Headloss (ft) from Pump to H.U? 0.007 6
2 Total Segment Headloss (ft) = Friction + Elev. 12.007 122.0.0 16
Hydraulic Unit
® H.U. ElevMEMOA�
3 Headloss from H.0 (ft J3 ��
Supply Force Main Friction Losses
H.U. to J20
�» Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s �
5.061 10.970
4 Friction Headloss (ft)
.51 .30
1 2
Minor Losses (ft)
® Line Velocity (fUs) 1.51 2.30
J20toA1 &A >
Segment Flow Rate (gpm) _
Line Length (ft)
Line Size ID (in)'
-- 1.478 3.203
5 Friction Headloss (ft)
Minor Losses (ft) 1.37 2.07
a®e
Line Velocity (fUs) 1 37 2.07
J11to4A-SM1
Segment Flow Rate (gpm)
.® Line Length (ft)�
Line Size ID (in)s 0.346 1.112
6 Friction Headloss (ft) 0.035 0.111
Minor Losses (ft)
1.24 2.34
Line Velocity (fUs)
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 229
t
Drip System Headloss Results a .� ���,
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (In)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12 1.831 5.139
9 Total Segment Headloss (ft) = Friction + Elev. -12.169 -15.861
Return Force Main Friction Losses
4A-RM1 to J 11�
Segment Flow Rate (gpm)
a� Line Length (ft)5. ,
Line Size ID (in.)
Minor Losses from Check Valve
1.871
Friction Headloss (ft) 2.4
2.41
Line Velocity (ft/s)
A 1 to J20 --T'77-7-70
Segment Flow Rate (gpm) 1314
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft) 6.072
No Friction Headloss (ft) 2.26
Line Velocity (fUs)
J20 to WWfF
Segment Flow Rate (gpm)
Line Length (ft) 3503
4
I Line Size ID (in.)
Minor Losses (ft) 16.186
Friction Headloss (ft) 2.26
Line Velocity (fUs)
IN Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWfF -- =
Brooks Engineering Associates, PA
p.2 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Enoineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4.11 (Q/C)185
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
R E uals the Re wired Flush Rate plus the Dose Flow Rate
Zone: 4A-18
No. Laterals:
4
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
1872
Design Flow gpm):
9.67
Application Flow (gpm):
Min. Design Scour Vel. ft/s)
Tubing ID (in)
a2.3
Residual Flow for Scour (gpm)'
01 Flush Rate (gpm)':
Supply Manifold Elev.
4A -SMI
Return Manifold Elev
Run
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run
Elev.
Len th #
Emitters
Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)
1
-
24
0.2
584
3.0
5.3
27
0.3
27
0.3
65
0.7
63
0.7
86
0.9
2 7
104
1.1
408
2.1
4.4
8
100
1.0
3 9
97
1.0
380
2.0
4.3
10
93
1.0
4
89
0.9
500
2.6
4.9
79
0.8
46
0.5
36
0.4
1872
936
9.7
9.7
18.9
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 4A-18
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs
I Dose Flow (a) Flush Flow (b)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.007
0.016
2 Total Segment Headloss (ft) = Friction + Elev.
12.007
12.016
Hydraulic Unit
H.U. Elev NOW
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)�
Line Length (ft)
Line Size ID (in)s
4 Friction Headloss (ft)
5.061
10.970
097
Minor Losses (ft)
1.51
1.51
.30
2.30
2
Line Velocity (ft1s)
J20toA1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
1.478
3.203
5 Friction Headloss (ft)
320
Minor Losses (ft)
1.37
1.37
2 .07
2.07
Line Velocity (ft/s)
J11 to 4A-SM1
i ^�
Segment Flow Rate (gpm)
Line Length (ft)
-
Line Size ID (in)s
0.346
1.112
6 Friction Headloss (ft)
111
Minor Losses (ft)
1.24
1.24
.34
2.34
2
Line Velocity (ft/s)
Supply Force Main Elevation Delta
229
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
Total Headloss (ft.) In drip system from supply manifold to return manifold°
¢ OW
8
Feed Manifold to Bottom Lateral
, - . ,I
Headloss (ft) in manifold°
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
1.323
4.297
9 Total Segment Headloss (ft) = Friction + Elev.
-12.677
-16.703
Return Force Main Friction Losses
4A -RMI to A 1
5)
Segment Flow Rate (gpm)
f
Line Length (ft)
165
Line Size ID (in.)
Minor Losses from Check Valve
1.871
Friction Headloss (ft)
2.41
2.4
Line Velocity (ft/s)
J11 to J20�
s
`�"`�"��
Segment Flow Rate (gpm)
Line Length (ft)
1314
Line Size ID (in.)
Minor Losses (ft)
"1,
6.072
Friction Headloss (ft)
2.26
2'26
Line Velocity (ft/s)
J20 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)R°
16.186
Friction Headloss (ft)
2'26
Line Velocity (ft/s)
Return Line Elevation Delta
233
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA
p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4A-18
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
352.3
152.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
146.7
63.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
251.1
108.7
Flush Pressure at backwash tank for Min. Flush Rate
583.2
252.4
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
467.4
117.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
PRV setting utilized
13.6
60.0
24.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
114.5
Flush Pressure at WWTF for Min. Flush Rate
2664.4. 5
144.3
62.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hr = (4.727 U d4 $') (Q/C)''85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re wired Flush Rateplus the Dose Flow Rate
4A-20
ls:
8
(in)
0.79h
:
"(gpm):
0.62acin
ft
2age:
4288ow
(gpm):
22.15
Application Flow (gpm):
4A- M3
Min. Design Scour Vel. (ft1s)
Tubing ID (in)
a40.6
Residual Flow for Scour (gpry
Req'd Flush Rate (gpm)':
Supply Manifold Elev.
4A- M3
Return Manifold Elev.
Rune
4A-SM3
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Len th
# Emitters
Flow (gpm)7
Length (ft)
Dose (gpm)
Flow (gpm)'
1 1
98
1.0
398
2.1
4.4
2
101
1.0
2 3
135
1.4
540
2.8
5.1
4_
135
1.4
3 5
136
1.4
544
2.8
5.1
6
136
1.4
4 7
�
137
1.4
548
2.8
5.1
8
137
1.4
5 9
137
1.4
548
2.8
5.1
10
137
1.4
6 11
139
1.4
558
2.9
5.2
12
140
1.4
7 13
141
1.5
568
2.9
5.2
14
143
1.5
8 15
145
1.5
584
3.0
5.3
16
147
1.5
4288
2144
22.2
22.2
40.6
Brooks Engineering Associates, PA p.t of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 4A-20
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
Inputs
Dose Flow (a)
Flush Flow (b)
1 Operating Head from Pump Curve'
Big
- -
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.007
0.016
2 Total Segment Headloss (ft) = Friction + Elev.
12.007
12.016
Hydraulic Unit
H.U. Elev_ ,': l
3 Headloss from H.0 (ft.)3�
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)'Line
Length Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft)
5.061
10.970
Minor Losses (ft)
0.506
1.097
Line Velocity (ft/s)
1.51
2.30
J20 to J13.
Segment Flow Rate (gpm)
Line Length (it)
Line Size ID (in)5
5 Friction Headloss (ft)
2.733
5.924
Minor Losses (ft)
0.273
0.592
Line Velocity (ft/s)
1.37
2.07
J13 to 4A-SM3
Segment Flow Rate (gpm)'
Line Length (ft)1
Line Size ID (in)s
6 Friction Headloss (ft)
0.623
1.903
Minor Losses (ft)
0.062
0.190
Line Velocity (ft/s)
1.49
2.72
Supply Force Main Elevation Delta
292
7 Elevation (ft) from H.U. to Manifold
Drip System Headioss Results
8 Total Headloss (ft.) in drip system from supply manifold to return
manifold" RUFF E
.;-
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.675
4.886
9 Total Segment Headloss (ft) = Friction + Elev.
-8.325
-12.114
Return Force Main Friction Losses
4A-RM3 to J13
Segment Flow Rate (gpm)��
Line Length (ft)
165
Line Size ID (in.)
MINIM
Minor Losses from Check Valve
Friction Headloss (ft)
3.531
Line Velocity (ft/s)
2.90
J13 to J20
Segment Flow Rate (gpm)
Line Length (ft)
2430
Line Size ID (in.)
4t2
Minor Losses (ft)
Friction Headloss (ft)
11.228
Line Velocity (ft/s)
2.26
J20 to WWTF
Segment Flow Rate (gpm)
-7 --
Line Length (ft)
3503
Line Size ID (in.)
;94
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (ft/s)
2.26
Return Line Elevation Delta
u
Elevation (ft) from Return Manifold to-WWTF94
Brooks Engineering Associates, PA
p2of3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4A-20
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
416.8
181.3
Low Pressure Check: P at Min. Flush Flow at Return Manifold
80.2
34.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
182.1
78.8
Flush Pressure at backwash tank for Min. Flush Rate
633.6
274.3
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
43.5
PSI
51.2
Pressure at manifold before PRV
465.7
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
setting utilized
138.6
55.6
60.0
24.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
,PRV
Flush Pressure at VJWTF for Min. Flush Rate
318.7
137.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
139.9
60.6
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d°'B7) (Q/C)''B5
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
R E uals the Re uired Flush Rate Plus the Dose Flow Rate
5A-21
Kals:
5
(in)
0.79h
:
0.62acin
ft
2age:
27.1
3018ow
(gpm):
15.59
Application Flow (gpm):
15.6
Min. Design Scour Vel.(ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Rea'd Flush Rate (gpm)':
27.1
Dose Lateral Lateral Min. Flush
hitters Flow (gpm)7 Length (ft) Dose (gpm) Flow (gpm)
76
0.8
610
3.2
5.5
76
0.8
76
0.8
77
0.8
74
0.8
598
3.1
5.4
74
0.8
75
0.8
76
0.8
74
0.8
606
3.1
5.4
75
0.8
77
0.8
77
0.8
76
0.8
602
3.1
5.4
75
0.8
75
0.8
75
0.8
75
0.8
602
3.1
5.4
75
0.8
76
0.8
75
0.8
1509
15.6
15.6
27.1
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5A-21
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE Inputs Dose Flow (a)l Flush Flow (b)
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2 0.015 0.014
2 Total Segment Headloss (ft) = Friction + Elev. 12.015 12.014
Hydraulic Unit
H.U. Elev'
3 Headloss from H.0 (ft.)'
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm) OR -
Line Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft) 10.507 9.784
Minor Losses (ft) 1.051 0.978
Line Velocity (ft/s) 2.25 2.16
J20 to J14
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft) 6.094 5.675
Minor Losses (ft) 0.609 0.567
Line Velocity (ft/s) 2.03 1.95
J14 to 5A -SMI
Segment Flow Rate (gpm)
Line Length (ft) R '�
Line Size ID (in)5
6 Friction Headloss (ft) 0.572 1.685
Minor Losses (ft) 0.057 0.169
Line Velocity (ft/s) 1.51 2.71
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 284
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold°mac
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateralz 1.865 5.193
9 Total Segment Headloss (ft) = Friction + Elev. -12.135 -15.807
Return Force Main Friction Losses
5A-RM1 to J14
Segment Flow Rate (gpm)
Line Length (ft) 190
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft) 2.550
Line Velocity (ft/s) 2.64
Ji4 to J20
Segment Flow Rate (gpm)
Line Length (ft) 2610
Line Size ID (in.)
Minor Losses (ft) L
Friction Headloss (ft) 12.060
Line Velocity (ft/s) 2'26
J20 to W WTF
Segment Flow Rate (gpm)"
Line Length (ft) 3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft) 16.186
Line Velocity (ft/s) 2'26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF 288
Brooks Engineering Associates, PA p.2 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 5A-21
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
416.2
180.2
Low Pressure Check: P at Min. Flush Flow at Return Manifold
83.8
36.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
183.2
79.3
Flush Pressure at backwash tank for Min. Flush Rate
623.5
269.9
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
44.6
455.1
PSI
51.2
117.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
138.6
48.6
60.0
21.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
305.8
132.4
Flush Pressure at WWTF for Min. Flush Rate
143.7
62.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4'B7) (Q/C)' S5
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing cures for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush Rate ]us the Dose Flow Rate
Zone: 5A-22
No. Laterals:
7
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter S acin f'
2
Total Footage:
3722
Design Flow (gpm):
19.23
Application Flow (gpm):
19.2
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Req'd Flush Rate (gpm)':
35.3
Supply Manifold Elev.
5A-SM1
Return Manifold Elev.
5A -RMI
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run
Elev..
Len th # Emitters Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm),
1 1
23
0.2
514
2.7
5.0
2
27
0.3
3
44
0.5
4
47
0.5
5
55
0.6
6
61
68
0.6
0.7
602
3.1
5.4
2
70
0.7
80
0.8
83
0.9
3 11
74
0.8
624
3.2
5.5
12
77
0.8
13
79
0.8
14
4 15
82
75
0.8
0.8
534
2.8
5.1
16
77
0.8
17
56
0.6
18
6 19
59
59
0.6
0.6
476
2.5
4.8
2061
0.6
21�
59
0.6
P2
59
0.6
7 P3
59
0.6
476
2.5
4.8
24�
59
0.6
25
„
60
0.6
26
8 P7
60
61
0.6
0.6
496
2.6
4.9
P8
62
0.6
P9
62
0.6
3039
12
63
0.7
3722
1861
19.2
19.2
35.3
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5A-22
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE Inputs Dose Flow (a)l Flush Flow b)
_ 1 Operating Head from Pump Curve
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
Line length (ft) from P.T. to H.U'
_ Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2 0.015 0.014
2 Total Segment Headloss (ft) = Friction + Elev. 12.015 12.014
Hydraulic Unit
H.U. Elev NOW
3 Headloss from H.0 (ft.)3
- Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)' %
.f 4 Friction Headloss (ft) 10.5 1 9.784
6
Minor Losses (ft) 2.25 2.1
—I
Line Velocity (ftls) 2 25 2.16
J20 to J14 Segment Flow Rate (gpm)
_
i
_ Line Length (ft)
_
Line Size ID (in)'
6.094 5.675
5 Friction Headloss (ft)
567
Minor Losses (ft) 2.0. .95
09 11
Line Velocity (ft/s) 2.03 .95
J14 to 5A -SMI �r
Segment Flow Rate (gpm) '---
Line Length (ft)
M"W-
Line Size ID (in)'
0.572 1.685
6 Friction Headloss (ft)
_ 0.057 0.169
Minor Losses (ft)
Line Velocity (ft/s) 1.51 2.71
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 264
Drip System Headloss Results
g Total Headloss (ft.) in drip system from supply manifold to return manifold
° � � ��
Feed Manifold to Bottom Lateral t
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (In)5
Friction Headloss (ft) from Manifold to Bottom Feed LateralZ 1.303 4.263
9 Total Segment Headloss (ft) = Friction + Elev. 25.697 29.737
Return Force Main Friction Losses
5A-RM1 to J14 —71
Segment Flow Rate (gpm) t"
j Line Length (ft) 190
Line Size ID (in.)
Minor Losses from Check Valve -
2.550
Friction Headloss (ft) 2.64
Line Velocity (ftls)
J14 to J20
Segment Flow Rate (gpm)
Line Length (ft) 2610
Line Size ID (in.) 40'
Minor Losses (ft) EMMA—
12.060
Friction Headloss (ft)
2.26
Line Velocity (ft/s)
J20 to WWTF 7.
Segment Flow Rate (gpm)
Line Length (ft) 3503
Line Size ID (in.) "
Minor Losses (ft)�
16.186
Friction Headloss (ft)
r--- 2.26
Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
(
Brooks Engineering Associates, PA p.2 of 3
i
10(2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Total Headloss at Min. Flush Rate at Return Manifold 80. 1.
8 35.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold 1 0. 8 85.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow 620.5 85.2
Flush Pressure at backwash tank for Min. Flush Rate
268.6
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
455.1
117.7
Pressure at manifold before PRV
154.3
66 .5
PRV setting calculated (pressure at manifold - pressure loss required)
66.0`
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
138.6
45.6 45.6
99.7
Flush Pressure at WWTF for Min. Flush Rate
157.3
131.1.7
68.1
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Brooks Engineering Associates, PA
P3 of 3 10/20(2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d°'B7) (Q/C)' B5
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
a E uais the Re uired Flush Rate lus the Dose Flow Rate
5A-23
ls:
11
(in)
0.79
h :
"(22m):24.72
0.62
acin ft
2
age:
4784
ow (g m):
24.72
Supply Manifold Elev. 5A-SM2
Return Manifold Elev.5A-RM2
Runi Run
a.. Fiav Lenath #
I, .
70
69
88
2 5
6
3 7
98
98
96
8
4 9
10
5 11
12
96
94
94
94
93
6 13
14
7 15
16
92
91
110
112
8 17
18
9 19
20
109
105
103
102
10 21
22
11 23
24
100
99
88
85
25
70
63
low (4(gpm)8:
2.0
couft/s)
384
)
WFlush
forEN50.0
1.9
Rate
374
Dose
Flow (gpr
0.8
0.7
0.7
0.9
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
0.9
1.1
1.2
1.1
1.1
1.1
1.1
1.0
1.0
0.9
0.9
0.7
Lateral Lateral Min. Flush
ength (ft) Dose (gpm) Flow (gpm)
600 3.1 5.4
392
2.0
4.3
384
2.0
4.3
376
1.9
4.2
374
1.9
4.2
366
1.9
4.2
444
2.3
4.6
428
2.2
4.5
410
2.1
4.4
398
2.1
4.4
612
3.2
5.5
10/20/2008
Brooks Engineering Associates, PA
p.1 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5A-23
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE Inputs Dose Flow (a) Flush Flow (b)
1 Operating Head from Pump Curve' ��'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
0.015 0.014
12.015 12.014
10/20/2008
Brooks Engineering Associates, PA
p.2 of 3
H.U. to J20�
Segment Flow Rate (gpm)
`
Line Length (ft)
Line Size ID (in)s
10.5
9.784
-
4 Friction Headloss (ft)
10.978
Minor Losses (ft)
2.25
2 .25
2.16
2.16
Line Velocity (ft/s)
J20toJ15
Segment Flow Rate (gpm)
Line Length (ft)�
Line Size ID (in)5
6.678
6.218
5 Friction Headloss (ft)
0.668
0.622
'
Minor Losses (ft)
2.03
1.95
Line Velocity (ft/s)
—�
J15 to 5A-SM2�g
—�
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (In)5�
0.391
1.348
6 Friction Headloss (ft)
5
Minor Losses (ft)
.46
1.46
1
2.85
2.8
Line Velocity (ft/s)
Supply Force Main Elevation Delta
276
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
Total Headloss (ft.) in drip system from supply manifold to return manifold"`
8
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
I
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.923
5.286
--
9 Total Segment Headloss (ft) = Friction + Elev.
19.077
22.714
Return Force Main Friction Losses
I
5A-RM2 to J 15
Segment Flow Rate (gpm)
190
_
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
1.343
-""
Friction Headloss (ft)
2.40
Line Velocity (ft1s)
J
J15 to J20
Segment Flow Rate (gpm)
2860
Line Length (ft),D
• -�
Line Size ID (in.)
Minor Losses (ft)�'
13.215
l
Friction Headloss (ft)
2.26
Line Velocity (ft/s)
J20 to WWTFs;
$�
,-
Segment Flow Rate (gpm)
3503
Line Length (ft)
Line Size ID (in.)
"
Minor Losses (ft)
16.186
Friction Headloss (ft)
226
Line Velocity (ft/s)
Return Line Elevation Delta
28
Elevation (ft) from Return Manifold to WWTF
10/20/2008
Brooks Engineering Associates, PA
p.2 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
MMARY ZONE SA -23
Feet
PSI
tal Headloss at Min. Flush Rate at Return Manifold
408.4
91.6
176.8
39.7
N Pressure Check: P at Min. Flush Flow at Return Manifold
197.7
85.6618.3
Ih Pressure Check: Emitter P on Bottom Lateral at Dose Flow
115.5
267.7
ish Pressure at backwash tank for Min. Flush Rate
25.5
11.0
PRV NEEDED? YES
ZONE SUMMARY WI PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
59.1
454.7
51.2
Pressure at manifold before PRV
154.3
66.5 66.5
PRV setting calculated (pressure at manifold - pressure loss required)
115.5
50.0
PRV setting utilized
Pressure Check: P at Min. Flush Flow at Return Manifold
25.5
11.0
Low
Flush Pressure at WWTF for Min. Flush Rate
277.8
127.6
120.2
55.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4'a') (Q/C)' as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
R E uals the Re uired Flush Rate lus the Dose Flow Rate
Zone: 5A•24
_
No. Laterals:
13
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter S acin ft
2
Total Footage:
6418
Design Flow (g m):
33.16
A plication Flow (gpm):
5A-SM2
Min. Design Scour Vel. (ft/s)
Tubing ID in)
M31
Residual Flow for Scour (gpm)
Return Manifold Elev.
Flush Rate (gpm)':
Supply Manifold Elev.
5A-SM2
Return Manifold Elev.
5A-RM2
Dose
Lateral
Lateral
Min. Flush
Lateral Run
Run Run
Elev. Len th # Emitters
Flow (gpm)'
Length (ft)
Dose (gpm
Flow (gpm)'
1 1
132
1.4
526
2.7
5.0
2
3
131
130
1.4
1.3
518
2.7
5.0
2
4
129
1.3
3 5
128
1.3
508
2.6
4.9
6
126
1.3
4 7
125
1.3
496
2.6
4.9
8
9
123
122
1.3
1.3
484
2.5
4.8
5
10
120
119
1.2
1.2
472
2.4
4.7
6 11
12
13
117
116
1.2
1.2
462
2.4
4.7
7
14
15
115
113
1.2
1.2
450
2.3
4.6
8
16
112
110
1.2
1.1
436
2.3
4.6
9 17
18
108
107
1.1
1.1
426
2.2
4.5
10 19
20
106
104
1.1
1.1
408
2.1
4.4
11 21
22s1
100
81
1.0
0.8
626
3.2
5.5
12 23
24
79
0.8
25
77
0.8
26
76
78
0.8
0.8
606
3.1
5.4
13 27
za
t
77
0.8
P9
75
0.8
an
73
0.8..
Brooks Engineering Associates, PA
p.1 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5A-24
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pumpto Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev ''
3 Headloss from H.0 (ft.)3 1.4
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
y
Line Length (ft)
Line Size ID (in)5
0� a_,4r 10.507
9.784
4 Friction Headloss (ft)
1.051
0.978
Minor Losses (ft)
2.25
2.16
Line Velocity (ft1s)
2860
J20 to J15
Segment Flow Rate (gpm)'
u�
Line Length (ft)
13.215
Line Size ID (in)5
6.678
6.218
5 Friction Headloss (ft)
0.668
0.622
Minor Losses (ft)
2.03
1.95
Line Velocity (ft/s)
16.186
J15 to 5A-SM2"11-m
,s9
Segment Flow Rate (913m)Line
Length (ft)WN
Line Size ID (in)5
0.391
1.348
6 Friction Headloss (ft)
5
Minor Losses (ft)
.46
1.46
1
2.8
2.85
Line Velocity (ft/s)
Supply Force Main Elevation Delta
276
EI -ion (ft) from H U to Manifold
7 ev
_
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold'
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
-J 9 Total Segment Headloss (ft) = Friction + Elev.
Return Force Main Friction Losses
5A-RM2 to J15
Segment Flow Rate Wpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
Line Velocity (ft/s)
J15 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
J20 to WWTF
r i Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
j Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
1.888 5.230
-35.112 -38.770
ry =
r t p.2 of 3 10/20/2008
Brooks Engineering Associates, PA
1
190
y
1.343
2.40
2860
13.215
2.26
3503
4'D26
16.186
2.26
ry =
r t p.2 of 3 10/20/2008
Brooks Engineering Associates, PA
1

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Total Headloss at Min. Flush Rate at Return Manifold
411.4
88.6
178.1
38.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
213.8
92.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
615.3
266.4
Flush Pressure at backwash tank for Min. Flush Rate
22.5
9.7
PRV NEEDED? YES
274 8
118.9
Pressure loss required (high pressure - 60 psi)
454.7
117.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
115.5
66.5
PRV setting utilized
22.5
9.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
274 8
118.9
Flush Pressure at WWTF for Min. Flush Rate
(High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
143.6
62.2
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d°'87) (Q/C)' as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush Rate Plus the Dose Flow Rate
zone: 5B-25
No. Laterals:
11
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
5986
Design Flow (gpm):
30.93
Supply Manifold Elev. 9 5B-SM1
Return Manifold Elev. .. ;, 5B-RM1
Run Run
2
2 3
4
3 5
6
4 7
8
5 9
10
6 11
12
7 13
14
g 15
16
9
10 21
22
23
ill
Ap lication Flow (gpm):
30.9
Min. Design Scour Vel. Lf s)
2.0
Tubin ID (in)
0.787
Residual Flow for Scour (gpm)'
2.30
Req'd Flush Rate (gpm)':
56.2
Dose Lateral
136 1.4
136 1.4
137 1.4
137 1.4
138 1.4
139 1.4
139 1.4
140 1.4
141 1.5
141 1.5
142 1.5
142 1.5
143 1.5
110 1.1
106 1.1
82 0.6
75 0.8
67 0.7
70 0.7
70 0.7
65 0.7
63 0.7
60 0.6
57 0.6
53 0.5
48 0.5
43 0.4
41 0.4
546
550
556
562
566
570
432
588
Lateral
>se (gp
2.8
2.8
2.8
2.9
2.9
2.9
2.9
2.2
3.0
Min. Flush
Flow (gpm)
5.1
5.1
5.1
5.2
5.2
5.2
5.2
4.5
5.3
516
2.7
5.0
556
2.9
5.2
10/20/2008
Brooks Engineering Associates, PA
PA of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5B-25
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT I Inputs Dose Flow fall Flush F -100w to)
LINE gu1�
Y Head from Pump Curve'
1 Opera ing
Drip System Headloss Results
Total Headloss (ft.) in drip system from supply manifold to return manifold'
190
8
Pump Tank to H.U.
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold' _
Elevation (ft) from Pumpto Hydraulic Units
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line length (ft) from P.T.to H.0 5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
'- -
9 Total Segment Headloss (ft) = Friction + Elev.
Line Size ID (in)
Return Force Main Friction Losses
11.262
0.015
0.013
Friction Headloss (ft) from Pump to H.0 2
�J
12.015
12.013
2 Total Segment Headloss (ft) = Friction + Elev.
Minor Losses from Check Valve
11.883
Hydraulic Unit
1.91
Line Velocity (ft/s)
_..
H.U. Elev EWA
3 Headloss from H.0 (ft.)3
Line Length (ft)
Line Size ID (in.)
Supply Force Main Friction Losses
Minor Losses (ft)
Friction Headloss (ft)
H.U. to J20
Line Velocity (ft/s)
J20 to WWTF
Segment Flow Rate (gpm)
Segment Flow Rate (gpm)
Line Length (ft)
Line Length (ft)
Minor Losses (ft)
Friction Headloss (ft)
Line Size ID (in)'
Line Velocity (ft/s)
10.507
8.787
4 Friction Headloss (ft)
1.051
0.879
Minor Losses (ft)
2.25
2.04
Line Velocity (ft1s)
J20 to J16_
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
7.752
6.483
5 Friction Headloss (ft)
0.775
0.648
Minor Losses (ft)
2'03
1.84
Line Velocity (ft/s)
116 to 5B -SMI
—
3 ..
Segment Flow Rate (gpm)
Line Length (ft)'
'
Line Size ID (In)5
,�
0.359
1.054
6 Friction Headloss (ft)
36
0.105
Minor Losses (ft)
1.39
1
2.50
2.50
Line Velocity (ftls)
.
Supply Force Main Elevation Delta
268
7 Elevation (ft) from H.U. to Manifold
1.610 4.779
-31.390 -35.221
Drip System Headloss Results
Total Headloss (ft.) in drip system from supply manifold to return manifold'
190
8
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold' _
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
'- -
9 Total Segment Headloss (ft) = Friction + Elev.
Return Force Main Friction Losses
11.262
56 -RMI to J16
1.91
Segment Flow Rate (gpm)
�J
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
11.883
Friction Headloss (ft)
1.91
Line Velocity (ft/s)
_..
J16 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
J20 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
i—
Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
1.610 4.779
-31.390 -35.221
F77276;.. "',
-1 p.2 of 3 10/20/2008
Brooks Engineering Associates, PA
i�I
190
2.511
2.93
3320
11.262
1.91
3503
11.883
1.91
F77276;.. "',
-1 p.2 of 3 10/20/2008
Brooks Engineering Associates, PA
i�I

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Total Headloss at Min. Flush Rate at Return Manifold
Low Pressure Check: P at Min. Flush Flow at Return Manifold
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
Feet PSI
396.3 171.E
103.7 44.9
216.9 93.9
Pressure loss required (high pressure - 60 psi)
78.3
453.5
51.2
117.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
115.5
50.0
PRV setting utilized
28.5
12.3
Low Pressure Check: P at Min. Flush Flow at Return Manifold
278.8
120.7
Flush Pressure at W WTF for Min. Flush Rate
139.9
60.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
10/20(2008
Brooks Engineering Associates, PA
P.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d°'s') (Q/C)f as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
Q E uals the Re uiq red Flush Rate plus the Dose FlW
Rate
5B-26
ls:
_, 8
(in)
0.79h
:
"gpm):
0.62acin
ft
2age:
4714ow
gpm):
24.36
8
39
45
49
50
51
53
76
76
75
75
74
74
73
74
75
75
75
75
75
74
74
74
75
75
75
74
75
74
74
74
71
71
70
68
lo=(9PM)8:
Lateral
S
Min. Flush
EM42.8
Length (ft)
w
Flow (gpm)
R
Dose
Lateral
Lateral
Min. Flush
N (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)
0.4
574
3.0
5.3
0.5
0.5
0.5
0.5
0.5
0.8
604
3.1
5.4
0.8
0.8
0.8
0.8
590
3.0
5.3
0.8
0.8
0.8
0.8
600
3.1
5.4
0.8
0.8
0.8
0.8
594
3.1
5.4
0.8
0.8
0.8
0.8
598
3.1
5.4
0.8
0.8
0.8
0.8
594
3.1
5.4
0.8
0.8
0.8
0.7
560
2.9
5.2
0.7
0.7
10/20/2008
Brooks Engineering Associates, PA
p.1 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5B-26
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs Dose Flow (a)�
Flush_ FI_ ow (6)I
LINE
1 Operating Head from Pump Curve'
R"
2.511
2.93
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
11.262
1.91
Line length (ft) from P.T. to H.U.'
3503
Line Size ID (in)
0.015
0.013
Friction Headloss (ft) from Pump to H.U?
12.015
12.013
2 Total Segment Headloss (ft) = Friction + Elev.
1.91
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20`
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
10.507
8.787
4 Friction Headloss (ft)
1.051
0.879
Minor Losses (ft)
2,25
2.04
Line Velocity MIS)
J20 to J16
Segment Flow Rate (gpm)
—
Line Length (ft)
Line Size ID (in)s
7.752
6.483
5 Friction Headloss (ft)
0,775
0.648
Minor Losses (ft)
2.03
1.84
Line Velocity (ftls)
J16 to 5B -SMI
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
0.359
1.054
6 Friction Headloss (ft)
0.036
0.105
Minor Losses (ft)
1,39
2.50
Line Velocity (ft/s)
Supply Force Main Elevation Delta
268
EI tion (ft) from H U to Manifold
7 eva
j
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold'
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold'
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
9 Total Segment Headloss (ft) = Friction + Elev.
Return Force Main Friction Losses
r 56 -RMI to J16
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
"1 Friction Headloss (ft)
Line Velocity (ft/s)
A 6 to J20
Segment Flow Rate (gpm)
Line Length (ft)
F� Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ftfs)
J20 to VVWTF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
c -I Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WVVTF
1.631 4.815
-28.369 -32.185
I p.2 of 3 10120/2008
Brooks Engineering Associates, PA
--wi
190
R"
2.511
2.93
3320
11.262
1.91
3503
11.883
1.91
I p.2 of 3 10120/2008
Brooks Engineering Associates, PA
--wi

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Total Headloss at Min. Flush Rate at Return Manifold 102.7 1 44.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold 213.9 92.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow 619.5 1 268.2
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at WWTF for Min. Flush Rate
wi. h Dr--. rhack� Emitter P on Bottom Lateral at Dose Flow
Feet PSI
75.3 51.2
453.5 117.7
154.3 66.5
115.5 50.0'
27.5 11.9
277.8 120.3
136.9 59.3
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4 87) (Q/C)'•as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush RatePlus the Dose Flow Rate
5B-27
ls:
9
in)
0.79
h :
ODesignFlow
0.62
acin ft
2
age:
3986
w (gpm):
20.59
Application Flow (gpm):
20.6
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (g m)e
2.30
Req'd Flush Rate (gpm)':
41.3
Supply Manifold Elev. zr ,
5B-SM2
Return Manifold Elev. 59
5B-RM2
Dose
Lateral
Lateral
Min. Flush
Run
Lateral Run Elev.
Run
Len th #
Emitters
Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)
1 1
144
1.5
574
3.0
5.3
2
143
137
1.5
1.4
542
2.8
5.1
2 3
4
5
134
131
1.4
1.4
516
2.7
5.0
3
6
127
1.3
4 7
123
1.3
484
2.5
4.8
6
119
1.2
5 9
'
114
1.2
446
2.3
4.6
10
11
109
106
1.1
1.1
416
2.1
4.4
6
12
102
90
1.1
0.9
338
1.7
4.0
7 13
14
79
71
0.8
0.7
272
1.4
3.7
8 15
16
` "
65
0.7
0.6
398
2.1
4.4
9
56
52
0.5
48
0.5
43
0.4
Brooks Engineering Associates, PA
PA of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5B-27
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT Inputs Dose Flow a) Flush Flow im
LINE _
t' Had from Pump Curve'
1 Opera ng e
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
Line length (ft) from P.T. to H.0 5 _
Line Size ID (in) ;T
Friction Headloss (ft) from Pump to H. S 0..
2 Total Segment Headloss (ft) = Friction + Elev. 122.01,01 5 12.013
3
0
Hydraulic Unit
H.U. Elev maw � e:
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
10.507
8.787
4 Friction Headloss (ft)
1.051
0.879
Minor Losses (ft)
2.25
2.04
Line Velocity (ft/s)
J20 to J16
Segment Flow Rate (gpm)
-
Line Length (ft)
6
Line Size ID (in)'
-`
7.752
6.483
5 Friction Headloss (ft)
Minor Losses (ft)
2.03
2'03
1
1.84
.84
Line Velocity (ft1s)
J16 to 5B-SM2�
Segment Flow Rate (gpm)
Y
Line Length (ft)
Line Size ID (in)'
2.563
8.678
6 Friction Headloss (ft)
0.256
0.868
Minor Losses (ft)
1.50
2.90
Line Velocity ON
Supply Force Main Elevation Delta
268
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return
manifold°
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold'
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Latera
0.867
3.478
9 Total Segment Headloss (ft) = Friction + Elev.
17.133
17.133
21.522
Return Force Main Friction Losses
5B-RM2 to J16
Segment Flow Rate (gpm)
865
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
6.497
Friction Headloss (ft)
2.16
Line Velocity (ft/s)
J16 to J20
Segment Flow Rate (gpm)
3320
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)�'
11.262
Friction Headloss (ft)
1.91
Line Velocity (ftfs)
J20 to WWTF
- -
Segment Flow Rate (gpm)
3503
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
11.883
Friction Headloss (ft)
1.91
Line Velocity (ft/s)
us Return Line Elevation Delta
Elevation (ft) from Return Manifold to 1F WTF
Brooks Engineering Associates, PA
p.2 of 3 10I20l2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4'„) (Q/C)' 85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
R E uals the Re uired Flush Rateplus the Dose Flow Rate
5B-28
ls:
5
in)
0.79h
:
"(9pm):
0.62acin
ft
2age:
25.4
2684ow
(gpm):
13.87
Application Flow gpm):
13.9
Min. Design Scour Vel. ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm),
2.30
Req'd Flush Rate (gpm)':
25.4
Supply Manifold Elev. ��
5B-SM2
Return Manifold Elev.., �.�,:..
5B-RM2
Run
Dose
Lateral
Lateral
Min. Flush
Run
Lateral Run Elev.
Len th # Emitters
Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm),
1 1
43
0.4
574
3.0
5.3
2
45
0.5
3
47
0.5
4
48
0.5
5
"
51
0.5
6
53
56
0.5
0.6
484
2.5
4.8
2
L
59
0.6
63
0.7
64
0.7
3 11
67
0.7
556
2.9
5.2
12
70
0.7
13
71
0.7
14
70
69
0.7
0.7
546
2.8
5.1
4
3
69
0.7
68
0.7
67
0.7
5 19 _
67
0.7
524
2.7
5.0
20
37
0.4
21
36
0.4
22
32
0.3
23
28
0.3
24
24
0.2
25
21
0.2
26 X23 .
17
0.2
2684
1342
13.9
13.9
25.4
Brooks Engineering Associates, PA
p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5B-28
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs Dose Flow (a)
Flush Flow (b)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
0.015
0.013
2 Total Segment Headloss (ft) = Friction + Elev.
12.015
12.013
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3�fi
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm).1�"'"
Line Length (ft)
Line Size ID (in)6
8.787
4 Friction Headloss (ft)
1.10.5 1
879
Minor Losses (ft)
2.25
2
2 .04
2.04
Line Velocity (ft/s)
.25
J20 to J16
f vx
k
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (In)5
7.752
6.483
5 Friction Headloss (ft)
648
Minor Losses (ft)
2'03
2.03
.84
1.84
1
Line Velocity (ft/s)
J16 to 513-SM2
—^
Segment Flow Rate (gpm)s(��
Line Length (ft)
Line Size ID (in)5
2.563
8.678
6 Friction Headloss (ft)
56
868
Minor Losses (ft)
1
1.50
2.90
2 .90
Line Velocity (ft/s)
.
Supply Force Main Elevation Delta
268
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results OF
Total Headloss (ft.) in drip system from supply manifold to return manifold"
8
Feed Manifold to Bottom Lateral
g .,
Headloss (ft) in manifold°
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.443
4.501
9 Total Segment Headloss (ft) = Friction + Elev.
-26.557
-30.499
Return Force Main Friction Losses
5B-RM2 to J16
Y
Segment Flow Rate (gpm)'
Line Length (ft)
865
Line Size ID (in.)
Minor Losses from Check Valve
6.497
Friction Headloss (ft)
2.16
2.16
Line Velocity (ft/s)
J16 to J20
".
Segment Flow Rate Wpm)
Line Length (ft)
3320
Line Size ID (in.)
Minor Losses (ft)
shay.
11.262
Friction Headloss (ft)
1.9911
Line Velocity (ft/s)
J20 to WWTF
Segment Flow Rate Wpm)
r
Line Length (ft)
3503
fi
Line Size ID (in.)
KW
Minor Losses (ft)
11.883
Friction Headloss (ft)
1.9911
Line Velocity (ft/s)
Return Line Elevation Delta
26
Elevation (ft) from Return Manifold to WWTF
r-1 p.2 of 3 10/20/2008
L_
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 56-28
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
399.0
172.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
101.0
43.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
209.6
90.8
Flush Pressure at backwash tank for Min. Flush Rate
606.9
262.7
PRV NEEDED? YES
ZONE SUMMARY NitPRV
Pressure loss required (high pressure - 60 psi)
Feet
71.0
451.1
PSI
51.2
117.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
127.1
45.1
55.0
19.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
284.4
123.1
Flush Pressure at WWTF for Min. Flush Rate
146.6
63.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d°'s') (Q/C)'ss
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A Erluals the Required Flush Rate lus the Dose Flow Rate
Zone: 40-29
No. Laterals:
7
Tubing: ID (in
0.79
Emitters h :
0.62
Emitter S acin ft
2
Total Footage:
5018
Design Flow (gpm):
25.93
Application Flow (gpm):
25.9
Min. Design Scour Vel. ftls)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Req'd Flush Rate (g m 6:
48.9
Supply Manifold Elev.
4B-SM1
Return Manifold Elev.
4B-RM2
Dose
Lateral
Lateral
Min. Flush
Run
Lateral Run Elev.
Run
Len th # Emitters
Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)6
1 1
19
0.2
534
2.8
5.1
2
32
0.3
3
45
0.5
4
55
0.6
5
58
0.6
6
56
74
0.6
0.8
616
3.2
5.5
2
74
O.B
N
80
0.8
80
0.8
3 11
101
1.0
406
2.1
4.4
12
102
1.1
13
102
1.1
410
2.1
4.4
14
103
1.1
15
104
1.1
418
2.2
4.5
16
105
1.1
17
106
1.1
426
2.2
4.5
18
107
98
1.1
1.0
610
3.2
5.5
4
71
0.7
59
0.7
67
0.7
5 23
76
0.8
580
3.0
5.3
24
72
0.7
25
72
0.7
26
70
0.7
6 �$
68
0.7
492
2.5
4.8
65
0.7
59
0.6
�31
54
0.6
7
�$
49
0.5
526
2.7
5.0
32
43
0.4
33
39
35
0.4
0.4
344
35
lad
30
0.3
3626
376
23
0.3
0.2
38 _,`.
18
0.2
5018
2509
25.9
25.9
48.9
Brooks Engineering Associates, PA PA of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 4B-29
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT In uts I Dose Flow (all Flush Flow (b)
LINE �x
1 O erating Head from Pump Curve'
10/20/2008
P
Pump Tank to H.U.
'
Elevation (ft) from Pumpto Hydraulic Units
Line length (ft) from P.T. to H.U'
",-
Line Size ID (in)
0.007
0.001
Friction Headloss (ft) from Pump to H.0 2
12.007
12.001
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
WWI
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
s�
Line Length (ft)
Line Size ID (in)5
5.061
0.920
-
4 Friction Headloss (ft)
0.092
Minor Losses (ft)
1.51
1
0.60
Line Velocity (ft/s)
.51
J20 to J16
Segment Flow Rate (gpm)`
+i
Line Length (ft)
Line Size ID (in)5
-
0.
0.679
- h
5 Friction Headloss (ft)
0.002121
0.068
Minor Losses (ft)
0.29
0.54
Line Velocity (ft/s)
J16 to 4B -SMI
a'
Segment Flow Rate (gpm)
Line Length (ft)
1W
n
Line Size ID (in)5
6 Friction Headloss (ft)
2.144
0.214
6.949
0.695
Minor Losses (ft)
1.12
2.12
Line Velocity (ft/s)
Il
Supply Force Main Elevation Delta
254
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
Total Headloss (ft.) in drip system from supply manifold to return manifold ° r '
8
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
q
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
1.453
4.518
-
9 Total Segment Headloss (ft) = Friction + Elev.
-30.547
-34.482
r,
Return Force Main Friction Losses
4B -RMI to J16
-FF
Segment Flow Rate (gpm)
_-
Line Length (ft)
1230
Line Size ID (in.)
Minor Losses from Check Valve
4.958
s'
Friction Headloss (ft)
1.54
Line Velocity (ft/s)
-•
J16toJ20
Segment Flow Rate (gpm)
Line Length (ft)
3320
�k26'
Line Size ID (in.)
Minor Losses (ft)
.'�
1.237
Friction Headloss (ft)
0.58
Line Velocity (ft/s)
J20 to WWT
Segment Flow Rate (gpm)
Line Length (ft)
3503
; J
Line Size ID (in.)
Minor Losses (ft)
1.305
Friction Headloss (ft)
0.58
0.58
Line Velocity (ft/s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF''�2Fit1'
rl
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP PEED MANIFOLD SYSTEM
NE 4B•29
Feet
PSI
at Min. Flush Rate at Return Manifold
379.5
164.3
54.3
Check: P at Min. Flush Flow at Return Manifold
=ighh
125.5
105.4
Check: Emitter P on Bottom Lateral at Dose Flow
243,4
273.5
at backwash tank for Min. Flush Rate
631.8
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feetr5l.2
104.8Pressure
466.86.5154.36.5PRV
SI
at manifold before PRV
setting calculated (pressure at manifold - pressure loss required)
setting utilized
Pressure Check: P at Min. Flush Flow at Return Manifold
115.50.0PRV
23.50.2Low
Flush Pressure at WWTF for Min. Flush Rate
276.09.5
139.0
60.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
1
Brooks Engineering Associates, PA'
p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d°'87) (QIC)t.ea
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E uals the Re uired Flush RatePlus the Dose
Zone: 311BNc. Laterals: 48Tubing: ID (in) 0.79Emitters h : 0.62Emitter S acin ft 2Total Footage: 18398Design Flow (gpm): 95.06
Supply Manifold Elev. '9 36-SM1
Return Manifold Elev 3B-RM1
Run Run
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
ME
3B-SM2
Return Manifold
ZMEM
3B-RM2
Dose
Lateral
Lateral
Min. Flush
Flow (gpm)7
Length (ft)
Supply Manifold Elev. '9 36-SM1
Return Manifold Elev 3B-RM1
Run Run
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
low ( m :95.1Scour Vel. (ftls) 2.0)0.787w for Scour (gpm)s 2.30Rate (gpm)e: 205.5
# Emitters
156
167
169
171
173
175
177
179
182
183
184
185
185
185
186
186
187
188
168
190
192
194
196
199
2
202
205
209
212
216
220
217
216
216
217
1x 215
$ 214
213
208
l 204
200
197
193
S+ 188
183
?l 178
172
3 166
till; 161
9199
Supply Manifold Elev.
ME
3B-SM2
Return Manifold
ZMEM
3B-RM2
Dose
Lateral
Lateral
# Emitters
156
167
169
171
173
175
177
179
182
183
184
185
185
185
186
186
187
188
168
190
192
194
196
199
2
202
205
209
212
216
220
217
216
216
217
1x 215
$ 214
213
208
l 204
200
197
193
S+ 188
183
?l 178
172
3 166
till; 161
9199
Supply Manifold Elev.
ME
3B-SM2
Return Manifold
Elev.
3B-RM2
Dose
Lateral
Lateral
Min. Flush
Flow (gpm)7
Length (ft)
Dose (gpm)
Flaw (922L1.6
312
1.6
3.9
1.7
334
1.7
4.0
1.7
338
1.7
4.0
1.8
342
1.8
4.1
1.8
346
1.8
4.1
1.8
350
1.8
4.1
1.8
354
1.6
4.1
1.8
358
1.8
4.1
1.9
364
1.9
4.2
1.9
366
1.9
4.2
1.9
368
1.9
4.2
1.9
370
1.9
4.2
1.9
370
1.9
4.2
1.9
370
1.9
4.2
1.9
372
1.9
4.2
1.9
372
1.9
4.2
1.9
374
1.9
4.2
1.9
376
1.9
4.2
1.9
376
1.9
4.2
2.0
380
2.0
4.3
2.0
384
2.0
4.3
2.0
388
2.0
4.3
2.0
392
2.0
4.3
2.1
398
2.1
4.4
2.1
404
2.1
4.4
2.1
410
2.1
4.4
2.2
41B
2.2
4.5
2.2
424
2.2
4.5
2.2
432
2.2
4.5
2.3
440
2.3
4.6
2.2
434
2.2
4.5
2.2
432
2.2
4.5
2.2
432
2.2
4.5
2.2
434
2.2
4.5
2.2
430
2.2
4.5
2.2
428
2.2
4.5
2.2
426
2.2
4.5
2.1
416
2.1
4.4
2.1
408
2.1
4.4
2.1
400
2.1
4.4
2.0
394
2.0
4.3
2.0
386
2.0
4.3
1.9
376
1.9
4.2
1.9
366
1.9
4.2
1.8
356
1.8
4.1
1.8
344
1.8
4.1
1.7
332
1.7
4.0
� ;
592
1.7
4.0 -
p.1 of 3 10/20/2008
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 3B-30
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
I Inputs
I Dose Flow fall
Flush Flow (b)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 .5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.2
0.005 0.019
2 Total Segment Headloss (ft) = Friction + Elev.
12.005 12.019
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3�
Supply Force Main Friction Losses
H.U. to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
2.324 9.667
4 Friction Headloss (ft)
Minor Losses (ft)
2
2.53
11.17 .53
Line Velocity (ft/s)
.17
Supply Force Main Elevation Delta
66
5 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
4
�rt
6 Total Headloss (ft.) in drip system from supply manifold to return
manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Latera 12
0.587 2.378
7 Total Segment Headloss (ft) = Friction + Elev.
-50.413 -55.622
Return Force Main Friction Losses
3B-SM2 to WWTF
-�F y.A4
Segment Flow Rate (gpm)
2585
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
17.538
8 Friction Headloss (ft)
2.78
Line Velocity (ft/s)
Return Line Elevation Delta
2
9 Elevation (ft) from Return Manifold to WWTF
{ 10/20/2008
Brooks Engineering Associates, PA p.2 of 3
i

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3B-30 SU0 ANIFOLD 36-SM2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
160.7
69.6
143.4454.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
331.3
196.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
446.8
193.4
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
470.4
117.7
Pressure at manifold before PRV
(pressure at manifold - pressure loss required)
154.3
66.5
PRV setting calculated
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
104.0
44.0
19.0
40.9
Flush Pressure at WWTF for Min. Flush Rate
94.4
147.4
63.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Note: Return Flush Tank needed. See Pressure Calcs for Zone 3B-30 Submanifold 1
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 38-30 SUBMANIFOLD 3B -SMI
F
PSI
Total Headloss at Min. Flush Rate at Return Manifold
88eet '7
42.7
170.3
Manifold
Low Pressure Check: P at Min. Flush Flow at Return Manifold
517 0
223.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
382 8
165.7
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi) 470.4 117.7
Pressure at manifold before PRV 154.3 66.5
PRV setting calculated (pressure at manifold - pressure loss required) 104.0 45.0
PRV setting utilized440 19.0
.
Low Pressure Check: P at Min. Flush Flow at Return Manifold 13.2
Flush Pressure at WW30.4 TF for Min. Flush Rate 30.463.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow 147.5
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush
rl�
`II
iLI
1
3L
I'. J
it
10/20/2008
Brooks Engineering Associates, PA p.3 of 3
1

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineers Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
Run
at critical points of interest. The governing criteria are:
Flow (gpm)'
all emitters operate between 7 and 70 psi,
Dose (gpm
there is sufficient pressure to return the flush to the Hydraulic Unit,
1
a flushing flow velocity of 2 ftls is provided.
158
2. The source of either the calculations or the data inputs are indicated in the footnotes.
630
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in
Series Curve,
(Flush flow is for single zone and Dose flow is for dual zones.)
1.6
1.6
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4'e')
3.2
3 From Wastewater Systems Inc. Data
3
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
157
156
5 From Engineering Drawings
622
6 Calculated from Q = VA
5.5
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
g
7
8 E uals the Re wired Flush Rate I the Dose Flow Rate
5t.6
616
Zone: 6A-31
18
5.5
Application Flow (gpm):
Min. Desi n Scour Vel. ft/s
2 0
154
153
No. Laterals:
Tubin : ID in 0.79
612
Tubin ID in
(gpm)e
0.78'
2.30
6
Emitters h : 0.62
153
124
Residual Flow for Scour
Req'd Flush Rate ( m)B:
93.0
2.6
Emitter 5 acin ft 2
Total Foote e: 9982
7
12
13
124
126
Desi n Flow m : 51.57
506
2.6
Supply Manifold Elev. 6A-SM5
8
Return Manifold Elev. 6A-RM5
127
129
Supply Manifold Elev. 6ASM4
518
Return Manifold Elev. 6A-RM4
5.0
Supply Manifold Elev. 6A-SM3
16
17
Return Manifold Elev. "" 6A-RM3
Run Run Dose Lateral Lateral
Min. Flushe
feral
Run
Elev. Len # Emitters
Flow (gpm)'
Length (ft)
Dose (gpm
Flow (gpm)
5.6
1
1
158
1.6
630
3.3
2
2
3
157
157
1.6
1.6
628
3.2
5.5
3
4
5
157
156
1.6
1.6
622
3.2
5.5
4
g
7
155
154
1.6
1.6
616
3.2
5.5
g
g
g
154
153
1.6
1.6
612
3.2
5.5
6
10
11
153
124
1.6
1.3
496
2.6
4.9
7
12
13
124
126
1.3
1.3
506
2.6
4.9
8
14
15
127
129
1.3
1.3
518
2.7
5.0
9
16
17
130
131
1.3
1.4
526
2.7
5.0
10
18
19
132
134
1.4
1.4
538
2.8
5.1
20 u'58 r 7� 135
i 67
1.4
0.7
622
3.2
5.5
11
4
54
0.6
w `'?
51
0.5
48
0.5
46
0.5
12
-
45
44
0.5
0.5
544
2.8
5.1
_
a 45
0.5
45
0.5
45
0.5
;S- 46
0.5
13
47
48
0.5
0.5
584
3.0
5.3
48
0.5
49
0.5
49
0.5
49
0.5
5.4
14
39
49
0.5
598
3.1
40
50
0.5
41
50
OS
42
50
0.5
43
50
0.5
15
44
45
50
51
0.5
0.5
612
3.2
5.5
46
_
50
0.5
47
51
0.5
48
. °. 51
0.5
49
50
51
C 52
0.5
0.5
16
51
_ 52
0.5
0.5
624
3.2
5.5
52
53
52
52
0.5
54
52
0.5
55
52
0.5
17
56
57.98
S4r 52
49
0.5
0.5
488
2.5
4.8
58
,.v`r 45
0.5
59
' :_'¢;? 42
'� $ 39
0.4
0.4
60
61
a
36
0.4
62"r
33
37
0.3
0.3
218
1.1
3.4
18
84
28
0.3
65
b 26
0.3
66
E9$ti "`P r 24
0, a
51.6
93.1
P.1 of 3 10120/2008
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 6A-31
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
Inputs Dose Flow (al Flush Flow Ib)
LINE
1 Operating Head from Pump Curve
Pump Tank to H.U.
(ft) from Pump to Hydraulic Units
Elevation
Line length (ft) from P.T. to H.0 s
Line Size ID (in) s
Friction Headloss (ft) from Pump to H.U.
0.010
0.011
12 011
2 Total Segment Headloss (ft) = Friction + Elev.
12.010
Hydraulic Unit „,�,.
H.U. Elev
3 Headloss from H.0 (RJs
Supply Force Main Friction Losses
H.U. to 3B-SM2
Segment Flow Rate (gpm)
ySBi�s
Line Length (ft)
Line Size ID (in)5'"`
5.052
5.635
4 Friction Headloss (ft)
0.505
Minor Losses (ft)
1.78
1.89 1.89
.89
Line Velocity (ft1s)
3B-SM2 to 3B-SMicv,,_
Segment Flow Rate (gpm)
-
Line Length (ft)x
Line Size ID (45
_Z
0.410
0.458
5 Friction Headloss (ft)
0.041
0.046
Minor Losses (ft)
1.78
1.89
Line Velocity (ft/s)
3B-SM1 to 6A-SM3
-- a -g
„`m. -z ,
Segment Flow Rate (gpm),.
Line Length (ft)
Line Size ID 0n)5
0.731
2.174
6 Friction Headloss (ft)
0.073
0.217
Minor Losses (ft)
1,30
2.35
Line Velocity (ftls)
Supply Force Main Elevation Delta
174
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold'��°-'
6A-31_SM-3 Feed Manifold to Bottom Lateral
Headloss (ft) in manifold4Une
Length (ft) from Supply Manifold tc Bottom Feed Laterals
No
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (M)'
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
0.000
-49.000
0.000
-56.000
9 Total Segment Headloss (ft) = Fdction + Elev.
Return Force Main Friction Losses
6A-RM3to3B-SM1
Segment Flow Rate (gpm)
440
LineLength (ft)
Line Size ID (In.)
Minor Losses from Check Valve
5.261
Friction Headloss (ft)
2.78
2.78
Line Velocity (ft/s)
38-SM1 to 3B-SM2
Segment Flow Rate (gpm)
210
Line Length (ft)
_
Line Size ID (in.)
"
Minor Losses (ft)
0.515
- Friction Headloss (ft)
1.61
Line Velocity (fils)
3B-SM2 to W WTF
Segment Flow Rate (gpm)
2585
Line Length (ft)
_
- Line Size ID (in.)
Minor Losses (ft)
6.341
Friction Headloss (ft)
1.61
Line Velocity (ft/s)
Return Line Elevation Delta
0<
Elevation (ft) from Return Manifold to WWTF
'7 p.2 of3 90!20/2006
Brooks Engineering Associates, PA
',_ _)

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-3 SUSMANIFOLD 6ASM3
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
-05.7
546.7
-19.8
236.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
686'2
301'4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
200.0
86.6
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
WI PRV
Feet
PSI
uired (high pressure - 60 ps)
557.5
473'2
51.2
17.7
[NE:MAY
fold before PRV
(pressure at manifold - pressure loss required)
154.3
66.5lated
66.5115.5 50.0
ed
eck: P at Min. Flush Flow at Return Manifold_151.6
20.5
8.9
-65.6
t W WTF for Min. Flush Rate
157.5
68.2
heck: Emitter P on Bottom Lateral at Dose Flow
Note; Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to
return the flush.
p.3 of 3 10I20I2008
Brooks Engineering Associates, PA
J

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A31 Submanifold 6ASM4
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
10'3
490'7
4.4
212'4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
624.2
2702
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
254.0
110.0
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
ZONE SUMMARY WI PRV
Feet
PSI
485.6
512
loss required (high pressure - 60 psi)
473.2
17.7
at manifold before PRV
154.3
66.5
66.5
ng calculated (pressure at manifold - pressure loss required)
Leur
115.5
•:50 0
ng utilized
20,5
8.9
e Check: P at Min. Flush Flow at Return Manifold
-976
-42.3
ssure at WWTF for Min. Flush Rate
141.5
61.3
sure Check: Emitter P on Bottom Lateral at DOse Flow
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure
to return
the flush.
p.3 of 3 10120/2008
Brooks Engineering Associates, PA
_j

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-31 SUBMANIFOLD 6ASM5
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
72.3
428.7
31.3
185.6
Low Pressure Check: P at Min. Flush Flow at Return Manifold
570.2
246.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
306.0
132.5
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
ZONE SUMMARY WI PRV
Feet
PSI
431.6
51
Pressure loss required (high pressure - 60 psi)
473.2
117.7
Pressure at manifold before PRV
154.3
66.5
PRV setting calculated (pressure at manifold -pressure loss required)
115.5
-.=50.0
PRV setting utilized
20,5
8,9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
-45.6
-19.7
Flush Pressure at W WTF for Min. Flush Rate
149,5
64.7
Hi h Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure
to return the flush.
10/2012008
p.3 of 3
Brooks Engineering Associates, PA -
J

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d''87) (Q/C)' 85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
D Cl w Rate
8
e Re uired Flush Rate lus the ose
o32 6
Application Flow (gpm):12
6A•32
Min. Design Scour Vel. (ft/s) 2.0
s:
0.787
Tubing ID (in)h
Wuals
(in 0.79
: 0.62
Residual Flow for Scour (gpm2.30
���nr, +f+i 2
Req'd Flush Rate (gpm)8: 60.4
---!
Total Footae:
6350
Design Flow (gpm):
32.81
Supply Manifold Elev
6A-SM2
6A-RM2
Supply Manifold Elev.
Return Manifold Elev.
6A-SM1
6A-RM1
Return Manifold Elev
Dose
Lateral
Lateral
Min. Flush
a
Lateral Run
Run'
Elev.
Run
Len th # Emitters
Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (g m)8
1
42
0.4
530
2.7
5.0
r
43
0.4
44
0.5
44
0.5
45
0.5
47
0.5
2 7
48
0.5
646
3.3
5.6
8
50
0.5
g
53
0.5
10
56
0.6
11
57
0.6
[an
12
59
60
0.6
0.6
540
2.8
5.1
3
66
0.7
70
0.7
74
0.8
4 17
78
0.8
322
1.7
4.0
c�
18
':
83
0.9
94
1.0
400
j,
5 19
20
106
112
1.1
1.2
520
2.7
5.0
6 21
22
7 23
148
157
1.5
1.6
622
3.2
5.5
24
8 25
154
152
1.6
1.6
604
3.1
5.4
26
27
150
146
1.6
1.5
578
3.0
5.3
9
P8
143
140
1.5
1.4
552
2.9
5.2
10 29
30
136
1.4
i.J
11 31
128
1.3
502
2.6
4.9
32
123
67
1.3
0.7
534
2.8
5.1
F-1
12 33
34
57
0.6
35
t3
50
0.5
36
44
0.5
37
37
0.4
-;
_i
38
...
8360
12
3175
0.1
32.8
32.8
60.4
~
Brooks Engineering Associates, PA
p.1 of 3
10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
r-� p.2 of 3 10/20!2008
Brooks Engineering Associates, PA
;T j
ZONE 6A-32
TOP LOAD MANIFOLD PRESSURE ANALYSIS
'
INPUT
In its I Dose Flow fall Flush Flow (b)
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
to H.U-2
0.010
0.011
Friction Headloss (ft) from Pump
12.010
12.011
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
_
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to 313-SM2
t
_
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5.052
5.635
4 Friction Headloss (ft)
0.505
0.564
Minor Losses (ft)
1.78
1.89
_
Line Velocity (ft/s)
313-SM2 to 3B-SM1�:
Segment Flow Rate (gpm)�
--.!
Line Length (ft)
Line Size ID (in)5
0.410
0.456
'
5 Friction Headloss (ft)
Minor Losses (ft)
1
1.78
1.89
1.89
Line Velocity (ft/s)
.78
3B-SM1 to 6A-SM3
�. .
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
0.731
2.174
6 Friction Headloss (ft)
0.073
0.217
Minor Losses (ft)
1.30
2.35
Line Velocity (ft/s)
Supply Force Main Elevation Delta
18
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
Headloss (ft.) in drip system from supply manifold to return
manifold°�
....::
n rl
8 Total
6A -32 -SM -1 Feed Manifold to Bottom Lateral
j
Headloss (ft) in manifold°
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
�� r!
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral?
1.333
4.313
-'
9 Total Segment Headloss (ft) = Friction + Elev.
-41.667
-45.687
Return Force Main Friction Losses
�1
6A-RM3 to 3B-SM1�
Segment Flow Rate (gpm)
440
I'. +
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
5.261
Friction Headloss (ft)
2.78
Line Velocity (ft/s)
3B -SM 1 to 38-SM2
Segment Flow Rate (gpm)
210
Line Length (ft)
71
Line Size ID (in.)
Minor Losses (ft)
ow
0.515
i
Friction Headloss (ft)
1.61
Line Velocity (ft/s)
3B-SM2 to WWTF
%
" 1
Segment Flow Rate (gpm)
2585
Line Length (ft)<
Line Size ID (in.)
Minor Losses (ft)
�,.'��"
6.341
Friction Headloss (ft)
1.61
Line Velocity (ft/s)
Jj
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
3� +
r-� p.2 of 3 10/20!2008
Brooks Engineering Associates, PA
;T j

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-32 Submanifold 6A-SM1
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
143.3
357.7
62.0
154.9
Law Pressure Check: P at Min. Flush Flow at Return Manifold -
setting
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
215.1
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
496.8
383.0
165.8
Flush Pressure at backwash tank for Min. Flush Rate
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
PRV NEEDED? YES
ZONE SUMMARY WI PRV
Pressure loss required (high pressure - 60 psi)
Feet
358'2
473.2
1171.7
Pressure at manifold before PRV
PRV calculated (pressure at manifold - pressure loss required)
154.3
setting
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
115.5
23.5
Flush Pressure at WWTF for Min. Flush Rate
31 4
150.2.4
65.
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Note: Return Flush Tank needed. Flush Pressure at WWTF is too low. May not have sufficient pressure to return the flush.
10/20/2008
Brooks Engineering Associates, PA
p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
'total Headloss at Min. Flush Rate at Return Manifold
187.3
313.7
6t•t
135.8
Low Pressure Check: P at Min. Flush Flow at Return Manifold
442 8
191.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
427.0
184.8
Flush Pressure at backwash tank for Min. Flush Rate
115.5
P3.5
50.0'
10.2
PRV NEEDED? YES
75.4
32.6
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush
�n
F"1
�J
-a
i
I i
Brooks Engineering Associates, PA p.3 of 3
10/20/2008
304.2
51.2
Pressure loss required (high pressure - 60 psi)
473.2
117.7
Pressure at manifold before PRV
calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting
PRV setting utilized
115.5
P3.5
50.0'
10.2
Low Pressure Check: P at Min. Flush Flow at Return Manifold
75.4
32.6
Flush Pressure at WWTF for Min. Flush Rate
140.2
60.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush
�n
F"1
�J
-a
i
I i
Brooks Engineering Associates, PA p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
,t
Engineer's Notes &Instructions:
is to determine the pressures in the drip system
1. The purpose of this calculation spreadsheet
at critical points of interest. The governing criteria are:
'
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ftis is provided.
r
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
_
Footnotes
From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series
Curve.
1
(Flush flow is for single zone and Dose flow is for dual zones.)
..,_I
2 Headioss from pipe friction calculated from Hazen -Williams Equation: hr = (4.727 L/ d"'87) (Q C)f.es
3 From Wastewater Systems Inc. Data
--
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawinqs
6 Calculated from Q = VA
-�-1
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 E uals the Re wired Flush Rate lus the Dose Flow Rate
sss
Zone: 653 Application Flow (gpm :
2 0
"-
Laterals: 30 Min. Desi n Scour Vel. it/s
Tubin ID in
0 787
Tubin : 10 in0.79 0.62 Residual Flow for Scour ( pm)e
Emitters h :
2.30
Emitter S acin it2 Re 'd Flush Rate (gpmle:
126.6
Total Foota e: 11528
Desi n Flow m : 59.56.
_
Supply Manifold Elev.. ` 6BSM3
Return Manifold Elev. _".. 6B-RM3
_
Supply Manifold Elev. 6B-SM2
Return Manifold Elev. 6B-RM2
'1
Supply Manifold Elev.� 6B-SM1
_
Return Manifold Elev. _. - . 68-RM1
Dose Lateral Lateral
Min. Flush
Rung Run
Run Eley. Len th # Emitters Flow (gpm ° Length (ft) Dose (gpm)
Flow (gpm)a
Lateral
1 1 74 0.8 628 3.2
5.5
2 77 0.8
3 80 0.6
83 0.9
5 87 0.9 354 1.8
4.1
2
6 90 0.9
7 92 1.0 376 1.9
4.2
3
6 96 1.0
4 9 98 1.0 398 2.1
4.4
101 1.0
5 101 104 1.1 414 2.1
4.4
12 103 1.1
5 13 - 101 1.0 400 2.1
4.4
_,.
14 99 1.0
7 15 98 1.0 388 2.0
4.3
16 96 1.0
8 17 96 1.0 380 2.0
4.3
h rl
18 94 1.0
93 1.0 372 1.9
4.2
9 19
20 1 93 1.0
21 92 1.0 368 1.9
4.2
10
22 92 1.0
91 0.9 364 1.9
4.2
`l q.
11 23
24 91 0.9
12 25 91 0.9 364 1.9
4.2
26 91 0.9
13 27 90 0.9 360 1.9
4.2
28 90 0.9
14 29 69 0.9 356 1.8
4.1
30 89 0.9
15 31 88 0.9 352 1.8
4.1
32 68 0.9
88 0.9 350 1.8
4.1
16 33
34 87 0.9
87 0.9 348 1.8
4.1
...
17 35
36 87 0.9
86 0.9 $46 1.8
4.1
18 37
38 87 0.9
87 0.9 348 1.8
4.1
19 39
87 0.9
40
20 41 87 0.9 348 1.6
4.9
87 0.9
1 " 87 0.9 348 1.8
4.1
21 43
44 87 0.9
87 0.9 346 1.8
4.1
C n
22 45
46 86 0.9
85 0.9 340 1.S
4.1
23 47
48 85 0.9
-". 86 0.9 344 1.8
4.1
24 49
50 2j 86 0.9
86 0.9 342 1.8
4.1
25 51
52 85 0.9
83 0.9 328 1.7
4.0
26 53
54 81 0.8
27 55 80 0.8 316 1.6
3.9
---
56 78 0.8
75 0.8 592 3.1
5.4
28 57
58 74 0.8
59 74 0.8
60 73 0.8
29 6170 0.7 518 2.7
5.0
62 f 66 0.7
'"
63 . 63 0.7
_
64 �" 6o 0.6
30 65 4 58 0.6 440 2.3
4.6
p 56 0.6
-t
67 #� '_ 54 0.6
68 r` +54:= Y '1ff" a 52 0.5
11528 5764 59.6 59.6
128.6
10/20/2008
._.._.l
P.1 of 3
Brooks Engineering Associates, PA
�:J

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 613.33
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUTInputs
Dose Flow l 11 Flush Flowlb
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
from Pump to Hydraulic Unit'
Elevation (ft)
Line length (ft) from P.T. to H.U'
Line Size ID (in) s
Friction Headloss (ft) from Pump to H.U.
0.010
0.011
12.011
2 Total Segment Headloss (ft) = Friction + Elev.
12.010
Hydraulic Unit
H.U. Elev
;
3 Headloss from H.0 (ft.)3
Supply Farce Main Friction Losses
H.U. to 3B-SM2'€qqj,
Segment Flow Rate (gpm)
Line Length (ft)
-'
Line Size ID (in)'
tI
5.052
5.635
4 Friction Headloss (ft)
Minor Losses (ft)
1.78
1'78
1.89
1 .89
Line Velocity We)
3B-SM2 to 33 -SMI
Segment Flow Rate Wpm)
Line Length (ft)
35
Line Size ID (in)''
).410
0.458
5 Friction Headloss (ft)
Minor Losses (ft)
-
1.78
1.78
1.89
1 .89
Line Velocity (ft/s)
3B-SM1 to 6A-SM3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in) s
(Llziai
0.731
2.174
6 Friction Headloss (ft)
0.073
0.217
Minor Losses (ft)
1.30
2.35
Line Velocity (ft/s)
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
-174
Drip System Headloss Results
b`
�
8 Total Headloss (ft.) in drip system from supply manifold to return
manifold°
66 -33 -SM -1 Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
M
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID 0n)'
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
1.412
4.449
9 Total Segment Headloss (ft) = Friction + Elev.
-53.588
-57.651
Return Force Main Friction Losses
6A-RM3 to 3B-SM1
Segment Flow Rate (gpm)
440
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
_
5.261
Friction Headloss (ft)
2.78
Line Velocity (fus)
39-SM1 to 3B-SM2,"``
Segment Flow Rate (gpm)
210
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
0.515
Friction Headloss (ft)
1.61
Line Velocity (ft/s)
3B-SM2toWWTF
Segment Flow Rate (gpm)
2565
- Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
6.341
Friction Headloss (ft)
1.61
Line Velocity (ft/s)
Return Line Elevation Delta,,
Elevation (ft) from Return Manifold to W WTF
_
10/20/2008
p.2 of 3
Brooks Engineering Associates, PA
I 1

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 58.33 Submanifold 68SM1
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
`17.7
552.7
-20'7
239.3
Low Pressure Check: P at Min. Flush Flow at Return Manifold
700.6
03.4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
194.0
84.0
84.0
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
MMARY WI PRV
Feet
PSI
loss required (high pressure - 60 psi)
562.2
473.2
51.2
117.7
at manifold before PRV
154.3
66.5
ing calculated (pressure at manifold - pressure loss required)
EP'aa.0
115.5
50.0.
ing utilized
22 5
9.7
9.7
sure Check: P at Min. Flush Flow at Return Manifold
-161 6
-70.0
ssure at W WTF for Min. Flush Rate
162.1
70.2
ssure Check: Emitter P on Bottom Lateral at Dose Flow
Note: Return Flush Tank needed. Flush Pressure at VJWTF is too low. May not have sufficient
pressure to return
the flush.
'`, p.3 of 3 10/20/2008
Brooks Engineering Associates. PA
L_.,9

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 68-33 Submanifold 6BSM2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
18.3
7.9
210.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
486.7
274.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
634.8
260.0
112.6
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
ZONE SUMMARY W1 PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
496.2
51.2
17.7
Pressure at manifold before PRV
loss required)
154.3
154.3
66.5
66.5
PRV setting calculated (pressure at manifold - pressure
115.5
.SDA...
PRV setting utilized
22.5
9.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
-95.6
-41
Flush Pressure at WWTF for Min. Flush Rate
162.1
70.22
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient
pressure to return
the flush.
�.1
Brooks Engineering Associates, PA
p.3 of 10/20/2008
1

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6833 Submanifold6BSM3
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
64.3
440.7
2T8
190.8
Low Pressure Check: P at Min. Flush Flow at Return Manifold
568.8
246.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
312.0
135.1
Flush Pressure at backwash tank for Min. Flush Rate
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure -60 psi)
430.2
473.2
51.2
117.7
Pressure at manifold before PRV
loss required)
154.3
66.5
PRV setting calculated (pressure at manifold - pressure
115.5
50.0
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
22.5
9.7
18.9
Flush Pressure at W WTF for Min. Flush Rate
-43.6
142.1
61.5
61.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have
sufficient pressure to return
the flush.
Brooks Engineering Associates, PA
P.3 of 3 10/20/2008
!..—j

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
Brooks Engineering Associates, PA p.1 of 3 10/20/2008
all emitters operate between 7 and 70 psi,
24
0.2
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source
of either the calculations or the data inputs are indicated in the footnotes.
0.3
3. The inputs
for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1
From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2
Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4.17) (Q/C)t as
3
From Wastewater Systems Inc. Data
0.3
4
Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5
From Engineering Drawings
6
Calculated from Q = VA
7
Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8
Equals the Required Flush Rate Plus the Dose
Flow Rate
0.4
Zone: 48-34
Application Flow ( pm):
41.1
No. Laterals: 20
0.4
Min. Design Scour Vel. ft1s
2.0
Tubing: ID in 0.79
Tubing ID in
0.787
0.5
Emitters h : 0.62
3.1
Residual Flow for Scour (gpm)'
2.30
Emitter Spacing ft 2
53
Req'd Flush Rate (gpm)':
87.1
Total Footage: 7946
11
Design Flow (gpm): 41.05
1.0
Supply Manifold Elev.
j 4B-SM4
Return Manifold Elev.
- 4B-RM4
Supply Manifold Elev.
4B-SM3
Return Manifold Elev.
-, 4B-RM3
396
2.0
Supply Manifold Elev.
4B-SM2
Return Manifold Elev.
.t �;-. 4B-RM2
Run Run Dose Lateral Lateral
Min. Flush
LateralRun Elev. th # Emitters Flow (gpm)' Length (ft) Dose (gpm)
Flow (gpm)'
396
_Len
1 - 22 0.2 496 2.6
4.9
Brooks Engineering Associates, PA p.1 of 3 10/20/2008
24
0.2
27
0.3
29
0.3
31
0.3
34
0.4
38
0.4
�9
43
0.4
2
-
48
0.5
598
3.1
5.4
10
53
0.5
11
99
1.0
12
99
1.0
3 13
99
1.0
396
2.0
4.3
14
99
1.0
4 15
99
1.0
396
2.0
4.3
16
99
1.0
5 17
99
1.0
396
2.0
4.3
18
99
1.0
6 19
99
1.0
396
2.0
4.3
20
99
1.0
7 21
98
1.0
392
2.0
4.3
22
98
1.0
8 23
97
1.0
388
2.0
4.3
24
97
1.0
9 25
-
96
1.0
382
2.0
4.3
26
95
1.0
10 27
94
1.0
376
1.9
4.2
28
94
1.0
11 29
93
1.0
372
1.9
4.2
30
93
1.0
12 31
92
1.0
366
1.9
4.2
32
13 33
_
89
0.9
356
1.8
4.1
34
X89
0.9
14 35
89
0.9
354
..0
4.1
36
88
0.9
15 37
,$.:..
87
0.9
348
1.8
4.1
38
87
0.9
16 39
86
0.9
342
1.8
4.1
40
85
0.9
17 41
-
85
0.9
338
1.7
4.0
42
84
0.9
18 43
82
0.6
326
1.7
4.0
44
- ��
81
0.8
19 45
$=
79
0.8
314
1.6
3.9
46
78
0.8
20
75
0.8
614
3.2
5.5
61
0.6
53
0.5
'- -
";
47
0.5
39
0.4
32
0.3
7946
3973
41.1
41.1
37.'
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 413-34
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINEInputs
(a) Flush Flow (b)
1 Operating Head from Pump Curve'
NOW*
_ -
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.010
0.011
2 Total Segment Headloss (ft) = Friction + Elev.
12.010
12.011
Hydraulic Unit
H.U. Elev SIWO
3 Headloss from H.0 (ft.)s
Supply Force Main Friction Losses
H.U. to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s�
4 Friction Headloss (ft)
5.052
5.635
Minor Losses (ft)
0.505
0.564
Line Velocity (ft/s)
1.78
1.89
3B-SM2 to 3B-SM1
Segment Flow Rate (gpm)x..'�'
'rr�
Line Length (ft)
Line Size ID (in)s
5 Friction Headloss (ft)
0.410
0.458
Minor Losses (ft)
0.041
0.046
Line Velocity (ft(s)
1.78
1.89
3B-SM1 to 6A-SM3
Segment Flow Rate (gpm)
_
Line Length (ft)
Line Size ID (in)'
6 Friction Headloss (ft)
0.731
2.174
Minor Losses (ft)
0.073
0.217
Line Velocity (ft/s)
1.30
2.35
Supply Force Main Elevation Delta
-156
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return
manifold" FTF�-
4B-34-SM-2 Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals,
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
0.559
2.865
9 Total Segment Headloss (ft) = Friction+ Elev.
-40.441
-45.135
Return Force Main Friction Losses
6A-RM3 to 3B-SM1
MINOR
Segment Flaw Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
5.261
Line Velocity (ft/s)
2.78
3B -SMI to 3B-SM2
Segment Flow Rate (gpm)
,.y
Line Length (ft)
210
Line Size ID (in.)
Minor Losses (ft)
_
0.515
Friction Headloss (ft)
Line Velocity (ft/s)
1,61
3B-SM2 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
2585
,
Line Size ID (in.)
��'flPs _,
Minor Losses (ft)
6.341
Friction Headloss (ft)
Line Velocity (ft/s)
1.61
Return Line Elevation Delta
Elevation (ft) from Return Manifold to W WTF
52 :
'71
1[--t
Brooks Engineering Associates, PA p2 of 3 10/20/2008
',J- J

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4B-34 Submanifold 4B-SM2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
-32.7
-14.2
Low Pressure Check: P at Min. Flush Flow at Return Manifold
537.7
232.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
664.6
287.7
Flush Pressure at backwash tank for Min. Flush Rate
217.0
93.9
EEDED? YES
ZONE SUMMARY W1 PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
526.0
51.2
117.7
Pressure at manifold before PRV
468.2
154.3
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
PRV setting utilized
115.5
25.5
50.0
11.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at W WTF for Min. Flush Rate
-138.5
-60.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
148.9
64.5
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush
p.3of3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4B-34 Submanifold 4B-SM3
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
11.3
493.7
4.9
213.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold -
611.6
264.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
259.0
112.1
Flush Pressure at backwash tank for Min. Flush Rate
-96.6
-41.8
60.6
DEEDED? YES
ZONE SUMMARY WI PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
473.0
468.2
51.2
117.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
Low Pressure Check: P at Min. Flush Flow at Return Manifold
115.5
25.5
50.0
11.0
Flush Pressure at W WTF for Min. Flush Rate
-96.6
-41.8
60.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
139.9
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush.
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4B-34 Submanifold 4B-SM4
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
-32.7
537.7
-14.2
232.8
Low Pressure Check: P at Min. Flush Flow at Return Manifold
564.6
287.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
305.0
132.0
Flush Pressure at backwash tank for Min. Flush Rate
-50.6
148.9
-21
64.55
NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
526.0
468.2
51.2
7.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
6.5
66.5 66.5
utilized
PRV settling25.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
25.5
.0
11
11.0
Flush Pressure at W WTF for Min. Flush Rate
-50.6
148.9
-21
64.55
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush.
Brooks Engineering Associates, PA
p.3 of 3 10/20/2006

{- i

n
m
n

6.8 Rainfall data analyses for short term wet weather storage
requirements

310301 15 years
STATE CLIMATE OFFICE OF NORTH CAROLINA
NC CRONOS Database
Data retrieval from 310301- Asheville for 1970-01-01 thru 2007-05-17 (13651 days)
13,651 records for this period of record (100% data available)
*Stores design flow if temperature is < 32 F or Precip > 0.25.
*If there are suitable conditions on a day after a storage event. Twice the design flow is irrigated.
Design Flow Maximum Storage
200000 1,200,000
6 Days of storage
9 Days of storage with 1.5 safety factor

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Attachment A - Aqueonics Plant Cut -Sheets for: concrete mix design, railing, chemical
feed pumps, Parkson sand filter and air compressor, DuraPac trickling filter media,
Trojan UV, level controller & tranduscers, chemical feed pumps & pressure relief
valves.
Attachment B - Cut -Sheets & Pump Curves for WWTP Pumps:forward flow/recycle
pumps, sand filter flow pumps, equalization tank grinder pumps, sludge tank
decanting pump.
Attachment C - Cut -Sheets for WWTP Blowers
Attachment D - Cut -sheets and pump curve for Irrigation Dosing/Flushing Pump
Attachment E - Cut -sheets for flushing return pumps
Attachment F - Cut sheets for alternate pond liner
Attachment G - WSI PC Controller Electrical Schematics
Attachment H - Cut -sheets for drip system valving
Attachment I - Cut -sheets for Flow Meter
Attachment J - Cut -Sheets for Disc Filtration System
Attachment K -Cut-Sheets for Rainbird Rain Gauge
Attachment L — Drip Line Cut Sheets

Aqueonics Plant Cut -Sheets for: concrete mix design, railing, chemical feed pumps,
Parkson sand filter and air compressor, DuraPac trickling filter media, Trojan UV,
level controller & tranduscers, chemical feed pumps & pressure relief valves.
r-

MARION CENTER SUPPLY .
READY MIX CC}NCRE 1 E
P.O. BOX 173
MARION CENTER, PA 15759
( 724) 397-5505 Fax [phone]
WESSITE: WWW.MARICNCEN T ERSUPPLY,COM
DATE: 14 -Aug -08
::
CUSTOMER::.
Pte)
PPOJFCT: Treatment Plant
MATERl50URCE
ASTM TYPE Q09AGE
Cement. Cemex, Plttsburgh/Wampurn, PA
C-150 Illi n/a
EXE. Select- RM Excell Minerals, Sarver, PA
C114&1157 nia
Coarse Aggregate: Hansen Aggregates, Torrance, PA
C-33 #t57 n/a
Fine Aggregate. Glacial Sand & Gravel, Tarrtown, PA
C-33 A n/a
Water. Onsite Well
n/a potable rM
AIr,EntraI Wng: Master Builders Inc., MBAE M
C-260 n/a As Required
Water Reducer. Master Builders Inc., Pozzolith 20ON
C-494 A -B -D See Below
Retarder. Master Builders Inc,, Pozzolith 100XR
C-494 B -D See Below
Super Plasticdzier Master Builders Inc-, Glenium 3030 NS
C-494 A F As Required
Non Chloride Acc, Master Builders Inc., Pozzolity NO 534
C-494 C -E As Required
MIX DESIGN 4000 psi Air Entrained
Material Weight Gallons S.G, Volume
(Ibs,) (oto. ft.)
Cement 420 3.15 2.14
EXL Select - RM 140 290 0.77
Coarse Aggregate 1800 2.68 10.76
Flne Aggregate 1376 2.57 8.58
Water 195 23.41 1.00 3.13
Air 6.01,5% 5.000/0 1.62
TOTAL 3931 77.00
Slump (inches): 4 Maximum
Calculated Unit Weight (pcf): 145,60
Water / Ratio: 0.35
Marion Center Supply will not be held responsible for any type of cracking_ Cracking
is a natural thing which we have absolutely no control ever-
... ADMIXTURE NOTES "*w
1. At ambient temperatures below 75 degrees, 3 oz/cwt of 20ON
2. At ambient temperatures from 75 - 85 degrees, 3 ozico of f 10UR
of 1 R
$. At ambient temperatures above 85 degrees, 4 02Jcwt
7

E7 1-� X/'`!
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r
Valley City:
Cement
530 Ib
3.15 Sp Gr
62.4
2.70 ft3
Fly Ash
110 Ib
2.35 Sp Gr
62.4
0.75 ft3
Slag Cement
0 lb
2,35 Sp Gr
62.4
0.00 ft3
Gravel 57
840 Ib
2.64 Sp Gr
62.4
5.10 ft3
Gravel 8
560 Ib
2.64 Sp Gr
62.4
3.40 ft3
Concrete sand
1428 lb
2.64 Sp Gr
62.4
8.67 ft3
Water gl
34.00 283.22 lb
1 Sp Gr
62.4
4.54 ft3
Air
7% 1.89
1
1
1.89 ft3
6100
48 oz
AEA14
4 oz
NC
50 oz If Needed
Plastiment
15 cz If Needed
27.04 ft3
Comments:
water/cern coarse/fine cemlf/a total agg
agg cu.ft.
2828
640 1400.00
0.40 0.50
22% 40%
8.50

Cat 7.a S15.p-OnFitti.ngs 2/16104 12:39 PM Page 1
Hollaender Products are produced from only the highest
quality materials and feature proprietary fasteners
and design features.
Aluminum Alloy 535
• Nlost corrosive resistant aluminum casting alloy
available today
• High strength as cast
• Bright attractive burnished mill finish
• Conforms to ASTM 826 & 8979
Proprietary Internal/External Reverse Knurl Cup
Point Set Screw
• Knurl cup point design provides tremendous resist-
ance to loosening due to heavy vibration
• Full contact of paint greatly resists pull out and
rotational slip
• Conforms to FF -S-200, ANSI/ASME 813.3
Type CIG
The RailaendeP Advantage
• Speed of Installation — Studies have shown
significant cost savings when compared to the
cost of welded handrail and other structures
• Ease of installation — Only tools required are a
saw, hex key and tape measure
• flexibility — Cast fittings can be used with galva-
nized steel, aluminum, stainless steel and black
iron pipe
• Reusability — Structures fabricated with
Hollaender fittings can easily be disassembled
and reconfigured
The Rib" Design . .
Holleender'O
Speed -Rail"
Mu -Rail"
Sneed-RailO II
Rackmaster'o
Mend -A -Rail"
Interna -Rails
Bumble Beee
All are registered trademarks of the
Hollaender Manufacturing Company.
Call Toil Free; 800 -772 -an = wwvr,hollaenderxam
• Strength — Railing systems can be designed using
standard Hollaender products to meet any building
code. Please refer to Technical Section of Catalog,
wvvw.hi)llaender.com or call our engineers.
• Time Tested — Products are backed by over 50
years of experience
RailaendeP isotopes Ills waPlds best known hrands
Speed -Rail'
inline design has become the benchmark for quality
throughout the industry.
NU -Rail'
Offset design of heavier duty structural fittings allows
multiple pieces of pipe to cross, minimizing number
of cuts.
Rackmaster'
Heaviest duty line developed for the construction of
rack systems.
Mend -A -Rail'
Ideal for repairing broken welds on existing pipe
structures.
Speed -Rail" 11
Patented modular fitting system which easily allows
for additions and changes to existing structures
without having to entirely disassemble.
Applicailons ape limited only by the inmginallon
Handrails & guardrails, playgrounds and carts,
store fixtures, offshore petrolchemical, industrial
plants, racking systems, warehouses, health &
medical buildings, portable structures, recreational
areas, amusement parks, film industry, government
facilities & public works, displays, and much,
much more.
Instant Structures'

Cat 1A Slip-OnFittings 2116(04 12:39 PM Page 2
Your Handrail Source.
I'v'spoilcal 41.0118ende" Wun R"11801RIUMS
speed- or + speed -nor u * Nome * Racimaster®
Call Tali Free: 809-7724300 = vumhollaender.com
I'TheFMW lith theRib"'

Cat lA Slip-OnFit rings 2/16/04 12:39 PM Page 3
I.P.S. Size item Number
3/4' 15000
/a 17000
1-1i2° 18000
Companenu: Iil ido. 99C
111 No. 2S8
I.P.S. Size item Number
31,1° 05020
} ° 06020
47020
2✓• 09020
I.P.S. Size Item Number
1.1/4" 07030
1-1/2° 0"0036
I.P.S. Size Item Number
314"
05040
1"
06040
1•t!4'
07040
}-1/2
08040
2^
09040
I.P.S. Size Item Number
3/4` 05050
}" 06054
1.114' 07056
Call Toll Free: 800-7724800. is ww,bollaender.catn
Now&
Your Handrail Source.
I.P.S. Size Item Numher
3/4° DSD6D
06060
t_1Jq^ 07060
..___. 1•in' 08066
"TheFzthaag teeth the Rib
I.P.S. Size Item Number
1-114° 07080
1.112^ 08080
i.P.S. Size item Numher
3/4'
05090
1^
06090
1•ij4"
07090
1-i12°
00090
2"
09090

Cat 1A Slip-onFitcinas 2/16/04 12:39 PM Page 4
ME I.P.S. Size Item Number
I.P.S. Size Nem Number
1.112' 10020
Components: (1) No. 7S6
11 No. 2SB
u ,a: I.ES. Stize Item Number
ii
3/4" 85120
06120
r
� 1.1/4° 07120
r
00120
a
I.P.S. Size Item Number
314' 05130
z 1" 06130
09130
2' 09130
I.P.S. Size Item Number
314" 05140
a 1' 06140
�'`;f : r`..
R 3. ,
a r ) 7 1-1;2' 08140
ux
2' 09146
C a I I ToII Free: 800-772.8300 + m m hallaender,cn in ,The Failing with the Rib"'
I.P.S. Size Item Number
3/4'
05150
1'
as15a
1-1l4'
07150
I -t/?'
06150
I.P.S. Size Item Number
314'
05160
i"
06160
1-1/a•
07160
I2'
06160
I.P.S. Size Item Number
314"
05170
1'
06170
1.114°
07170
1.1%2"
00170
I.P.S. Size item Number
r G616G
1-1l4° 07100
1.112' 06150

Cat 1A slip-CnPictings 2/16/04 12:39 PM Page 8
!.?S. Size item Number
314'
05450
1,
06450
1_i/d'
07450
1.114"
00450
I.P.S. Size Item Number
I-lld' 17150
1-1/2' 10150
I.P.S. Size Item Number
3/4'
05520
1"
06520
(d'
07520
1.114"
00520
2^
09520
I.P.S. Size
Item Number
3/4'
05530
1^
06530
i-Ud'
67530
08530
2'
09530
[M caps rot included
,,The Fmtw Mth the MY"
I.P.S. Size Item Number
3/4" 05600
i" 06600
1.114' 07600
1-112' 08600
2` 09600
I.P.S. Size
Item Number
3/4°
05610
V
06610
1.114"
07610
1-1/Y
08610

Cat 3A Flanges 2/16/01 12:49 PM Page 1
Or
ss
Your Handrail Source.
Gal[ T,qIt Free: wo-71mam * wu ut.hallaender.com
��
f3ss�es
Hollaender offers an extensive line of flanges for
mounting handrail, guardrail, and other pipe structures.
These flanges are available in all The optional
finishes. Selecting the right flange becomes extremely
important in all handrail applications. To aid in the
selection process, please refer to the chart on the
following page, and dimensional drawings on the
subsequent pages.
our engineering staff is available to answer questions
regarding the appropriate hardware. Concrete
anchors and machined bolts may be ordered to
complete the handrail system. Niany applications
require toeplete. (Refer to Tech information section,
building codes and OSHA standard pipe railing fnr
requirements.)
Refer to our accessories section for our toeplate and
toeplate brackets. Please refer to our web page at
www.hollaendercom for additional technical support.
Or
ss
Your Handrail Source.
Gal[ T,qIt Free: wo-71mam * wu ut.hallaender.com

-76
Sulzer CompaXTm
The space -saving » tior
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Sulzer CompaX is the name for the new, space -saving
and efficient solution to your mixing problems in the
turbulent flow regime. In comparsion to conventional
static mixer configurations, the Sulzer CompaX has
an amazingly reduced overall length. This greatly im-
proves your operational flexibility and reduces installa-
tion costs. Further more the additive can be admixed in
an easy and reliable way.
Functional description
The patented Sulzer CompaX design consists of a
highly efficient mixing device with integrated dosing in-
let point. The additive is fed into the zone where strong
turbulent flow prevails.
This design secures homogeneous mixing over a very
short distance with the use of only one mixing element
and with only one additive dosing point.
The Sulzer CompaX is patented technology.
Field of application
The Sulzer CompaX is widely used for the inline mixing
of liquids, gases and suspensions in the turbulent flow
regime.
outstanding features
The following features make the Sulzer CompaX an
advantageous and efficient solution to your mixing
needs:
• very short mixing distance: independent,of
_ mixing ratio, a homogeneous mixture is achieved
only 3 pipe diameters downstream of the mixer
• low pressure drop (typical;y i 0 —100 mbar)
• extremely short overall installation length
(approx. 0.3 pipe -0)
• easy to fit, low installation costs
• simple dosing of additive: no multipoint dosing
system necessary
• no clogging (both in the main flow and in additive
_ stream)
• robust construction, no moving parts
• easy to clean
• excellent price/performance ratio

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1 1 suszer L:ornpaA
Homogeneity data
• 1 : 2000
• 1:100
1:20
1
5
1
0 2 8 10 11
4 6
UD 1-1
Applications
There are many potential application areas for the Sulzer
CompaX:
• concentration and temperature equalisation of low -
viscosity liquids and gases
• mixing of additives
• dilution of concentrates
• water and wastewater treatment (adjustment of pH
value, mixing of flocculation agents, neutralisation
processes using acids or caustic solutions)
• concentration- and flow equalisation for an accurate
representative sampling from a single point down-
stream the mixer
• etc.
1
0,3 0,5 1
Velocity (m/s)
5
Design features
The Sulzer CompaX consists of a mixer with an inte-
grated dosing point. The dosing point is designed for
the mixing of an additive into a primary stream at ratios
ranging from 1 to 3.
The mixer is installed in the pipe, mounted between two
flanges (DIN 2633 or ANSI B16.5). The overall installa-
tion length is equivalent to less than half of the actual
pipe diameter.
Sulzer CompaX is available in the following materials:
• Stainless steel (1.4571)
• Polypropylene (PP)
• FRP for diameters > DN 500
• following other materials on request
PVC, PTFE, SS-ETFE coated
For mixing ratios > 1 to 3 and nominal diameters
DN > 100 mm flanged versions are available.
Pressure rating: Stainlesssteel = 16 bar @ 120 °C
PP = 10 bar @ 20'C

Headquarters
Sulzer Chemtech Ltd
P.O. Box 65
8404 Winterthur, Switzerland
Phone [phone]
Fax [phone]
[e-mail]
www.sulzerchemtech.com
North and South America
Sulzer Chemtech USA, Inc.
4019 South Jackson Avenue
Tulsa, OK 74107, USA
Phone [phone]
Fax [phone]
Asia Pacific
Sulzer Chemtech Pte. Ltd.
10 Benoi Sector
Singapore 629845
Phone [phone]
Fax [phone]
Sulzer Chemtech Ltd, a member of the Sulzer Corporation, with head- The activity program comprises:
quarters in Winterthur, Switzerland, is active in the field of process engi- . Process components such as trays, structured and random
neering and employs some 2500 persons worldwide. packings, internals for separation columns and reaction technology
Sulzer Chemtech is represented in all important industrial countries and . Engineering services for separation and reaction technology such
sets standards in the field of mass transfer and static mixing with its as optimizing energy consumption, plant optimization studies,
advanced and economical solutions. pre -engineering for governmental approval, basic engineering
• Separation and purification of organic chemicals by means of
crystallization and membranes
• Mixing and reaction technology with static mixers
• Mixing and Cartridges Technology
• Tower field services
23.13.06.40 - 11.08 - 50 - Printed in Switzerland

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®ZPARKSON CORPORATION
DynaSanc? Filter
DSF 19FT2 DBTF SS
SALES DRAWING
003758-01
PROJECT NAME SHEET NUMBER:
1 OF 1
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UNLESS OTHERWISE SPECIFIED SIGNATURES DATE
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DIMENSIONS ARE IN FEET DRAWN: F. J. CAMARGO 11-2-98
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AND INCHES
CHECKED: P. TATASCIORE 10-2-98
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DATE: 3-22-99 BY: F. J. CAMARGO CHECKED: P. TATASCIORE
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APPtiOVED: P. TATASCIORE DESCRIPTION
M FLW SV Baur x FSR
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MODIFIED MODIFIED BASE PLATE AS SHOWN
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®ZPARKSON CORPORATION
DynaSanc? Filter
DSF 19FT2 DBTF SS
SALES DRAWING
003758-01
PROJECT NAME SHEET NUMBER:
1 OF 1
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NEMA Premium" Bald®r 5.0 horsepower totally enclosed, fan -cooled, electric
motors. Specifications: EM3615T
Catalog Number:
EM3615T
Specification Number:
36G271T031
Horsepower:
5
Voltage:
230/460
Hertz:
60
Phase:
3
Full Load Amps:
13/6.5
Usable at 208 Volts:
13.6
RPM:
1750
Frame Size:
184T
Service Factor:
1.15
Rating:
40C AMB -CONT
Locked Rotor Code:
K
NEMA Design Code:
B
Insulation Class:
F
Full Load Efficiency:
90.2
Power Factor:
80
Enclosure:
TEFC
Baldor Type:
3643M
DE Bearing:
6206
ODE Bearing:
6205
Electrical Specification Number:
36WGT031
Mechanical Specification Number:
36G271
Base:
RG
Mounting:
F1

RASCHIG GmbH
Mundenheimer Strasse 100
67061 Ludwigshafen - Germany
Phone: [phone]
Fax: [phone]
_=
email: [e-mail]
www.raschig.de
Locations/Production Sites
Ludwigshafen and
Espenhain, Germany
Houston, Texas
El Dorado, Kansas
Monterrey, Mexico
,._
crossflow and vertical
flow PVC sheet media for trickling filters,
submerged fixed beds and other
wastewater treatment applications
DURA -PAC is a self-
supporting PVC sheet
media, capable of
withstanding loads
in excess of industry
standards. DURA -PAC
modules are available
in various sizes and
specific surface areas
of 30, 31, 48 or 68 ft2/ftp.
DURA -PAC is a plastic sheet media
available in two basic designs. DURA -PAC
XF is a cross flow media recommended
for low to medium BOD loading
applications. DURA -PAC VF is a vertical
flow media recommended for high BOD
loading applications. DURA -PAC's
volumetric void ratios of at least 95% allow
for uniform redistribution of wastewater
and air while maximizing contact between
the biomass and the wastewater.
DURA -PAC is available in specific surface
areas of 30, 31, 48 and 68 ft2/ft3. 31 ft2/ft3
media is typically used for BOD removal
and 48 ft2/ft3 media can be used for
nitrification to reduce the size of new
nitrifying trickling filters.
The DURA -PAC media is non-toxic to
microorganisms and immune to rot. It
is resistant to degradation by ultraviolet
light, fungi, bases and acids, and other
compounds normally found in wastewater.
DURA -PAC consists of thermoformed flat
PVC sheets. Sheets are sized in varied
thicknesses indexed to applications. For
cross flow applications (DURA -PAC XF)
these sheets are corrugated horizontally
and bonded to one another in a
honeycomb pattern module. Vertical flow
media modules (DURA -PAC VF) are
formed by alternating flat and corrugated
sheets. DURA -PAC modules typically
measure 2'x 4'x 2'. Custom module
sizes are available. DURA -PAC sheets
can also be shipped to the job site for
assembly, if the application requires.
DURA -PAC is one of five trickling filter
media designs from Jaeger
Environmental. Jaeger Environmental has
manufactured trickling filter media since
1979, with system installations worldwide.
We offer random and structured media for
municipal and industrial applications.
Product specifications for DURA -PRC
are detailed on the reverse side of this
presentation. For further information,
or to discuss your application, contact
Jaeger Environmental via phone, fax or
e-mail.

A, Standard Product Specifications
1. The media shall be fabricated from rigid PVC
sheets completely corrugated forming a
cross -corrugated pattern with adjacent sheets
to permit continuous horizontal redistribution
of both the air and wastewater throughout the
depth of the media. The PVC roll stock sheets
shall be of uniform thickness with no sections
less than t 0.002 inch manufacturing
tolerance. The media shall be specifically
designed for use in the biological oxidation
of municipal and industrial wastewater.
2. The polyvinyl chloride used in the media shall
be resistant to degradation from ultraviolet
radiation, rot, fungi, bacteria and other forms
of microorganisms. The media shall be
chemically resistant to concentrations of
common inorganic mineral acids or alkalies
and organic solvents or compounds normally
experienced in sewage.
3. Each module shall consist of several
PVC sheets, bonded together to form a
structurally self-supporting block measuring
24" wide x 24" high x 48" or 72" long. The
modules shall be designed with a minimum
specific surface area of 30 (or 31, 48 or 68)
square feet per cubic foot with a minimum
95% void volume ratio. Each module shall
be capable of withstanding a minimum load
of 35 pounds per square foot per foot of
media depth. Maximum allowable deflection
shall be limited to 2%.
4. The manufacturer shall submit test reports
for the mil thicknesses to be supplied.Test
reports shall comply with the requirements
of paragraph C. If there are no test reports
or if there are any alterations to the media
in respect to materials or design, the
manufacturer shall test the modules in
accordance with paragraph C.
5. Individual sheets used in the manufacture
of the media shall conform to commercial
standards ANSIIASTMD1784-78:12454C with
the following physical properties when tested
in accordance with the method indicated:
B. Installation
1. The media shall be placed inside the filter by
crane or mechanical conveyor. The media
modules shall be transported by cranes or
placed on wooden slides or conveyors to the
working level. Thel media modules shall be
placed by hand in their final location.
2. Use 1/2 inch thick plywood, pegboard or other
suitable temporary planking to protect the
media from foot traffic. Do not allow workers
to directly walk or stand on the media.
3. Place each module as close as possible to
each other while avoiding damage to the
modules. The sheets of all modules in a layer
shall be placed parallel to each other in order
to maximize uniform and continuous horizontal
movement of air and water.
4. Modules in each layer shall be rotated 90°
to the layer immediately below to enhance
water redistribution and to maximize
self-supporting of the media.
5. The media modules shall be carefully
trimmed or cut to fit within 2 inches (50.8 mm)
or less of the center column. Cut or trim
modules to fit within 2 inches (50.8 mm) or
less of the filter perimeter wall.
6. Shaping, trimming and cutting of the media
may be done in the filter provided appropriate
measures are taken to prevent any chips,
broken pieces or similar debris from falling
into the media. Canvas or similar working
materials shall be used to cover the media
modules. Before a new layer of modules is
added, the existing layer shall be cleared of
all construction material or objects that may
have fallen on it. The top layer of media shall
also be protected from damage caused by
falling material due to any subsequent work
until start-up of the system.
7. The media modules in the bottom layer shall
be placed on the supports provided. Support
ledge (a minimum of 4 inches wide) should
be provided around the center column and
the tank perimeter wall. The top of the support
beams and ledges should be at the same
elevation and within a maximum tolerance
of t 1/8 inch (3.18 mm) in their elevation.
Properties
Test Method
Results
A. Tensile Strength (psi)
ASTM D-638/882
4,000-8,000
B. Tensile Modulus
ASTM D-638/882
300,000-550,000
C. Modulus of Elasticity (psi)
ASTM D-746
Min 325,000
D. Impact Strength (ft-Ib/in of notch)
ASTM D-256
1.0-5.0
E. Gardner Impact
ASTM D-4226
Proc.A 0.8in. Ib./mil
F. Heat Distortion Temp (°F@264 psi)
ASTM D-648
155 — 170° F
G. Izod Impact (ft-Ib/in)
ASTM D-256
0.5-2.2
H. Maximum Service Temp
135" F
1. UL Flammability
94
V-0
J. Specific Gravity
ASTM D-792
1.3 - 1.5
K. Resistance to Grease, Fats & Oils
ASTM D-722
Excellent
L. Resistance to Acids & Alkalies
ASTM D-534
Excellent
M. Flammability
ASTM D-635
<5 secs, <5mm burn
DURA -PAC Is Represented By:
@ 2366 Durapac Flyer 08/07
C. Module Testing
1. Structural testing of fabricated modules shall
be performed by an independent testing
laboratory approved by the engineer.
2. All tests shall simulate service conditions and
conform to the following criteria.
a. The test samples shall consist of a stack
of modules at least two modules high. The
arrangement of the stack shall simulate
the geometry as placed in the filter towers.
b, Modules intended for the base layer shall
be tested on a simulation of the support
system. Modules intended for all other
layers shall be tested on a flat base.
c. Test loads shall be the design loads of the
media specified.
d. The test load shall be uniformly applied at
a temperature of 75° F, (t 2° F) and the
design load shall be applied as follows:
1. A pre -load, equal to 10 percent of the
design load, shall be applied for 1 hour
to seat modules and to establish a
baseline flexural condition.
2, The loading shall be increased in 100 -
pound -per -square -foot intervals. Each
loading shall be held for a minimum of
5 minutes and the deflection recorded
at the end of the 5 -minute period.
3. Incremental loading shall continue until
recorded deflections are 1 percent and,
subsequently, 2 percent.
e. Maximum allowable compressive deflection
of the individual modules shall be 2
percent.
f. if more than 10 percent of the modules
tested in any strength gradation exhibit
a compressive deflection of greater than
2.0 percent, or if any one module exhibits
a deflection greater than 4.0 percent,
additional testing may be required as
considered necessary to determine the
structural suitability of the media. If the
tests indicate the media is structurally
unsuitable for its intended use, the media
may be replaced with new media meeting
the specifications and passing the
structural testing.
D. Product Handling And Storage
1. If storage is required, assembled media
modules shall be stored on a fiat, clean
surface to prevent damage to the module
edges.
2. Modules should be checked at least once per
week. Modules that may have fallen shall be
inspected for any damage and undamaged
modules should be restacked and secured.
Damaged modules should be either repaired
or discarded.
3. During shipment and storage, modules shall
always be stacked on their long face with the
plastic sheets in a vertical position. Modules
shall not be stacked more than four high,
and modules in each layer shall be set at
right angles to those below. Weathered or
otherwise damaged media are not acceptable
and will be replaced as deemed necessary or
appropriate,
E. Cleaning
As installation of each module layer is completed
modules surfaces should be inspected for the
presence of debris or other construction materials.
Any foreign material detected should be removed
and all surfaces cleaned. Upon completion of the
media installation, a final check of the media
surface should be conducted for the presence of
foreign material and any material detected
removed prior to the application of water. Following
completion of the inspection and the removal of all
foreign material, the media should be thoroughly
flushed with clean water.

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Siemens AG 2008
Continuous level measurement Ultrasonic controllers
Overview 1, Application
I t
Benefits
• Monitors wet wells, weirs and flumes
• Digital communications with built-in Modbus RTU via RS -485
• Compatible with SmartLinx system and SIMATIC PDM config-
uration software
• Single or dual point level monitoring
• 6 relay (standard), 1 or 3 relay (optional)
• Auto False -Echo Suppression for fixed obstruction avoidance
• Anti -grease ring/tide mark buildup
• Differential amplifier transceiver for common mode noise re-
jection and improved signal-to-noise ratio
• Wall and panel mounting options
7
'J
For water authorities, municipal water and wastewater p an s,
HydroRanger 200 is an economical, low -maintenance solution
delivering control efficiency and productivity needed to meet to
day's exacting standards. It offers single point monitoring with all
models, and optional dual -point monitoring with i 6 relay model.
As well, it has digital communications with built-in Modbus RTU
via RS -485.
The standard 6 relay HydroRanger 200 will monitor open chan-
nel flow and features more advanced relay alarming and pump
control functions as well as volume conversion. It is compatible
with SIMATIC PDM allowing for PC configuration and setup.
Sonic Intelligenced advanced echo -processing software pro-
vides increased reading reliability. The optional 1 or 3 relay mod-
els provide accurate level measurement functions only; these
two models do not provide open channel flow, differential level
measurement or volume conversion functions.
HydroRanger 200 uses proven continuous ultrasonic echo rang-
ing technology to monitor water and wastewater of any consis-
tency up to 15 m (50 ft) in depth. Achievable resolution is 0.1 %
with accuracy to 0.25% of range. Unlike contacting devices,
HydroRanger 200 is immune to problems caused by suspended
solids, harsh corrosives, grease or silt in the effluent, reducing
downtime.
• Key Applications: wet wells, flumes/weirs, bar screen control
Siemens FI 01 '2009

© Siemens AG 2008
Conti11 nuous level measurement Ultrasonic controllers
Discrete
10 to 50 V DC switching level
us r
Logical 0 = < 0.5 V DC
DC version
12 to 30 V DC (20 W)
Design
Technical specifications
—
Weight
Mode of Operation
• Wall mount
Measuring principle Ultrasonic level measurement
. Panel mount
Measuring range 0.3 to 15 m 0 to 50 ft), transducer
Material (enclosure)
dependent
Compatible transducers: ST -H
F and G, Class III (wall mount
Degree of protection (enclosure)
Measuring points 1 or 2
• MCERTS Class 1 approved for
• Wall mount
Input
Analog 0 to 20 mA or 4 to 20 mA, from
• Panel mount
alternate device, scaleanle (6
Cable
relay model)
—'
Transducer and mA output signal
Accuracy
Error in measurement
Resolution
Temperature compensation
Rated operating conditions
Installation conditions
Location
Installation category
Pollution degree
Ambient conditions
Ambient temperature (enclosure)
,_ Siemens FI 01 • 2009
0.25% of range or 6 mm (0.24"),
whichever is greater
0.1 % of measuring range or 2 mm
(0.08"), whichever is greater3)
• -50 to +150 °C (-58 to +302 °F)
• Integral temperature sensor in
transducer
• External TS -3 temperature sen-
sor (optional)
• Programmable fixed tempera-
ture values
Max. separation between trans-
ducer and transceiver
1.37 kg (3.02 Ins)
1.50 kg (3.31 lbs)
Polycarbonate
IP65/Type 4X/NEMA 4X
IP54/Type 3/NEMA 3
2 -core copper conductor, twisted,
shielded, 300 Vrms, 0.82 mma
(18 AWG), Belden© 8760 or
equivalent is acceptable
365 rn (1200 ft)
Displays and controls 100 x 40 mm (4 x 1.5") multi-orocK
LCD with backlighting
Programming Programming using handheld
programmer or via PC with
SIMATIC PDM software
Power supply"
Discrete
10 to 50 V DC switching level
100 to 230 V AC - 15%, 50/60 Hz,
Logical 0 = < 0.5 V DC
DC version
12 to 30 V DC (20 W)
Logical 1 = 10 to 50 V DC
• CE, C-TICK6)
Max. 3 mA
Output
--,
Echomaxo" transducer
44 kHz
Ultrasonic transducer
Compatible transducers: ST -H
F and G, Class III (wall mount
and Echomax series XPS-10/10F,
• MCERTS Class 1 approved for
XPS 15/15F, XCT-8, XCT-12 and
Open Channel Flow
XRS-5
y
RelaysI
Rating 5 A at 250 V AC, non-
-
`
inductive
1
Model with 1 relay2)
1 SPST Form A
Model with 3 relays2)
2 SPST Form A/1 SPDT Form C
3 _
Model with 6 relays
4 SPST Form A/2 SPDT Form C
�
mA output
0to20mAor4to20mA
• Max. load
750 0, isolated
• Resolution
0.1 % of range
Accuracy
Error in measurement
Resolution
Temperature compensation
Rated operating conditions
Installation conditions
Location
Installation category
Pollution degree
Ambient conditions
Ambient temperature (enclosure)
,_ Siemens FI 01 • 2009
0.25% of range or 6 mm (0.24"),
whichever is greater
0.1 % of measuring range or 2 mm
(0.08"), whichever is greater3)
• -50 to +150 °C (-58 to +302 °F)
• Integral temperature sensor in
transducer
• External TS -3 temperature sen-
sor (optional)
• Programmable fixed tempera-
ture values
Max. separation between trans-
ducer and transceiver
1.37 kg (3.02 Ins)
1.50 kg (3.31 lbs)
Polycarbonate
IP65/Type 4X/NEMA 4X
IP54/Type 3/NEMA 3
2 -core copper conductor, twisted,
shielded, 300 Vrms, 0.82 mma
(18 AWG), Belden© 8760 or
equivalent is acceptable
365 rn (1200 ft)
Displays and controls 100 x 40 mm (4 x 1.5") multi-orocK
LCD with backlighting
Programming Programming using handheld
programmer or via PC with
SIMATIC PDM software
Power supply"
AC version
100 to 230 V AC - 15%, 50/60 Hz,
36VA(17W)
DC version
12 to 30 V DC (20 W)
certificates and approvals
• CE, C-TICK6)
• Lloyd's Register of Shipping
• ABS Type Approval
• FM, CSANRTLIC, UL listed
• CSA Class I, Div. 2, Groups A, B,
C and D, Class Il, Div. 2, Groups
F and G, Class III (wall mount
only)
• MCERTS Class 1 approved for
Open Channel Flow
communication • RS -232 with Modbus RTU or
ASCII via RJ -11 connector
• RS -485 with Modbus RTU or
ASCII via terminal blocks
• Optional: SmartLinxO" cards for
PROFIBUS DP
- DeviceNejm
Allen-Bradley Remote 1/0
t) All relays certified for use with equipment that fails in a state at or under the
rated maximums of the relays
indoor /outdoor
) This model is level control only; no open channel flow, differential level or
II volume conversion functions
3) Program range is defined as the empty distance to the face of the trans -
4 ducer plus any range extension
4) Maximum power consumption is listed
s) EMC performance available upon request
-20 to +50 °C (-4 to +122 `F)

Siemens AG 2008
Power supply
100 to 230 V AC
12 to 30 V DC
Number of measurement points
Single point model, 6 relays
Dual point model, 6 relays
Single point model, level only, 1 relay2)
Single point model, tel only, 3 relays2)
mu
Comnlcation (SmartLinx)
Without module
SmartLinx© Allen-Bradley© Remote 1/0 module
SmartLinx PROFIBUS DP module
SmartLinx DeviceNetTM module
See SmartLinx product page 5/260 for more infor-
mation.
Approvals
General Purpose CE, FM, CSAus/c, UL listed,
C -TICK
CSA Class I, Div. 2, Groups A, B, C and D; Class 11,
Div 2, Groups F and G; Class III (for wall mount
applications only)
Please add "-Z" to Order No. and specify Order
code(s).
TS -3 Temperature ensor - s
A SITRANS RD100 Remote display - see RD100 on
B page 5/263
SITRANS RD200 Remote display - see RD200 on
page 5/265
a'
1 !;
2
3•
t
2
Order code
Stainless steel tag [69 mm x 50 mm (2.71 x 1.97")): Y15
Measuring -point number/identification (max. 16
characters) specify in plain text
s?cr t ?;= r„ri z;irsa
Order No.
C) 7ML1998-5FC03
English
French
Continuous level measurement Ultrasonic controllers
German
C) 7ML1998-5FC32
Note: The instruction manual should be ordered as
5
a separate line on the order.
an
woa
Selection and Ordering data
order No. Selection and Ordering data Order No
C)
7 M L 5 0 3 4- Siemens HydroRanger 200 C) 7 M L 5 0 3 4-
Siemens HydroRanger 200
ller for u to six pumps that
l levecontroller p
Ultrasonic t
Ultrasonic level controller for up to six pumps that
� control, differential control and open
"" "`
provides control, differential control and open
provides
channel flow monitoring. The HydroRanger 200 is
channel flow monitoring. The HydroRanger 200 is
also available as a level measurement controller
also available as a level measurement controller
only. Select option from model code below.
only. Select option from model code below.
C) 7ML1998-iBti02
Mounting
1 Handheld programmer 7ML1830-2AK
Wall mount, standard enclosure
Tag stainless steel, 12 x 45 mm (0.47 x 1.77'), one 7ML1930-IAC
Wall mount, 4 entries, 4 M20 cable glands included
2
text line, suitable for enclosure
3
Panel mounts)
- --
See TS -3 on page 5/147
Power supply
100 to 230 V AC
12 to 30 V DC
Number of measurement points
Single point model, 6 relays
Dual point model, 6 relays
Single point model, level only, 1 relay2)
Single point model, tel only, 3 relays2)
mu
Comnlcation (SmartLinx)
Without module
SmartLinx© Allen-Bradley© Remote 1/0 module
SmartLinx PROFIBUS DP module
SmartLinx DeviceNetTM module
See SmartLinx product page 5/260 for more infor-
mation.
Approvals
General Purpose CE, FM, CSAus/c, UL listed,
C -TICK
CSA Class I, Div. 2, Groups A, B, C and D; Class 11,
Div 2, Groups F and G; Class III (for wall mount
applications only)
Please add "-Z" to Order No. and specify Order
code(s).
TS -3 Temperature ensor - s
A SITRANS RD100 Remote display - see RD100 on
B page 5/263
SITRANS RD200 Remote display - see RD200 on
page 5/265
a'
1 !;
2
3•
t
2
Order code
Stainless steel tag [69 mm x 50 mm (2.71 x 1.97")): Y15
Measuring -point number/identification (max. 16
characters) specify in plain text
s?cr t ?;= r„ri z;irsa
Order No.
C) 7ML1998-5FC03
English
French
C) 71VIL1998.5FC11
German
C) 7ML1998-5FC32
Note: The instruction manual should be ordered as
a separate line on the order.
This device is shipped with the Siemens Milltronics
manual CD containing the complete ATEX Quick
Start and instruction manual library.
SmartLinx Allen-Bradley Remote VO, English
C) 7ML1998-1AP03
SmartLinx PROFIBUS DP, English
C) 7ML1998-1A003
SmartLinx PROFIBUS DP, German
C) 7ML1998 1AQ33
SmartLinx PROFIBUS DP, French
C) 7ML1998-1A012
SmartLinx DeviceNet, English
C) 7ML1998-iBti02
Note: The appropriate SmartLinx instruction manual
should be ordered as a separate tine on the order.
Power Supply Board (100 to 230 V AC) C) 7ML1830-IMD
Power Supply Board (12 to 30 V DC) C) 7ML1830-IME
Display Board C) 7ML1830-1MF
See SmartLinx product page 5/260 for more infor-
mation. _
1) Available with approval option 1 only
2) This model is level control only; no open channel flow, differential level, or
volume conversion functions
C) Subject to export regulations AL: N, ECCN: F-AR99
Siemens FI 01 • 2009

© Siemens AG 2008
`.
Continuous level measurement Ultrasonic controllers
.
Selection and Ordering data Order No.•
Selection and Ordering data
'Milltronics
_
Mtra onics HydroRanger 200 C) 7 M L 1 0 3 4-
HydroRanger 200 C)
Ultrasonic level controller for up to six pumps that
7 M L 1003 4-
Ultrasonic Intel controller for six pumps that m:�
control, differential control and open
x„
oto
provides control, differential control and open
provides
channel flow monitoring. The HydroRanger 200 is
channel flow monitoring. The HydroRanger 200 is
also available as a level measurement controller
also available as a level measurement controller
only. Select option from model code below.
only. Select option from model Code below.
Mounting
1
c;, -r .,a
Handheld programmer
7ML1830-2AK
Wall mount, standard enclosure
Wall mount, 4 entries, 4 M20 cable glands included 2
Tag stainless steel, 12 x 45 mm (0.47 x 1.77"), one
7ML1930-IAC
Panel mounit) 3
text line, suitable for enclosure
TS -3 Temperature Sensor - see TS -3 on page 51147
Power supply
A
SITRANS RD100 Remote display - see RD100 on
100 to 230 V AC
B
page 5/263
12 to 30 V DC
SITRANS RD200 Remote display - see RD200 on
Communication (SmartLinx)
page 5/265
Without module A
SmartLinx'° Alien -Bradley" Remote 1/0 module 6.
SmartLinx PROFIBUS DP module C
SmartLinx DeviceNetTM module p
See SmartLinx product page 5/260 for more infor-
mation.
Approvals
General Purpose CE, FM, CSAusrc, UL listed,
C -TICK
CSA Class I, Div. 2, Groups A, B, C and D; Class II,
Div 2, Groups F and G; Class III (for wall mount
applications only)
Number of measurement points
Single point model, 6 relays
Dual point model, 6 relays
Single point model, level only, 1 relay2)
Single point model, level only, 3 relays2)
Please add "-Z" to Order No. and specify Order
code(s).
Power Supply Board (100 to 230 V AC) C) 7ML1830-lMD
Power Supply Board (12 to 30 V DC) C) 7ML1830-1ME
Display Board M 7ML1830-IMF
See SmartLinx product page 5/260 for more infor-
mation.
1 1) Available with approval option 1 only
2) This model is level control only; no open channel flow, differential level, or
2 volume conversion functions
C) Subject to export regulations AL: N, ECCN: EAR99
OModbus is a registered trademark of Schneider Electric.
"'Belden is a registered trademark of Belden Wire and Cable Company.
Allen-Bradley is a registered trademark of Rockwell Automation.
2 TMDeviceNet is a trademark of Open DeviceNet Vendor Association (ODVA)
3
;q
Order code
Stainless steel tag [69 mm x 50 mm (2.71 x 1.97")]: Y75
Measuring -point number/identification
(max. 16 characters) specify in plain text
Order No.
English C) 7ML1998-1FC06
French C) 7ML1998-1FC14
German C) 7ML1998.1 FC34
Note: The instruction manual should be ordered as
a separate line on the order.
This device is shipped with the Siemens Milltronics
manual CD containing the complete ATEX Quick
Start and instruction manual library.
SmartLinx Allen-Bradley Remote 1/0, English C) 7ML1998-1AP03
SmartLinx PROFIBUS DP, English C) 7ML1998-1AQ03
SmartLinx PROFIBUS DP, German C) 7ML1998-1AQ33
SmartLinx PROFIBUS DP, French C) 7ML1998-1AQ12
SmartLinx DeviceNet, English C) 7ML1998-18H02
Note: The appropriate SmartLinx instruction rnanuai
should be ordered as a separate line on the order.
L-1 Siemens FI 01 � 2009

© Siemens AG 2008
Continuous level measurement Ultrasonic controllers
®irraensional draw'sngs Schematics
Wall Mount Version
14.9 mm 160.3 mm
(0.58") 6,325"
91 mm
mounting 3 58'
•
( )
6.6 mm
(0.26")
15.2 mm
30 m
i 5.125"'
holes
10 4.3 too,
(0.17") (A)
cover
240 mm
5 )
m
(z6�ws
227 mm
(8.93")
Sutable location for
housing
mounting sc re w
_i
conduit entrances,
(provided by customer)
Siemens Mllltronics
Mounting holes
recommends using a hale
(Accessed under fid)
punch tar dnlfmg the holes.
04.3 mm (0.17")
(x4)
Panel Mount Version
198 mm —=
36
97 mm
0
0.
_ ....:278 mm
0014") ;'
a
s
HydroRanger 200 dimensions
o
r
HydroRanger 200 connections
Siemens FI 01 - 2009

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SPECIFICATIONS- ECH®IMAX° N�l�+-C(�NTACT9�IC ULTRASONIC TRANSDUCERS
Model
Min.Range Max Range Beam=SeHaelre"dFa
Foam
Built In
Temp.Range
Chemical
Thread FlangeA Freq.
Mount. kNz
Weight
KgM
1aF.011 G1396952ACfi faz. ,0t,5i396952M16!}
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Angle Temp:
Temp.
CelsiusImmunity
Rating
Size
Opt. (nam.)
(lbs.)
_•
rc tle io
Ir:l -33 d d2 6!i fi9IX! Fxx: +33 A A2 Sg Iii 9_
Ft. M Ft• -30
Rating
Rating
(Fahrenheit)
—
tet 01M1 662281631li6 Fnx'. �Ol i 352235u 2962
Am°rrs N°. 1155. 11, ci Yan;.. 0310)eJ;.:x:cr. F.. Mexiw
`
THE SURE SHOT XPS SERIES
tct.-5215,62,2b Fux - 515.26.86
hhxxaLv:sni 50. Nt­23 yl 2:c:1i. The Nuth°05a
ln:.-3t(Jjl6 !i•1215, Fax: •61(0)fli bh265.12
105 Sa6;um Jnve. M,Iq l ,lexis U.SFA=."tp&t
XPS-10
0.3
1 10 33 12° Kynar@
Ajo 1 vanture in Siugay°re, a gales °TFiea In Brazil and
dislribNorx (n 56 c°unirirts.
Yes
(4� oto 203°)
Excellent
1;; BSP
43
(1 65)
(2053°)
XPS-15
0.3
1
15
50
6°
Kynaro
95°
Yes
-40° to 95°
Excellent
1" NPT
43
Z;88
(blue)
XPS-30
0.6
2
30
100
6°
Kynar®
95°
Yes
40° to 95°
Exce{lent
1y2
30
4,14
(9.12)
(blue)
(203°)
(-40° to 203°)
BSP/NPT
22
T9
(17.4)
Excellent
Compa-
tible
XPS-40
0:9
3
40
130
6°
Kynaro �I
65° Yes
40° to 95°
(-40° to 203°)
(blue)
(149°)
THE HOT SHOT XCT SERIES
8 26 12° Kynaro
– –
Yes
-40° to 145°
(-40° to 293°)
Excellent
1'r NPT
1" BSP
43
75
(1.65)
(white)
R1.5
1.5
1.2
40 .
6°
Kynar®
–
–
Yes
-40° to 145°
to 293°)
Excellent,
1"NPT
43
1:28
(2.81)
(whike)(40°
HE LONG SHOT XLT / AS SERIES
Representative
—
Milltronics versatile line of sophisticated RangerTM transceivers provide reliable level con-
trol in a single vessel or a multiple tank farm:
35751060 NA
35751062 A4
1
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=
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_
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t}}�'¢�V
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to1.. • 32(01332fi AS SA Faz: •32(J)3i2fi 05 5.5
C,nrxury tint, B - Ig d wnreser Englar:d WR1 gt4
Fax- •1M1 IgOSA59501
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Wertisxasxe 11. pAg5d6 Om<elde•f. Germa-l9
ial �192t1 Sf:25025 251 562 u0: J
1 Ifat Wan Suer. Bunn 602. Ou:;:ry 3aY. k°n3 Kang
tet 01M1 662281631li6 Fnx'. �Ol i 352235u 2962
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`
tct.-5215,62,2b Fux - 515.26.86
hhxxaLv:sni 50. Nt­23 yl 2:c:1i. The Nuth°05a
ln:.-3t(Jjl6 !i•1215, Fax: •61(0)fli bh265.12
105 Sa6;um Jnve. M,Iq l ,lexis U.SFA=."tp&t
_IiI277 3543 1211 ]A`lA
Ajo 1 vanture in Siugay°re, a gales °TFiea In Brazil and
dislribNorx (n 56 c°unirirts.
35751060 NA
35751062 A4

f3,1,�:,-,,�-; WALLACE &TIERNAN
N,,
ENCORE' 700
DIAPHRAG
METERING PUMIJ
SB.440.400.GE

ENCORE"' 700 DIAPHRAGM METERING PUMP
MORE APPLICATIONS, MORE BENEFITS,
MORE FEA'fl1RES._MORE PUMP ^
Ilyrlraulic rliaplrragrri punar ale renowned for their durability, brit start -Lip ancf
maintenance earl be laborlaus, palclrtl;ally allcvl service MgvIl- r ptuying and replacing
lnte.. inedlate 171tids. 14cfdidoriall}, many de.°iiA 7S al -e vVY ft"I 'Il'1VC ttl C178RgIng 3'L1ct1Orl
torarlitiorls. If undiagoosed, blocked 01-s'tarved s'ruxinrl carr lead ro hjdra7llic ovc:'r and
sulurquent diaphragm failure.
lveclianical diaplimgm pumps are lar less sopllisdalled. start -rip And s'eI'vic'e are
typically rllueb smoother• since therr ale no rnmy intermediate fkrids, inter -nal re'llef valves
nr frydratilic relil1 circuits 0 lanaoer v!ith. But, imUl noes; mechar7lcal diapl;' g pumps
haven't s/cared file bydl ttt/ic diapfuagnl plyllp's'.reprrtatiotvfor robur tneis'.
Welcome to the L.iir.nr'e"±i 7DO advantage...
• A whnle new class of metering ptaznii..,
combines the rnl'nIsIIless oi' hydrailllc
diaphragm drives with tha unparalleled
econonly, sin'lplidly and se.rviceahility of
ulechanical diiiphragan hgoid ends.
+ i Iancties capaci}.ics to 2,400 141,
hack pressures to l.Z bar.
Non loss Tnotion (amplit.Llde modulation)
stroke adjust mechanism rCrt(li'.r5 unrivaled
f:tfaciency, It3rtgevity and rt'liability-
• Choice of two l'ic:ld convertible drives_
direct ccnlplecl or pulley coupled, For an
a(Iciitional 4:1.. t1 a.mdown on Stroke frtKlUertcy
Witt) a stanciard induction rnotor',
• Nff:iSinrl f.'.'ragineenO licltfi(i end,, IIICLe1' 11 l
snl(ltior,s, aggressive chemicals, high viscosit'.y'
polyn)ers and Slurries Witt, lar grf:-at.er
cflic:iency i.han conventional liquid c.nds.
• cleat f''VC., Cartridge N<alves lax fast., foolproof
service bvitil vlo pipirlh disturbances and
built -.In visual isaciicat:ion of operation,
0 4'r(;rniurn iliaphr'agnl design ensurers High
mete3 it11; as{:i;tn2tcy; e en at vaa,yi.ng diseha, ge

TYPICAL APPLICATIONS, _ Tyl7zcal Inchisn'iey Typical !Applications, Metering $c Pumping
METERING AND PUMPING
- Water and Wastewater Coali.tlants, oxidising agents, disinftxtants,yc�n['rosion
Treatment. irillibitors, chemicals for rastC, ociour and pH I con-n-cl
FULL MECHANICAL MOVEMENT
AMPLITUDE MODULATION ADVANTAGE
9 Agriculture
i
Acids, caustics, disinfectants acid oxidising agerits
Bactericides, algaecides, acids, cacistics, detergents,
corrosion inhibitors Kid lutlricants
Additives for petrochemical., f?hann<ir..elrtital,
pulp and paper, plastics and tcxtlle man facetn'c:
filtration and fermeritado?n Aids; bHCtPri01de5': ne'icN"
caustics and detergCrits
Fertilisers, herbicides, p(:sticidcs and
fond suppltsrnents
Metering pump manufacturers generally use
one of three diaphragm actuation methods.
Solenoid Pumps.
'I'he must.sirnpte and econarrdcal type or
punlp, these prnvide a ptdsed flow with huge
pressut-L spikes, considerable noise and wear.
Lost -Motion Putnps,
These motor driven pumps are higher in
capacity titan solenoid pumps, but also give
rapid accelentlon to the liquid at rest in the
pump Plead due tQ non-contim-1.011S
diaphragm motion.
Non -boss Motion Pumps,
'Pile diapliragrn is driven by a .rotating
crankshaft, here the eccentricity can txe
smoothly adjusted dUrinf operation. `.rhere
are no 1'CUiIT1 Spt'77:Ig5, and l:he cliaphragrn
moves w th simple harmonic niotion..Ckle
11.uld velocity profile is sinusoidal at all stroke
lengths, adjusting si:rolce len tll simply alters
the amplitude of the sine wave, This design
provides reliability and longevity, and pump
valves operate with far greater efficiency.
`Phis graph shows the velority profiles for each pump type. For ally given output, the areas
circumscribed by each curve are identical,. Note the dili'erence in corn-loss-Inotion designs,
u Encor.0700 non -loss ..:
motion mechanical
b diaphragm Pump
sofenntd.: Post motion
um
t .. S CIUr, •� SIICLILII
Swimming Pools
_
t �
Food Pr(?ces'sirtg
Chemical Processing
a
Brewing & Distillation
9 Agriculture
i
Acids, caustics, disinfectants acid oxidising agerits
Bactericides, algaecides, acids, cacistics, detergents,
corrosion inhibitors Kid lutlricants
Additives for petrochemical., f?hann<ir..elrtital,
pulp and paper, plastics and tcxtlle man facetn'c:
filtration and fermeritado?n Aids; bHCtPri01de5': ne'icN"
caustics and detergCrits
Fertilisers, herbicides, p(:sticidcs and
fond suppltsrnents
Metering pump manufacturers generally use
one of three diaphragm actuation methods.
Solenoid Pumps.
'I'he must.sirnpte and econarrdcal type or
punlp, these prnvide a ptdsed flow with huge
pressut-L spikes, considerable noise and wear.
Lost -Motion Putnps,
These motor driven pumps are higher in
capacity titan solenoid pumps, but also give
rapid accelentlon to the liquid at rest in the
pump Plead due tQ non-contim-1.011S
diaphragm motion.
Non -boss Motion Pumps,
'Pile diapliragrn is driven by a .rotating
crankshaft, here the eccentricity can txe
smoothly adjusted dUrinf operation. `.rhere
are no 1'CUiIT1 Spt'77:Ig5, and l:he cliaphragrn
moves w th simple harmonic niotion..Ckle
11.uld velocity profile is sinusoidal at all stroke
lengths, adjusting si:rolce len tll simply alters
the amplitude of the sine wave, This design
provides reliability and longevity, and pump
valves operate with far greater efficiency.
`Phis graph shows the velority profiles for each pump type. For ally given output, the areas
circumscribed by each curve are identical,. Note the dili'erence in corn-loss-Inotion designs,
u Encor.0700 non -loss ..:
motion mechanical
b diaphragm Pump
sofenntd.: Post motion
um
t .. S CIUr, •� SIICLILII

'alld.f'EI! tlI,CE2p1tI2
h�l�dle t.With
L€sak atthe
vantages:
ENCORE@ 700 DIAPHRAGM METERING PUMP
Available with standard induction and variable speed motors
(opt.lonat) for wider operating ranges and automatic process control.
Short suction and discharge
porting minimises friction tosses
and cavitation, improving
hydraulic characteristics and
lxnviding far more efficient fluid
metering than conventional
liquid end designs.
Our premium composite
diaphragm is manufactured to
stringent specifications to ensure
long life even under the most
demanding applications.
The. design incorporates trflon-
racing, for the highest degree of
chernical resistance and nylon
reinforcements. all honcleci to a
pre -formed elastomeric support.
We've aciclecl convolutions for
unconstrained ronin£; action,
a steel backing plate to assure
volumetric accuracy even at varying
discharge pressrlres and an o -ring
groove in the head's diaphragm
cavity for c:omplele sealing.
High precision guided ball -and -seat clear
PVC cartridge valves (except 165turn head)
provide built-in sight' fleasindication 'and fast,
foolproof service. The design 'includes wide
flow paths and four -point guides to rontrol
ball rise and assure proper seating. 'rhe valve
fborrsing is compression sealed to the pump
A secondary diaphragm seal
completely separal.es the pumphead from
the drive unit.. This double, diaphragm /
isolating design eliminates the risk of
cross cont'arninating gearb0x Illliricant and
Process fluid.

/Available in two field convertible
drive arrangements: direct chive or
pulley drive for an adciitionat 4:1.
rangeability nn stroke frequency with
a standard induction motor. When
the putley drive arrangement is
cornbineti with a DC variable
speed motor, total operating
turndown can be as high as 8f} 11
With double simplex
capability, two drive units,
each with independent
capacity control, can be.
multiplexed for blending
applications or future
process expansion.
This robust mechanical asxcrribly fl'atllf'e.' liberal use of heavy duty
parts including an epoxyTRinted cast iron gearbox for superior
corrosion resistance, 318 SS fasteners, load absorbing tapered roller
bearings, robust gears and steel and nacktlar iron drive components,
C)latain prec..ise and highly repeatable feed rate settings with a
10 turn rriicrorneter-tylre stroke length adjuster.
��— A percent scale and vernier indicate Stroke lengill in
r f),l )t5u 1I1C1'eiYletltS. Feed rage is inl`initely adjustable from t) to iQ0°/n.
t`tutornatic capacii'_v control via stroke length is also available.
An optional diaphragm leak detection system senses the early
stages of diaphragm i'alluce. The system consists of a sol'sd state;
electro -optic. sensor that mnt.tnts to the liquid end and a 1.1' 35
control box. 1'lris box, which can be. mourited at t}ie pump, ar
up to 30 metres, can monitor tIva 11quid ends, LEI}'s and a relay
provide both local and ren.tote indicali.orr, of t tils.lre.
lilertm-nptrr sensor

EN CORE@ 700 DIAPHRAGM METERING PUMP
MANUAL ANF) AUTOMATIC
STROKE LENGTH CONTROL
'lyre' ,ncnre@0 700 metering purnp carr be
controlled by varying the stroke length or
stroke frequency, The following control
schemes are available:
Manual or 12ennte Ivlanual Control
Start -Stop Control where the rnWnr is
wired into the circuit of a transfer pump,
switch, iirner or cnnirdler
Flow Proportional Control from a single
process variable
Residual, Compound Loop or Set -Point
Control using one or two process
variables
Manual Stroke Length Control
A 10 u.trn micrometer gives continuous
feed rate acljustruent over a 10:1 range. A
percent scale and vernier indicate stroke
length setting to 1 part in 400. F,ach
revolution of the knob changes feed rate by
10%. Stroke length is infinitely adjustable
from 0 to 10Wyo.
Automatic Stroke Length Control
For autornatic capacity control via stroke
length, our new 11) 65 actuator is used {n
conjunction with either of two new process
variable, controfters. I'lre cornpact, field-
retrofittable actuator easily installs on the
pump and features local inartual override
and it window for clear indication of stroke
length. Tcvo new microprocessor -based
controllers are available:
SCU, Signal Conditioning Unit
,file econoulical SCU gives automatic
process control in
response to one
process variable,
typically flow
rate.. Housed in a
IP 65 enclosure,
tile $CU features
an S -character
alphanuntertc LCD display with 6-1button
keypad and menu -driven operator, prompts
for simple operation, sotup and calibration,
Input flow scaling and output dosage
adjustinent allow independent scaling frorl'l
10 to 400%. See publication TI 40.100GE
for t'rlore detalls.
Variable Speed Control
For precise and acci.rl'9te,, feed rate control
via stroking speed, an SCIt Drive Unit
varies the speed of a DC; punlj:? motor.
Stroke frequency. can he regulataci rnanually
by potentiometer setting, or aui.omirtically
via a 4-20 mA process variable input signal
(optional). Closed-loop speed regulation
provides reed rate c:ont.rni accurate to 1% of
full scale. With continuous adjustment over
a 20:1 range, total operating turndown
with water like solutions is 200:1. on direct
drive units, 800:1 on pulley drives.
Dosing or starling of a process variable can
be accomplished by mealas of all SCU,
Signal Conditioning Urdt used in
conjunction with an SCR drive. rnr more
cornplex control, a PCU' Control
Unit can be, used to provide setpoint
control in response to two process variablen ,
such as plant flow and chlorine residual.
PCU, process Control Unit
The PCU is a full feature setpoirlt
controller. It provides automatic process
control in response to two process lnputs,
typically Ilow rate and chlorine resichial.
The. PCU can operate in any or your
different control modes including residual
feedback, compound loop, dual signal 1'eecl
forward (for dechlorination) and flow
proportional. 1n
addition, the
4 PCU can be
configured for
` ? center zero
iN operation in
<4l` corrtpou.nd loop
.._..:................._�,_.M.�.� rttoc3e when a
DEOXl2000'"' Dechlorination Analynr is
used. Fit..}used in a 11' 65 ericlouue, the.
VCU f'eatur'es a tai ;e adphallUnieric display,
an LED bargrxph to indicate i'low input or
actuator position In 5% incrernents, a 6-
button krypad and menu driven ope.raior
prornpts in, simple operation, setup and
calihration.
Ec.r mare inl'nrmation request publdcaliail
T[ 40.20UCE.

TECHNICAL INFORMATION
CAPACITIES AND DISCHARGE PRESSURES
I
3U i -]x 1450 RPM 1'n;.•„+re (t.')
L)Irtpivagnro
SrUke
l;npaci,y
_...... ,
Pul€r)
Stx�.e"'"
1450 RPM
Lmuenn„(�:,rl:,�ile sixon}
Lis]'
fliihlnpl
5i:er,
Pivyuency _-__..
T^1111,
(.55) (aw)
Slink,•; n,h,.
M111
.31 t3Y) .77 .55
-
3S
60
2.1
7.0
1
(4, IDx
120
4.2
15.8
1
12
44
5.0
19..0
1
12
12 .. ..
50
60
10.0
44.2
I
12
12.0
20.0
80.0
1
12
144
24
106.41
1
12 -
_..-...._.
30
f)A
:35.5
75
60
INR
71
126
37S
1.4]'3
- - Ifl
144
45.6
170.3
1
- 10
30
1&0
60.7
I
0
If}U
60
32.1
MA
1
- 4 -
R^
124)
fi4.2
242`3
1
- - 9
144
77.0
201.4
30
37,5
141 n
1
5
1L5
GQ
7b.43
283.11
1
- 5 -
Rl
120
1311.1]
Se"1.8
I
-
144
180.0
683.3
I
-
30
6G-0
260d1
I
3 - -
105
61)
132.(1
520.£7
1
- 3
R34x
1'LO
I(A.0
If141.1)
1
- 3
1-1.t
317.0
£'1,513.0
1
- - 3
"IZeliercn simplex capacity, dn,+hle-sianp)e>: arrvl8eitte,lrg otuxt be reai£(gured ,dt3x same stmke•beSuenn' - both liquid cods.
`"Fen puttey ,ici,l:.nr;mge,uc,lls, caµaci5ics Ilolcd ar tut µidley etc}r 1. Capacit ies pia steµs2, 3,
r�spcw(ivcl)'.
Accuracy
Repeatable metering accuracy is t 2% of
full scale, at constant hydraulic conditions,
over.a 10:1 operating range.
Stroke Length
L.ieju& Fnd .4izc .35 il-f 5017111 ' +.811?m
Liquid Dick Size 7.'S, 100, 12.5 and
Xl 5n1�r7.'
9-6tnln {0.3751.
Feed Rate Adjustment
Feed rate is infinitely adjl.m.able from
0 through 100%. A }percent scale and
Vet'ilitr ind.iCa3.e StrCike. length s+:llfirlg ill
(7.`1.5`%1 increments. Trach revolution of the
knob changes stroke lt:tlgtll by 10`%r.
operating Range
Dir'ccr Drfvc Arrlrtgcinm
Stroke length is adjustable over a
10:1 range; stroke frequency is adjustabte
over a 20:1 range (using at' optional
variahle speed drive). 'Intal combined
maximum operating ttlrodOV,111 can be as
iligb as 200:1. Above 100:1 continuous
turndown, total avaiiable operating range
shc)u.ld he evaluated against specific
c}lenticals being metered.
Aiiiey Drive !Irr<a.n�cn7er7t'
RrOkC length is acijtistabie river a
10:1, range; stroke frequency is adjustable
over an 80.1 range (ushlig all Optiol'lal
variable speed drive), Total cntnbined
rnaximurn operating turndown can be as
high as 800:1. Above 100:1 contir"JoUS
turnclow'rl, total available operating range
sl'lould be evaluated against specirk
chenlic:als being metered.
Speed of Response
Automatic stroke length control response
time is LOG seconds from 0 to 100%.
Variable speed COMIol response tittle is
under 3 seconds [roll, 0 to 100°/,.
Suction Lift
1 -he, pllnip Wlil self prime with 3 metres of
water suction lift (wetted valves, 'zero back
pressure, full stroke and speed, waterlikc
solutions), Once primed, the pump will
operate ,with 3 metres of water stiction lift..
Flooded suction is recommended.
Weight and Shipping Weight
Stn lesi.rnplr..r50 kg; 60 kg; dntrlrlr..rimp/cx
73 kg; 88 kg. For arrangements will,
automatic stroke lens h control add
5.5 kg; 7.3kg.
Temperature Limits
Will) 11VC-liquid 6'nd ambient S:CIllpCI'atures
from 2-52'('., process fluid temperatulis
up to 52°C.
bliilr 16f'1'ltrrligtrid e17(1'process fi(lid
temperatures up to 6?'C.
(lechnicaI lnforcnation conanued un next
i3a€ie•)
lcflen• .Hy ,aeon and \htun arc regisrere E irxdnn:arks of
735. DuYnnt C;n.

Electrical Requirments
Standard iliciuction motor arrangnlerlt Is
1450 rpm, 1.15/230 Volts, 50f -1z, single
phase, TEFL. Motors with other electrical
characteristics are available as ara option.
Diaphragm leak detector requiras 115/2:50
Volts, Relay rating 5 Amps @0 2.50 Volts, 30
VDC. IP 65 enc:fosure. Variable speed drive
control unit re(luires 11.5/230 Volts, 50/60
Hz, single phase, 200 mA (11.5V, 1.00 mA
(23OV). Automatic stroke length actuator -
3 alarm contacts (high, low, actilatt)r
disengaged} N.O., rated 5 Arnps @ 250
Volts.
Materials of Construction
ear Ixrx and 1lrluid and adspter. epoxy
painted, cast iron
,Stroke positioner enclosure: epoxy painted,
cast. aluminum
Furrtp IreacL• PVC; or PVDF
51rr.lion ztltd discharge valve houdnm clear
PVC, grey PVC or PVDF
Vaivn. 6alLs; 31.8 stainless, TFE, ceramic,
glass and polyurethane (for slurry servic(,)
1/tive seals' 1-lypaion and Viton
lJiaplut,n '`I'1 E fsu:ecJ, fabric. reinforced,
elastomer backed, wal) to steel or cast iron
backing plate
h(nurttirrg box (optlonalJ: ABS
'I'hie pump is UV rtsistanl.
F'1
Dtie to continual product devetoprr,cnt and
in:prnvemenL, c:Awaill specii'icttinrrs may
charq+ withcxil prior ami mlminent.
F -i
ENCORE 700 DIAPHRAGM METERING PUMP
Polymer and Slurry Handling
Capabilities
Polymer solutions at viscosities up to 5,000
cps at. 144 %pro. Viscosities measut'ed with a
Brookfield Viscometer with Na, 2 spindle
it 3 rpm,
Ilydrate.d time sltu-rits uta to 0.38 k.g per
litre of water; activated carbon slt.lrries Up
to 0.11. kg per litre of water;
diatornaccous earth slurries Lap to 0.17 kg
per litre of water,
Chemical Metering Systems
I.,ow Cost packaged systerris can be custorn
configured from standard stock
components including tanks, waxers,
instrumentation and a wide range of
controls. All syst.ens are shipped assembled,
prewired and ready to install. Oilr
comprehensive range of co-oidinated
accessories provide the ability to PrOdOce
the best possible installation.
Accessories
Choose from Sack. Pressure Valves, Pressure
Relief Valves, Antisyphon Valves, Witl-
function Valves, Main Connectioi is,
Strainers, Pulsation Dantpeners,
Calibration Chambers, Solution Tanks,
Mixers, Liquid bevel SwiteW, Siun_y
Flushing Systems and nurnercnrs -M--thing
Accessories Just to name. a le..w.
PM Kits'"
Preventive Maintenance kits contain
original Wallace & Tiernan replacements
for those parts most susceptible to Wear.
They facilitate scheduled maintenartre and
help maintain equipment in good working
order, eliminating equipment breakdowns
and costly downtime.
For further technical information sere
publications:
'Fi.440.400.GE &.
Ti,440.400.2.GF,
;a°rl LLANI _E & i fir"":RNAN
C;hemr.eed Limited
Pric:iry Work&
'D-Mbridge, lent `1'N II OQL
Telepllorte: x-44 (0) 1732 771777
Fax: A4 (0) 1.732 771800
Erra1L' drafnrrnf ti%rl,'acr.-trrr>3<.17.rom
ltttpAwtviV..rsalla.e thrnalt .cen
j
[371[)2

02/0°f2088 19;21 ' 7658279869
TEC INC PAGE. 82
T , Inc.
SPECIFICATIONS
RE—TIOU4 F.UDDR-1
The TEC weight loaded pressure relief valve offers non -
vibrating, reliable capacity relief for positive displacement
blowers.
The pressure relief valve is installed in the discharge air
stream to prevent damage.to positive displacement blowers
when Operating pressures exceed the maximum pressure
rating. of the blower.
As the system pressure approaches the vatve set point, tate
weight loaded cylinder is forced up from the valve seat and
exposes the vent ports for fast and efficient blow -down.
When acceptable system pressures are re -stored, the valve
automatically returns to the original set position.
The valve cylinder and seat are constructed of cast imn and
accurately machined to vary tight toterances for smooth
operation.
Removable weights have been carefully designed to permit
accurate pressure settings in Y2 PSI increments.
Adjustments In the relief setting can be made by adding or
removing weights.
SIZE A
B
C .
.0
E
Wt,
1" 1.0" FPT
4.19
4.75
2.00
6.00
5
1.5" FPT
5.81
6.d•4
2.63
8.13
to
2.5" FPT
7.63
8.88
3,63
9.88 25
PF
RFCIRMANCtEr
1s
FLOW RATING - CFM
2 3 4
40 60 80
3n 120 16(
(68 F & 14.7
.1RE - PSIG
144
R
�"PSPE TRP''
1125
10
TEC, Inc.
3594 S. CR. 350 E.
Connersville, IN 47331 SWL1193
PH: [phone] FX: [phone]

El
GENERAL DIME
FLOW
MALE: THREADED ENDS
A"
FOR STYLE 5002
ALL DIME
101-0 — ---, STANDARD MODELS& MATERIALS
5002 -AL Aluminum
'WIMP,
50
6002 -BR Brass
y
1
3-1/2
1.316
1-5/8
4
6
4 1/2
4-7t
1-1/4
3-1/2
1 1.660
2
5
7
8
5-911
6-5/8
6-1/8
7-1/8
1-1/2
4
1 1.900
2-3/8
2-1/4
'):ZIA
6
8
10
8-6/8
9-1/2
Monet and Inconel springs available upon request.
PRESSURE RATINGS NOT SHOWN.
/-1/0
3-1/4
muwmmwn�
12
10-3/4
11-1/2
5-1/2
3-1 /' i
�:::
3 !, � 3
12
14
12-3/4
13-3/4
ALL DIME
101-0 — ---, STANDARD MODELS& MATERIALS
5002 -AL Aluminum
Aluminum
50
6002 -BR Brass
Brass
150
6002-304 304 Stainless Steel
1 304 Stainless Steel
i
150
5002.316 316 Stainless Steel
i 316 Stainless Steel
150i
5002 -Class A Steel
Aluminum
150
5002 Class D Steel
Cadmium Plated Steel
150
—Standard Elastomer: Buna-N
OPTIONAL MATERIAL SELECTION '
7
A TERIAL •TEMPERATURE RANGE
• Aluminum
• Bronze
8,: N 60 to 2251 F
• 304 Stainiess.Steel
* Neoprene 10 to 225* F
• 316 Stainless Steel
- Butyl —65 to 3251 F
• Cadmium Plated Steel
Hypalon —20 to 3001 F
• Electroless Nickel Plated Steel or Aluminum
EPOM —40 to KO I F
• Monet*•
Viton —20 to 400° F
• Titanium'
• Teflon —20 to 450, F
• HastallaY
• Silicone —100 to 500° F
'Non stock item — Available upon request.
FDA Approved —40 to 2251 F
White Neoprene I
rxw-7---
*This temperature range is for general guidance. The
• 304 Stainless Steel
figures may vary with application.
316 Stainless Steil
CONSULT FACTORY FOR MATERIALS, SIZES AND
Monet and Inconel springs available upon request.
PRESSURE RATINGS NOT SHOWN.
END CONFIGURATIONS ALSO AVAILABLE.
• COMBINATION
muwmmwn�

Cut -Sheets & Pump Curves for WWTP Pumps:forward flow/recycle pumps, sand filter
flow pumps, equalization tank grinder pumps, sludge tank decanting pump.

,Company: Aqueonics Recirculation Pump Selection
-Date: '10/5/2008
Pump;
Sizs: 30MMP
Type: Self -Primera
Synch speed: Adjustable
Cuve: 30MM2000
Sp.cific Speeds:
Dimensions:
Pumr Limits:
r-,
Temperature: 140 °F
Prl>ssure: 125 psi g
SKhere size: 2.5 in
--- Data Point ---
Flow: 147 US gpm
Head: 30 ft
Eff: 44%
Power: 2.5 hp
—� NP 3Hr: 6.54 ft
{ -- Design Curve ---
Shutoff head: 39.9 ft
r= Shutoff dP: 17.2 psi
Mir, flow: --- US gpm
BEP: 47% @ 180 US gpm
NGL power:
1 2.66 hp @ 180 US gpm
Speed: 1200 rpm
Dia: 8.4062 in
Impeller:
Ns: ---
Nss: ---
Suction: --- in
Discharge: 3 in
Power: --- hp
Eye area: --- in'
Search Criteria:
Flow: ---US gpm
Fluid:
Water
Density: 62.25 Ib/ft'
Viscosity: 1.105 cP
NPSHa: ---ft
Head: --- ft
Temperature: 60 'F
Vapor pressure: 0.2563 psi a
Atm pressure: 14.7 psi a
Motor.
Standard: NEMA --- hp
Enclosure: TEFC Speed: ---
Frame: ---
Sizing criteria: Max Power on Design Curve
Performance Evaluation:
90
8.4062 in
_ _
80
Efficiency
40 _ _
NPSHr
ft
US gpm rpm
ft
%
hp
70
J 173 1200
30
47
60
u
�d
30.2
50
c
v
6.39
115 1200
31.9
W
d
2 20.
4.55
40
33.4
35
2.07
- 30
57.6 1200
35.4
27
20
1.69
10
10
0` 20
40 60 80 100 120 140 160 180 _
0
10
2 5'
a
Z
0 20
40 60 80 100 120 140 160 180
3
2
.c
L 1''
3
0- 0 20
40 60 80 100 120 140 160 180
US gpm
Performance Evaluation:
Flow Speed
Head
Efficiency
Power
NPSHr
ft
US gpm rpm
ft
%
hp
J 173 1200
27.9
46
2.63
8.31
vI 144 1200
30.2
44
2.49
6.39
115 1200
31.9
41
2.26
4.55
86.4 1200
33.4
35
2.07
3.07
57.6 1200
35.4
27
1.94
1.69
H,!Optimize Hydromatic 8
Selected from catalog: Self -Primer Pumps 60Hz Vers: Feb 2006

Operation is recommended in the bounded area with operational point within the curve limit.
Performance curves are based on actual tests with clear water at 701, F. and 1280 feet site elevation.
Conditions of Service:
GPM: TDH:
F HYDROMATICO
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Operation is recommended in the bounded area with operational point within the curve limit.
Performance curves are based on actual tests with clear water at 701, F. and 1280 feet site elevation.
Conditions of Service:
GPM: TDH:
F HYDROMATICO

W ■ _t __®®__l��_� ...�vJ �s�sa v.®w NM ®�YY�®s�
Self Sewage - Trash
CH
r_=+ NOTE! To the installer: Please make sure you provide
this manual to the owner of the pumping equipment or to
the responsible party who maintains the system.
r
Pentair Pump Group

The MP / MPH self -priming
centrifugal pump has a semi -open
impeller and suction flap valve.
Pump is designed to handle raw
un -screened sewage, mild indus-
trial waste and slurries containing
entrained solids. The material of
construction is a cast iron volute
case and bearing frame, ductile
iron impeller and wear plate.
Thank you for purchasing your
Hydromatic self -priming pump.
If there are any additional
questions not covered in this manual
please contact the HYDROMATIC
representative or HYDROMATIC
Pump Co.
Before Operation:
Read the following instructions
carefully. Reasonable care and
safe methods should be practiced
for installation and operation of
pump. Check all local codes and
requirements before installation.
Attention:
This manual contains important
information for the safe use of
this product. Read this manual
completely before using this
product and refer to it often for
continued safe product use. DO
NOT THROW AWAY OR LOSE
THIS MANUAL. Deep it in a
safe place so that you may refer to
it often.
Unpacking Pump:
Remove pump from pallet. When
unpacking unit, check for
concealed damage. Claims for
damage must be made at: the
receiving end through the delivery
carrier. Damage claims cannot be
processed from the factory. Check
for and tighten all loose attaching
hardware. Check oil levels and
lubricate as necessary.
Warning: Before handling these
pumps and controls, always
disconnect the power first. Do
not smoke or use sparkable
electrical devices or flames in a
septic (gaseous) or possible
septic area.
Pump Not Operating Or
In Storage:
If pump is not put into service
immediately, it must be properly
stored to prevent damage. Store
unit in a dry warm location. Never
store unit in the open even if it is
protected with plastic or other
covering. The bearing housing
and motor will draw moisture,
which may result in pump failure
after being put in operation.
While in storage pumps with
carbon ceramic seals must
have impellers manually rotated
(6 to 12 revolutions) after
setting non -operational for 3
months or longer and prior to
electrical startup.
Pumps with tungsten carbide seals
must have impellers manually
rotated (6 to 12 revolutions) after
setting non -operational for 3
weeks or longer and prior to
electrical startup.
Motors:
Pump unit may be shipped less
the motor for customer to supply
and mount.
Motor Types:
Pumps can be driven by Standard
drip -proof, totally enclosed fan
cooled, totally enclosed explosion
proof or drip proof with encapsulated
windings for moisture protection.
If motor is to operate in the open
or in a dusty location a totally
enclosed fan cooled motor must
be used. If pump is to operate in a
damp location a motor with
encapsulated winding should be
used. Motors are to be sized so
that no overload will exist in the
operating range of the pump.
Note: When pump units are
mounted at the factory, the
driver and pump are aligned
before shipment. During transit
and handling of pump and
components misalignment may
occur. Before operation the drive
alignment should be checked.
Shaft Couplings:
We recommend using Wood's
flexible coupling to prevent
misalignment and noise that can
be caused by other couplings. The
extra cost of the coupling is easily
saved in installation and field
service that can result from
coupling problems.
V -belt drive:
Where V -belts are used, keep belts
tight by adjusting motor base
screws. Belts should run cool. If
belts heat up it will indicate
slipping. The V -belts should be
fiddle string tight
CAUTION: Belt guards and
coupling guards must be
properly installed before
operating pump unit.
Electrical Starting Equipment:
If electrical starting equipment is
not furnished with pump, certain
precautions must be observed in
selecting motor starter.

Type Of Starter:
For three phase power a magnetic
starter with 3 leg overload
protection is recommended to
prevent motor burn out that can
occur from single phasing or
transformer faults on three phase
systems. For single-phase motors
a standard starter with 2 -leg overload
protection is recommended.
Electrical:
1. For motor overload protection
the magnetic starter trip amp
rating should not be more than
1.25 times the full load amps
of the motor. HYDROMATIC
recommends a rating of 1.15
times the full load amps of
the motor.
2. Always use fused disconnect
switch or circuit breaker
ahead of magnetic starter for
short circuit protection. When
duplex pumps are used and are
operated from single disconnect
switch be sure disconnect
switch is large enough to
withstand the starting current
of both pumps coming on at
once. This can occur after a
power failure. This is impor-
tant as a blown fuse or tripped
circuit breaker can make both
pumps and an alarm system
inoperative resulting in flooding
or other damage.
Ground:
Connect a ground wire to motors,
control box and other related con-
trols. Ground wired to be sized to
the National Electric Code article
250-95. Ground wire must be con-
nected to a driven ground stake or
to a ground wire from the supply
service. If a ground stake is used it
must be driven at least 8 feet into
the ground.
Codes:
All local wiring cosies must be
observed and any exceptions to
data given must be followed in
accordance with the local code.
Consult the local inspector before
installation to avoid costly delays
that can occur due to rejection
after job is finished.
Pump Installation Foundation:
Pump frame or base should be
installed on a concrete floor with
proper shims and grout. Use
hardwood tapered shims to drive
under base to level. Base should
be about 1 to 1 1/2" off the floor.
Build form around the base and
fill base inside cavity with grout.
Foundation bolts can be set in the
grout or set in the concrete floor
with expansion bolts.
Grout should be made with 1 part
cement and 2 parts sand. Mixture
should be fluid enough to run
under base. Wood shim blocks can
be removed after grout has set and
holes filled with quick set cement.
Piping:
All piping to suction and discharge
openings of pump must be
supported to remove stress from
the pump case and bearing frame.
Suction Pipe:
1. Suction pipe should be same
size as pump opening. DO
NOT use larger suction pipe as
priming time will be increased
and velocity may not be
high enough to properly
carry solids.
2. Pump should be installed as
close to the liquid being
pumped as possible with a
minimum of elbows or fittings.
3. To avoid air pockets suction
-pipe must be as short and
direct as possible. Suction pipe
must always slope upwards to
the pump from the source of
the liquid being pumped.
4. The suction pipe should be
installed at a distance equal to
1.1/2 times the diameter of the
suction pipe from the wall of
the wet well, minimum.
5. The suction pipe should be
installed at a distance equal to
one half the diameter of the
suction pipe or 3" from the
floor of the wet well, minimum.
6. If more than one suction pipe
is to be installed in the same
wet well, a distance equal to
at least 3 times the diameter
of the suction pipe should
separate them, minimum.
7. Submergence of the suction
pipe is critical to efficient pump
operations. See the following
chart for recommended minimum
submergence vs. velocity.
Submergence may be reduced
by installing a standard pipe
increaser fitting at the end
of the suction pipe. The larger
opening size will reduce the
inlet velocity and required
submergence. See Figure #1.
Vertical Suction Lift:
Vertical lift should not be more
than 15 feet. This is for starting
level only. After pump primes,
level can be pumped down to 18
to 20 feet if desired, but sump
level must rise up to the original.
level for restart. All suction line
joints must be air tight as a
leak in the suction pipe can
cause pump to loose prime or
not prime at all. Always
check N.P.S.H. calculations for
available atmosphere pressure
before applying pump.
M

Hydroinatic Pump F/7
(� I/- / 5 I -2 a) D0N (1 / / SM P 7
p nta"
ar ur
WAter
WELCOME
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Superior Features:
-Garbon/Ceramic type 21 mechanical seal
*00 -filled motor with automatic reset thermal
overload for maximum protection (one phase
models)
-Upper and lower single -row ball-bearing
oons-truotion
-Piggyback plug available for easy maintenance
and switch replacement
Dcywnioad PDF Sales Sheet
Download PDF Nllanuaj
Download Specificlation Subrnittal Dat,2
Specifications:
Typical
Application:
Capacities:
Heads:
Electrical:
Motor-,
Intermittont Liquid
High -Capacity sump/efflUerit,
seviage
up to 120 GPM (7.5 LPSI
up to 28 ft, (8,5 M)
115V, lo, 9,5 FLA, 60Hz;
230V, lo, 44-1 FLA, 6OHz
4110 HP split phase with
thermal overload protection,
1750 RPM
140-F (6WC)
Pag
ge I €f2
10X2008

flydroynatle NMIP
Copyright C Pentair
Pump Group Ali
Rights Re -served.
Pfivai�y Policy
rerms and, ( 'omdi Livtft
Temp-,
Minimum
Recommended
Sump Diameter:
Automatic
Operation,
Ma"t
b; ims Of
Construction:
impeller:
Discharge Size:
Solids Handling:
Power Cord,
Performances
,30,-----T-
simplex -- 18" (467 Mtn)
Duplex = 30" (762 mm)
Diaphragm pressure switch
(manual available)
Class 30 cast iron
Thermoplastic
2" NPT (50.8 m1n)
!-114" (31 .8 mm)
10,, SJTW (0` optional)
S -V350 & 5P.550A4
I
r..
34
0 Vs
Flydrom-afic reserve,', the. iigbj, to make revisions to its
products and their specifications, (Ids ca-Lalog, and related
Information without notice,
DI I
I age) ot ''

Company: aqueonics
flame:
viate: 10/5/2008
R @0 HYDROMATIC
-- Data Point ---
Flow: 70 US gpm
"I Head: 23 ft
Eff: %
Power: 3 hp
NPSHr: --- ft
-- Design Curve ---
JJ1Shutoff head: 34.5 ft
' Shutoff dP: 14.9 psi
Min flow: 5 US gpm
BEP: --- %
NOL power:
3hp@5USgpm
" - Max Curve --
r Max power:
3 hp @ 5 US gpm
50
8 in
40 -
.0 25 in
R
d
= 30
Performance Evaluation:
Search Criteria:
F-IFlow Speed
hump:
Efficiency Power NPSHr
Flow: 70 US gpm
Head: 23 ft
Size: HPGF/H/X-300
\ 84 1750
19.9
--- 3 ---
-, Type: GRINDER-SUBM
Speed: 1750 rpm
Fluid:
56 1750
Synch speed: 1800 rpm
Dia: 7.0625 in
Water
Temperature: 60 °F
Curve:
impeller:
Density: 62.25 lb/ft'
Vapor pressure: 0.2563 psi a
Ns: ---
Viscosity: 1.105 cP
Atm pressure: 14.7 psi a
Specific Speeds:
-
Nss: ---
NPSHa: 46.4 ft
Dimensions:
Suction: --- in
Discharge: 2 in
Motor.
YT
Pu�� iog1Q
to select a motor for this pump.
- ,r�i�
Pump Limits:
Catalog does not contain
data to verify that NPSHa is sufficient.
Temperature: 140 °F
Power: --- hp
Pressure: --- psi g
Eye area: --- int
Sphere size: --- in
-- Data Point ---
Flow: 70 US gpm
"I Head: 23 ft
Eff: %
Power: 3 hp
NPSHr: --- ft
-- Design Curve ---
JJ1Shutoff head: 34.5 ft
' Shutoff dP: 14.9 psi
Min flow: 5 US gpm
BEP: --- %
NOL power:
3hp@5USgpm
" - Max Curve --
r Max power:
3 hp @ 5 US gpm
50
8 in
40 -
.0 25 in
R
d
= 30
Performance Evaluation:
F-IFlow Speed
Head
Efficiency Power NPSHr
US gpm rpm
ft
% hp ft
\ 84 1750
19.9
--- 3 ---
rr 70 1750
23
--- 3 ---
56 1750
25.9
--- 3 ---
42 1750
28.6
--- 3 ---
28 1750
30.9
--- 3
2, r --1
H2Optimize Hydromatic 8 Selected from catalog: Grinder Pumps 60Hz Vers: Feb 2006

Lo eb TANK
DECANTING PUMP -_
Typical Application
CnpadlyU,i9f.Y, i9 �6 Nl � 190 139
Lie�Sn�ni9
Performance Curve
wage, High capacity sump
Capacities to
1120 GPM (7.5 s) .._
:Heads to
24 ft (7.3 m)
Electrical
1115V, lo, 12 OFLA, 6011z, 230V, lo, 6 OFLA, 60Hz I
11/2 HP split phase w/thermal overload protection,
Motor
4 750 RPM
'Minimum Recommended
118" (457mm)
;Simplex
Sump Diameter Duplex
'30" (762mm)
Automatic Operation
Wide angle float switch (manual available)
;Materials of Construction
'Class 30 cast iron
Impeller
Klass 30 cast iron non -clog
Discharge Size
2" (50 8mm); 3" (76.2mm) optional
:Solids handling
" 1�
2 (50 8mm)
Power cord
110' , SJTW, (20' optional)
Superior Features
Carbon/Ceramic type 21 mechanical seal
Oil filled motor w/automatic reset thermal overload
,for maximum protection
Upper and lower single row ball bearing
;construction
Piggy -back plug available for easy maintenance
land replacement

Cut -Sheets for WWTP Blowers

_ irL�r
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1U01MIUM
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•1.6
'
X675 f91
t
• ,
46
2,800
76
,1
71
67
2.1
63
2.5
59
75
3.0
3.4
56
72
3.5
4.0
2LP
2".6
0.035
3,250
91
102
1.3
1.4
86
97
1.8
2.0
82
93
2.h
2.6
79
78
2.9
3.2
86
3.7
83
4.3
2LVP
6.1
124 6.9
3,560
5 275
1760
162
149
2.0
1.9
157
142
2.8
2.8
3.5
153
135
188
3.7
37
4.7
149
130
182
4.6
4.5
5.6
146
124
177
5.3
5.2
6.7
143
120
172
6.1
6.1
7.8
74 5.2
3LP
3LVP
2;4".S
0.104
2,265
2,770
202
254
2.4
2.9
194
247
4.3
240
5.5
235
6.8
230
356
8.2
10.6
225
311
9.6
12.4
11.15
4HVP
3,600
341
3.7
3.0
333
243
5.3
4.5
327
234
7.1
5.7
321
227
8.9
7.1
220
8.5
213
9.9
4LP
-
1,760
2,190
253
326
3.7
316
5.3
307
7.1
300
8.8
293
366
10.6
12.7
266
360
12.4
14.8
4LVP
3"-S
0.170
2,620
400
4.4
389
556
6.3
8.7
381
547
8.4
11.6
373
539
10.6
14.5
533
17.4
526
20.3
238
343
13.2
340
3 600
1,500
566
463
5.8
5.2
449
7.5
438
10.0
427
12.4
418
14.9
17.5
409
500
17.4
20.4
5LP
4"•S
0.350
1.760
554
5.8
7.0
540
659
8.8
10.5
529
648
11.7
13.9
518
637
14.6
17.4
509
628
20.9
619
24.4
5LVP
311 17.0
350 18.7
340
2,100
673
27.0 324
31.1
6HVP
1,930
360
890
28.4
882
Q3J
27.8
427
1,170
739
8.0
716
11.9
18.0
697
1,120
15.9
24.0
680
1,103
59.9
29.9
664
1,068
23,9
35.9
650
1,074
27.9
41.9
6LP
s„ -P
o.716
1,760
1,930
1,162
1,284
12.0
13.1
1,139
1,261
19.7
1,242
22.3
1,225
32.8
1,1510
39.4
1,196
46.0
6LVP
7HVo
q" -S
Q.367
1,760
16,0
21.4
542
24.5
536 27. 6
524
33.7
514
620
46.4 610
53.5
2,050
1,170
1,277
13.3
16.7
5,248
1,602
20.0
25.0
1,5781,557
1,224J46,6
39.2
26.0
1,203
33.3
41.7
1,184
1,538
39.9
50.0
7Lp
8„ F
1 200
1,465
1,760
1,631
1,985
20.0
1,956
30.0
1,9321,911
40 465
47,1
50.1
1,892
60.1
170
5
7LVP
21050
2 333
23.3
2 304
35.0
21.8
2 2802259
1,2981271
8HVP
58.32
36.3
24070880
1,246
43.5
33.8
875
38.6
866 43.5
850
1,170
1,366
1,871
14.5
19.3
1,329
1,834
28.9
1,8035,775
48.2
1,1
57.9
SLP
BLVP
SO"•P
1.740
1,375
2,228
22.7
2,191
34.0
2,1592,132
56.7
74.2
2,107
2,647
SS.O
89.1
1,800
2,967
29.7
2,930
44.5
2,8992,871
1
MOM
2MP
1"-S 0.017
2,800.
3,250
25 1.7
33 1.9
22
30
2.1
2.5 28
2.7
3.0
t a
2MVP
3,560
38 2.1
35
2.7 34
3.9 63
4.4
60
5.1
5 275
1,760
67 3.1
64 3.6
64
59
4.6
.+
1S
3MP
2a_g 0.060
2,265
2;7711
95 4.6,
12.5` 5S
,, 899
119
,.„,`�. 87
7.1 117
6.4
7.9
112
9.5
3MVP
3,600
175 7.2
169
9.2 167
10.2
162
12.3
.1,760
144
6.8
136
6.8
132
9.8
4MP
2%"-S
0.117
2,190
2,620
194
245
8.5
10.2
186
236
10.9
13.1
182
233
12.1
14.5
4MVP
3 600
359
237
14.0
10.5
351
227
18.0
13.4
347
222
20.0
14.9
213
17.9
209
19.4
5MP
4"-S
0.210
1,500
1,760
292
12.3
2B1
15.8
18.8
277
34B
17.5
20.9
268
339
21.0
25.1
263
335
22.8
27.2
SMVP
2,100
2 850
363
521
14.6
19.9
353
510
25.5
5d6
28.4
497
34.0
493
36.9
283
29.7
1,170
332
14.9
316
19,1
28.8
309
535
21.2
32.0
296
522
25.5
38.3
289
515
27.6
41.5
509
44.7
6MP
5"-S
0.383
1,760
1,930
558
622
22.4
24.5
542
607
31.5
600
35.0
587
42.0
580
45.5
574
735
49.1
59.7
6MVP
2 350
784
29.9
768
3B.4
761
42.7
748
51.2
741
55.5
1,170
693
28.5
671
36.6
661
40.7
7MP
6".F
0.733
1,465
1,760
909
1,125
35.6
42.8
887
1,103
45.8
55.0
877
1,093
50.9
61.1
7MVP
2,050
1,338
49.9
1,316
64.1
1,306
71.2
880
709
30.4
681
39.0
669
43.4
SMP
8".F
1.040
1,170
1,375
1,011
1,224
40.4
47-4
983
1,196
51.9
61.0
970
1,183
57.7
67.8
SMVP
1,800
1,666
62.1
1,638
79.9
1,625
88.7
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1U01MIUM
X675 f91
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44
13.0
41 3.4
3Hp
i'/<" -S
0.045
2,265
69
3.4
4.1
66
89
3.9
4.7
64 4.3
87 5.3
60
83
5.3
6.5
3HVP
2,770
3,600
91
129
5.4
126
6.1
124 6.9
120
8.4
117
10.0 113
1,760
80
4.0
77
4.6
74 5.2
4HP
1 -S
0.069
2,190
110
5.0
107
5.7
6.9
104 6.4
134 7.7
99
129
7.9
9.4
124
11.15
4HVP
2 620
139
207
6.0
8.2
137
204
9.4
201 10.6
196
13.0
192
15.3 188
17.7
-
3,600
1,50Q
154
7.0
151
6.0
147 9.
140
177
10.9
12.8
178
152 165
17.5
5HP
2h".S
0.14Q
1,760
191
8.2
9.8
187
235
9.3
11.1
183 10.5
231 128
224
15.3
218
18.1 213
20.9
5HVP
2,100
2,850
238
343
13.2
340
15.1
336 17.0
329
20.8
323
24.6 318
28.4
1,170
168
6.8
182
S0.
_
177 11.3
168
302
13.8
20.8
159
293
16.4
24.6 285
28.4
6HP
3"-S
0.227
1,760
321
13.3
316
15.5
311 17.0
350 18.7
340
22.8
332
27.0 324
31.1
6HVP
1,930
360
14.5
17.7
355
450
16.6
20.2
445 22.8436
27.8
427
32.9 419
37.9
2,350
1,170
455
332
14.2
326
16.3
319 18.3
308
22.4
297
26.5 287
30.5
38.2
7HP
1,465
441
17.8
434
20.4
428 22.9
416
28.0
405
33.1 396
39.8 504
45.9
7HVo
q" -S
Q.367
1,760
549
21.4
542
24.5
536 27. 6
524
33.7
514
620
46.4 610
53.5
2,050
655
25.0
649
2B.5
-18 -9
_ 642 _ 32.1
345 21.2
631
329
39.2
26.0
315
30.7 301
35.4
880
363
16.5
354
518
25.1
509 28.3
493
345
40 465
47,1
BHP
4"-S
0.566
170
5
220
f
609
6
95
2.8
5.3
i 72.4
8HVP
1,800
884
33.8
875
38.6
866 43.5
850
53.,2
635
6 B22
p

i � 3
Proven Performance. Global Applications. Local Support.
Below are just a few examples of the industries that, 50% Less The sound data shown compares
over the decades, have depended upon the Sutorbiho Operating Noise the Legend and a comparably sized
,u blower operating at 3,275 rpm and
Legend to deliver clean, oil -free air to a wide range ,,,�,.,, �°���a�F„v:r
of global applications. 12 psig. An improved blower design
significantly reduces the sound
Industry Application °° pressure output of the Legend
blower. The typical reduction is
Aquaculture Aeration 3 dBA which represents 50% less
Cement and Lime Fluidization and Conveying noise than the competition.
Chemical Vacuum Processing and Conveying
°a
Coal Bed/Landlill
Methane Gas ecovery
Dairy
Automated Milking
Dry Bulk Hauling
Trailer Unloading and Aeration
Environmental Services
Sewer Cleaning and
Superior Local Sales and
Service
Our extensive network of authorized
Sutorbilt distributors offers the most
convenient local sales and service sup-
port of anyone in the industry today.
These factory trained professionals
are experts in blower/vacuum pump
technology providing system installation guidance, troubleshooting and
optimization recommendations of your new or existing applications.
Even a Legendary Warranty
Every Sutorbilt Legend Series blower/ vacuum pump is covered by
an uncontested warranty for 24 months from the date of shipment
or 18 months from the date of installation on all blower materials
and workmanship. Replacement or repair costs will be at no charge
._I„A;r ran,rn frvivhr. Contact vour Local Sutorbilt
Portable Restroom Services
Industrial
Material Vacuuming
Milling and Baking
Blending and Conveying
Oil and Gas
Gas Collection and Sparging
Power Generation
Fly Ash Conveying and Aeration
Process Gas
Gas Boosting
Pulp and Paper
Chip Conveying and
Process Vacuum
Resin and Plastic
Processing and Conveying
Soil Remediation
Vacuum Extraction and Sparging
Vacuum Excavation
Potholing and Slurry Recovery
Wastewater
Aeration and Backwashing
Superior Local Sales and
Service
Our extensive network of authorized
Sutorbilt distributors offers the most
convenient local sales and service sup-
port of anyone in the industry today.
These factory trained professionals
are experts in blower/vacuum pump
technology providing system installation guidance, troubleshooting and
optimization recommendations of your new or existing applications.
Even a Legendary Warranty
Every Sutorbilt Legend Series blower/ vacuum pump is covered by
an uncontested warranty for 24 months from the date of shipment
or 18 months from the date of installation on all blower materials
and workmanship. Replacement or repair costs will be at no charge
._I„A;r ran,rn frvivhr. Contact vour Local Sutorbilt

Small Compact Filter Silencers
w/ Standard Filter Design
TS" Series 1/2" - 3" MPT
• Industrial & Severe Duty + Engines • Waste Water Aeration
+ Piston Compressors • Construction\Contractor Industry + Nailers and Staplers
• Workshop 4 Vacuum Vent Breathers
+ Screw Compressors
+ Blowers - Side Channel & P.D. • Medical\Dental Industry
+ Hydraulic Breathers — fine filtration + Pneumatic Conveying
, � o
• Polyester: 99%+ removal efficiency standard to 5 micron + Interchangeable media: Polyester, Paper, NEPA
• + Several element sizes available per given connection
Paper: 99%+ removal. efficiency standard to 2 micron
+ Fully drawn weatherhood - no welds to rust or vibrate apart (safety factor)
+ Tubular silencing design - tube is positioned to maximize + Temp (continuous): min -15°F (-26°C ) max 220°F (104°C )
attenuation and air flow while minimizing pressure drop
• 4 Filter change ouIerenti:10"-15"H2Oovr Initial delta P
Durable carbon steel construction with baked enamel Pressure drop graphs ble uponrequest
finish and powder coated weatherhood
Me . a _�-•
+ 1/8" tap holes • Available in Stainless Steel + Various media available
+ Pressure Drop Indicator + Epoxy coated housings • Special connections, BSPT
OUTLET i
Dimension tolerance + 1/4"
4LET
TYPICAL NOISE ATTENUATION — FS SERIES
20
a
v 15
I
Z
t 10
b
5
83 125 250 500 1000 2000 4000 Woo
OCTAVE BAND CENTER FREQUENCIES - Hz
Noise attenuation may vary due to the wide range of
applications and machines
i,
Note: Model offerings and design parameters may change without notice.
Solberg — Discover the Possibilities
_ FS25-406 pg` 3
1151 Ardmore Ave. + Itasca, IL 60143 USA
Sales/Service: 630.773.1363 + Fax: [phone]
E-mail: [e-mail] + Web Site: www.soibergmfg.com

ATTACHMENT
Cut -sheets and pump curve for Irrigation Dosing/Flushing Pump

1/16/2008 12:21pm wwsl 7702766535 #439 Page 11/12
pficOlm
)PUMPS
LC - 20953 Configured Curve
........ ...............
By, TGJ
Date: 10/9/2009
Rev.
lProject: waste water systems
Tag 9 P-1 P-2
P.O. #
.......... ...
Model: 20053
Oust Ref#
.,ontr@ctor:
Qty:
qent/Rep: SPE
[Engineer:
Sei-Vioe:
Doc #
............ ...... . .......... ..... ..... . .... ... ------ ..... ..... ................. . ...... ..... ... —
Pow"
=Ower
L__........._..._...._..._ . . ....... . ... ...
...... . ..... ....... ... - --------- . ........ . . .......
0 so
Cap-acky - U69pni
100
-90
-80
,70
60
-50
-40
30
20
100 150 200 250 300 350 400 450 500 sso 600 650 700
Capacity - USgpm
0 so
40,
PSHr i
.......... . . ......... . ............... .......... .. ..... ....... . ......... .. ... .. ......... .....
2
j
0 so
100 150 200 250 300 350 400 450 Soo $50 600 650 700
Capacfty - USgprn
1%
........ ...............
. ......
19.54 In
..............
....... ... . .....
L
. .. . .... ...........
.......... ...
Tamp: 68.00 dog F
-------------
Efficiencyl
v,autoff Head,
...... . ..........
S.C.: 0.998
Diff. Press,
..........
---------- . ......... . ....
Visc.: too cp
....... ...
7
p. Dis--.
9-54 In
Pump Eff.. 58.18
Of Stages,
I
... .. ...... . .
---------------
,
Motor Data
40
...
... . ....
-,minal RPM,
. ...... .... ....... . ........ .
Phase: Three phase
---------
0 so
40,
PSHr i
.......... . . ......... . ............... .......... .. ..... ....... . ......... .. ... .. ......... .....
2
j
0 so
100 150 200 250 300 350 400 450 Soo $50 600 650 700
Capacfty - USgprn
1%
t
200 USqpm
lFluid: Water
Suct Press: 0,
350 ft
Tamp: 68.00 dog F
Dls. Press,
v,autoff Head,
363 ft
S.C.: 0.998
Diff. Press,
NPSHr:
7.04 ft
Visc.: too cp
SHP: 30.3 hp
7
p. Dis--.
9-54 In
Pump Eff.. 58.18
Of Stages,
I
SEP- 426 Usgpm
---------------
,
Motor Data
40
Voltage, 208-2301460
-,minal RPM,
3600
Phase: Three phase
81- 1.15
Ant1j;ll RPM-
3500
lHz, 60
Encl.:- ODP

`0/1,6/2008 12.21pm WA I 7702766535 #439 Page 12/12
ON o e- l-,
S'? T P M S
Nominal RPM 5600 Hased on hresir 4+�atc�-C Erb drtl•., F
rr'nperrer Din rncter: 6-3/T6`-fTU t:t�
155
150
145
t -
Ll 1 q. 0
LU
� 135
0
< 130
Li
1 125
W
120
to
115
110
705
B.P.C. 4.5
5o 75 100 725 150 175 200 225 250 275 930
CAPACITY tN iJ.S•. C4ALL014C, PER MINUTE
74
70
ZZ
ZW
W
U�
65 LL
50
x
LU
'10.0 tl.'5:
hl � C7
7,.5 i w
v(;,
G
QT-TC)TED 13Y-.
TAS
Q U(xi E) To..
brooks Ja.b cliffs
SELEC ICYN
CO'L 1 ITTf7'NS
Flow:
200.0 GPM
Priming Type,
Standard,
Total Dynamic Head:
140.0 fest
M-ot"or Loading:
Standard,
PLJMP DESCRIPTION
Pump Model:
532TPMS
Priming Type:
Stondard
Impeller Diameter:
6.186 in,
I•rrrp-al•ier Material:
Iron
Suction:
2Yg"NPT
Discharge:
2"NPT
Shaft Seal:
Mechanical-
echanicalPUMP
PUMPPERFORMANCE
Flow:
200.0 GFIA
Pa.wer:
Total Dynamic Head.
1 40.6 feet
Efficiency:
73,4
Nominal Sp&ed:
3600 RPM
NPSHR,
'14 2 feet
Shut—Off Head:
154.3 feet
Wax Power:
T T.0 Bf [P
QFst Eff: 73.7 @� 21-4.C� GPM
MOTOR
Size:
10 HP
Encl2sLrre:
TEFC
voltoye: Corisull Catalog/Facto•ry
Ha/P-hose:
PRICE/ORDER
INFORMATION
ataing No.:
FWC
Fcctory
(-,ig}lt:
200 lbs_
QT-TC)TED 13Y-.
TAS
Q U(xi E) To..
brooks Ja.b cliffs

Cut-sheets for flushing return pumps j' 7'

p®p SECTION: 3.20.022
`QVi1L/7YPZA1A9 JrNGE FM2091
�. 0207
® 0 Supersedes
Product information presented0506
here reflects conditions at time
of publication. Consult fac-
tory regarding discrepancies orVisit our Web site:
inconsistencies . MAIL TO: P0. BOX ?6347• Louisville, KY 40256-0347
SHIP T0: 3649 Cane Run Road • Louisville, KY 40214-9961 woww.zoeiier.com
[phone]. 1 (800) 928 -PUMP • FAX [phone]
_1A 6ki
1 t 1
Effluent turbine pumps are used in on-site applications that
demand more head than a traditional single stage centrifugal
submersible pump. Zoeller Pump Company is able to meet this
need by offering a complete line of submersible effluent turbine
pumps. These pumps have been proven in field applications and
have many years of development behind them. Typical appli-
cations include mound systems, drip systems, and recirculating
media filters. All units include cool running submersible motors
that do not require external water flow to prevent overheating.
An outer pump sleeve is not required. Pumps can be installed
directly in a dose tank as long as an effluent filter is used on the
septic tank outlet. These pumps can also be used in conjunction
with the Zoeller Effluent Turbine Filtered STEP system.
FEATURES:
Corrosion resistant.
p Many models available - 10, 19, 27, 35, 55 and 85 GPM.
• 1/2 thru 3 HP units.
115 and 230 Volt.
p 1-1/4" discharge (10, 19, 27 gpm) or 2" discharge (35, 55
and 85 GPM).
Heavy wall stainless steel pump shell.
• Franklin Electric submersible motors.
• Stainless steel hex drive pump shaft.
p High Efficiency floating stack.
p Glass -filled Noryl discharge and mounting ring
(10, 19, and 27 GPM models).
• Stainless steel discharge and mounting ring
(35, 55 and 85 GPM models).
• No external capacitors or relays required for starting
('/2-1'/z HP).
• Starting box provided for 2 & 3 HP units.
• External check valves available.
• Pressure effluent filter available.
m 10 feet of jacketed SO type power cord ('h - 1'/z HP units
only). Consult Factory for longer lengths.
• Timed dosing panels available.
• 5 year extended warranties available. (Consult Factory
for details.)
v uuNpIlyI.,
I 10, 19,27 GPM Models 35, 55, 85 GPM Models
co
P;
SK2226

PUMP PERFORMANCE CURVE
55 GPM
2" NPT DISCHARGE
75 250
H PP210
Voltage
Phase
Amps
3 H P-7 STAGE
70 225
5034-0005
112
230
65
12.0
1
60 200
5034-0006
112
55
175
6.0
2 HP -5 STAGE
50
5034-0007
314
45
150
8.0
2
v
125
1.5 HP -4 STAGE
z 40
125
9.8
3
0 35
1.5 HP
0 30
100
1HP-3 STAGE
13.1
25
30-3116°
5034-0010*
2
75
314 HP -2 STAGE
20-
5
32-5116"
15-
50-
230
1
14.5
1/2 HP -1 STAGE
10
STAGE
10
25
5
25
0
5
10 20 30 40 50 60 70 80 90 100
GALLONS
[_ITERS 0 40 80 120 160 200 240 280 320 360
FLOW PER HOURIMINUTE 015649
Part Number
H PP210
Voltage
Phase
Amps
Stages
Height
5034-0005
112
230
1
12.0
1
18-5116"
5034-0006
112
230
1
6.0
1
18-5116"
5034-0007
314
U
40
1
8.0
2
21-9116"5034-0008
125
1
z
0 35
1
9.8
3
24-314"5034-0009
1.5 HP
1-112
100
1
13.1
4
30-3116°
5034-0010*
2
230
1
13.2
5
32-5116"
5034-0011*
3
230
1
14.5
7
40-7116"
*Incl udes starter box and 25' long flat wire cable assembly.
PUMP PERFORMANCE CURVE
85 GPM
2" NPT DISCHARGE
60
200
Voltage
Phase
Amps
3 HP -6 STAGE
55
5035-0005
314
230
175
8.0
1
50
5035-0006
1
230
45
x
150
2
24"
5035-0007
17112
U
40
1
2 HP -4
STAGE
30-118"
125
2
z
0 35
1
13.2
4
32-718"
1.5 HP
0 30
100
_
3 STAGE
25
6
42-3/8"
75
20
1 HP -2 STAGE
15
50
314 HP -1
STAGE
10
25
5
I
0
20 40 60 80 100 120 140
GALLONS
LITERS 0 80 160 240 320 400 480
FLOW PER HOURIMINUTE 015545
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5035-0005
314
230
1
8.0
1
20-118"
5035-0006
1
230
1
9.8
2
24"
5035-0007
17112
230
1
13.1
3
30-118"
5035-0008*
2
230
1
13.2
4
32-718"
5035-0009*
3
230
1
14.5
6
42-3/8"
*Includes starter box and 25' long flat wire cable assembly.
Accessories
Filtered STEP System
Zoeller Pressure Effluent Filter
This Zoeller Filtered STEP
The Zoeller Pressure Filter will help
System is designed as an
prolongthelife of an on -site drainfiel d
economical and reliable
by filtering out solids which cause
solution to an On -Site
plugging. Used in both residential and
pumping requirement.
commercial applications, this unique
When the effluent must
design and mounting location allows
be pumped up hill, for
easy access to the filtering screen.
enhanced flow, pressure
sewerorwhere alternative
Use in low-pressure pipe, drip, or
systems require high head,
enhanced flow applications. Use as a
the Filtered STEP System
prefilter for dosed treatment devices
is the answer without the
such as recirculating media filters.
extra cost of a pumping
chamber.
For use with pumps up to
55 GPM. Contact Factory
for 85 GPM applications.
See FM2244 for more information.
See FM2090 for more information.
© Copyright 2007 Zoeller Co. All rights reserved.

Not,
All brass spring loaded check valves are designed to
screw directly into the pump discharge. Check valves
are assembled with components suitable for a septic
environment. Check valves should be used at the pump
in a pressure sewer system. A redundant PVC check
valve and isolator (ball) valve should also be used at
the sewer connection in pressure sewers.
Part
Number
Piping
Size
Pressure
Rating Weight
30-0187
1-1/4"
400 psi 2lbs.
30-0189
2"
400 psi 3 lbs.
1541
PVC check valves can be used inline with the pump
discharge piping or at the street service connection in a
pressure sewer system. Check valves are a true -union
design so they can be removed and serviced without
cutting the pipe. Clear PVC for easy inspection and
connection via a qlue joint.
Part
Number
Piping
Size
Pressure
Rating
Weight
30-0207
1"
125 si
Ilb.
30-0209
1-1/2"
125 si
Ilb.
30-0210
2"
125 si
3lbs.
Rail systems are used for easy pump removal from an efflu-
ent pit. Service personnel will not need to enter a hazardous
environment. Pump sits on floor and engages piping system
via a sliding disconnect fitting. All parts are stainless steel or
brass and suitable for a septic environment.
Part
Number
Piping Size
Weight
39-0098
1-1/4" Female pipe thread
10 lbs.
39-0099
1-1/2" Female pipe thread
11 lbs.
39-0100
2" Female pipe thread
12 lbs.
Disconnects Only
Part
39-0053
dPipeNumberWeight
�Ibs..39-0001
39-0002 1
2"
2.5 lbs
Stainless Steel Pull Rods
ALL ZOELLER_ ONSITE WASTEWATER PRODUCTS MUST BE INSTALLED IN ACCORDANCE WITH LOCAL AND/OR STATE PLUMB-
ING AND/OR HEALTH DEPARTMENT CODES.
© Copyright 2007 Zoeller Co. All rights reserved.

120
112
104
95
8s
w 80
72
z s4
56
o 48
40
32
24
1s
8
0
GALLONS
LITERS
0 8 16 24 32 40 48 56 64
FLOW PER MINUTE 015413
Part Number
..ICURVE
PUMP PERFORMANCE
10 GPM
1 1/4" INIPT DISCHARGE
Voltage
Phase
Amps
MINE����
Height
OEM
112
■■■■
■NON00
1
7
6
22-318"
5030-0006
1/2
230
1
6.0
6
22-318"
5030-0007
GALLONS
LITERS
0 8 16 24 32 40 48 56 64
FLOW PER MINUTE 015413
Part Number
HP
Voltage
Phase
Amps
Stages
Height
5030-0005
112
115
1
12.0
6
22-318"
5030-0006
1/2
230
1
6.0
6
22-318"
5030-0007
1/2
115
1
12.0
8
24-118"
5030-0008
112
230
1
6.0
8
24-1/8"
5030-0009
3/4
230
1
8.0
12
28-7/8"
27 GPM Model
HP
PUMPPERFORMANCE CURVE
I -a
dpi€?
E 27 GPM
8F
1 1/4" NPT DISCHARGE
t
3fi 320 7 12HP-70 STAGE
.,. 300-E
_
y@ }`€ ,
g Q g t
72 240N,1
s4
220-
2W
20E
200GE p"'s {may` p /71M
i 56 iB0
46 760
40
� 40 2
1E
LITERS 0 20 40 50 50 - — tau
FLOWPERMINUTE 015045
Part Number
HP
Voltage
Phase Amps
Stages
Height
Height
1l2
115
1 12.0421-118'230
1
1%" NPT DISCHARGE
80
280
1 HP -9 STAGE
1 6.0
4
21-118"230
AMEAR
314 HP
7 STAGE
21-15116"
1 8.0
6
24-5116"230
64
200
7
1 9.8
7
26-7116"
230
1
230
1 13.1
10
31-718°
015414
Part Number
H P
.19 GPM Models
Phase
Amps
PUMP PERFORMANCE CURVE
Height
5031-0005
19 GPM
115
1
1%" NPT DISCHARGE
80
280
1 HP -9 STAGE
112
230
72
240
314 HP
7 STAGE
21-15116"
5031-0007
314
230
64
200
7
25-1116"
5031-0008
1
230
1
0 56
= 48
160
28-118"
5033-0009
1-1/2
230
1
13.1
52
40
�7 325
120
W
12 HP
STAGE
24
80
16-
40-
a-
0--
05
5 10 15 20 25 30
GALLONS
LITERS 0 20 40 60 80 100
FLOW PER MINUTE
015414
Part Number
H P
Vdtage
Phase
Amps
Stages
Height
5031-0005
1/2
115
1
12.0
5
21-15/16"
5031-0006
112
230
1
6.0
5
21-15116"
5031-0007
314
230
1
8.0
7
25-1116"
5031-0008
1
230
1
9.8
9
28-118"
5 GPM Models
w w PUMP PERFORMANCE CURVE
35 GPM
2" NPT DISCHARGE
56 180
1.12 HP- 5 STAGE
48 160-
140- 1 HP-4STAGE
40
120
314HP-3STAGE
32 100
O
24 B0 112HP-2STAGE
O
60-
16
40
8
20
0
10 20 30 40 50 60
GALLONS
LITERS 0 40 80 120 160 200
FLOW PER MINUTE 015044
Pa t Number
H P
Vdtage
Phase
Amps
Stages
Height
5033-0005
112
115
1
12.0
2
19-7116"
5033-0006
112
230
1
6.0
2
19-7116"
5033-0007
314
230
1
8.0
3
22-3116"
5033-0008
1
230
1
9.8
4
24-15x16"
5033-0009
1-1/2
230
1
13.1
5
29-15116"
© Copyright 2007 Zoeller Co. All rights reserved.

120
112
104
96
88
o so
72
U
z 64
66
0 48
~ 40
32
24
18
0
10 GPM Models
I CURVE
.PERFORMANCE
i GPM
11/4" NPT DISCHARGE
H P
Voltage
Phase
Amps
nor
Height
.,
115
1
12.0
6
22-318"
5030-0006
1/2
230
1
6.0
6
22-3/8"
GALLONS
LITERS —�—
p 8 16 24 32 40 48 56 64
FLOW PER MINUTE 015413
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5030-0005
112
115
1
12.0
6
22-318"
5030-0006
1/2
230
1
6.0
6
22-3/8"
5030-0007
1/2
115
1
12.0
8
24-1/8"
5030-0008
112
230
1
6.0
8
24-1/8"
5030-0009
314
230
1
8.0
12
28-7/8"
rw
7 GPM Models 70 t
FLUNPEP.MINUTE
p
015045
Part Numbe
HP
Voltage
Phase
Amps
Stages
Height
5032-0005
112
115
1
12.0
4
21-1/8"
5032-0006
1/2
230
1
6.0
4
21-118"
5032-0007
3/4
230
1
8.0
5
24-5116"
5032-0008
1
230
1
9.8
7
26-7116"
5032-0009
1-112
230
1
13.1
10
31-718'
19 GPM Models
LL PUMP PERFORMANCE CURVE
19 GPM
1W NPT DISCHARGE
280
80 7,-9STAGE
72 240 314 HP
7 STAGE
64 200
0 56
=
48
160
V
¢ 40 112 HP
120 5 STAGE
32
Q
24 80
16
40
8
5 10 15 20 25
GALLONS
LITERS 0 20 40 60 80 10
FLOW PER MINUTE
015414
Part Number
H P
Vdtage
Phase
Amps
Stages
Helgm
5031 -ODDS
1l2
115
1
12.0
5
5031-0006
1/2
230
1
6.0
5
d25
5031-0007
3 4
230
1
8.0
7
-1/16'
5031-0008
1
230
1
9.8
9
35 GPM Models
w PUMP PERFORMANCE CURVE
35 GPM
T NPT DISCHARGE
56 180
W
48 160
140
40
120
x
32 100
r
0
0 24 80
E
40 i 8
20
0
10 20 30 40 50 60
GALLONS
LITERS
0 40 80 120 160 200
FLOW PER MINUTE 015044
Part Number
HP
Voltage
Phase
Amps
stages
Helgm
5033-0005
112
115
1
12.0
2
19-7116"
5033-0006
112
230
1
6.0
2
19-7116"
5033-0007
314
230
1
8.0
3
22-3116"
5033-0008
1
230
1
9.8
4
24-15116"
5033-0009
1-112
230
1
13.1
5
29-15!16"
© Copyright 2007 Zoeller Co. All rights reserved.

/7 FM2218
�l!!IL/TY /-1/M- 9NGTT Iq�Vp o' 0206
L Supersedes
® ® 1204
Product information presented P
here reflects conditions at time d
of publication. Consult fac-
tory regarding discrepancies or Visit our Web site:
inconsistencies. MAIL T0: P0. 80X 16347• Louisville, KY 40256-0347
SHIP T0: 3649 Cane Run Road - Louisville, KY 40211-1961 www.zoefeCCom
[phone]. 1 (800) 928 -PUMP . FAX [phone]
EFFLUENT TURBINE PUMP INFORMATION
Cable Guide: SJOVV: Junior hard service, same cons
*Dry run capable for up to 24 hours without damage.
**Minimum Liquid Level (measured from bottom of pump).
©Copyright 2006 Zoeller Co. All rights reserved.

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Rose Hill
"Percy Ri te" DATE: 09/22/07
Waste Water Systems, Inc.
P.O. BOX 1023 [phone]
FI I IJAY. (.A 3t754n Fnx (7016) X76--6535

PUMP A PUMP P
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24 VAC CONTROL
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Waste
Water
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REV -0
Rose Hill
P.O. BOX
1023
[phone]
DATE: 09/22/07
^ "Perc�R,ite"• _ _ ,.
ELLIJAY.
GA. 30540
Fclx (70161 97F-F53'�

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01 Rose Hill P.O. BOX 1023 [phone]
DATE: 09/22/07
"Perc`R,ite"m _ _ ELLIJAY. GA. 30540 Fax [phone]

bedrock. The top surface of layer one was set to actual field survey elevations and given a
layer thickness of 5'. Layer two for each model was given a uniform thickness of 100' based
on the depth of the deepest boring measured from the bottom of Layer 1. Layer 3 was given
a uniform thickness of 100' measured from the bottom of layer 2.
5.5.2.2 Time Parameters
The groundwater model was analyzed as a steady-state model. A model run time of 365
days was used as the time period of simulation. Loading rates were calculated at a yearly
rate to successfully calculate the annual loading rate for the groundwater model.
5.5.2.3 Hydrogeologic Parameters
Monthly precipitation data was averaged over a 30 year period to determine a precipitation
rate of 48.6 inches/year for the study site. An annual evapotranspiration rate value of 28.2
inches/year was subtracted from the averaged precipitation value for a net precipitation rate.
An industry held practice of utilizing 10 percent of the net precipitation rate was utilized as a
baseline groundwater recharge rate. 2.1 inches/year was applied to the surface layer 1 of the
model to simulate the groundwater recharge that occurs naturally. Additional recharge
values were utilized to calibrate the base model to field conditions, Hydraulic conductivity
values, well head observations, and stream elevation observations were utilized in the
groundwater model to simulate the actual field conditions.
5.5.3 Boundary Conditions
A River boundary condition was utilized to model the effect of the branch that exists along
the eastern side of area F. Each cell had a specified stage level, branch bottom level, and
bottom conductance value assigned to it, taken from field data from the site survey. The
bottom of layer 3 and the outer perimeter cells are considered no -flow boundaries.
5.6 Model Calibration
The base groundwater model was calibrated using actual field measurements of well levels
and hydraulic conductivity. Recharge values were varied to achieve a model that simulated
in-situ field conditions within 0% - 10% Root Mean Square Error. The base numerical
groundwater model of area F was calibrated to 3.815% Root Mean Square Error. The
calibration graph is included in Attachment D.
Brooks Engineering Associates, PA Hydrogeological Assessment Report
BEA Project No. 307808 23 The Cliffs at High Carolina

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FIELD VALVE CONNECTIONS
1 of 1
Waste
Water
Systems, Inc.
®
REV_O
Rose Hill
P.O. BOX
1023
[phone]
"PercaRite'<
DATE: 09/22/07
ELLIJAY,
GA. 30540
Fax (7O6) 276-6535

Cut -sheets for drip system valving

ILI%JI VDI VG_
700 & 800 SENE5 111110111.,
Basic
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Tie "basic Model 700/705 diaphragm -actuated and the 800/805
�01,�pl
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Ston -actuated valves are hydraulica0y-operated, globe valves in either
the standard oblique M or angle pattern design. Each valve comprises
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two major components, the body -seat assembly and the actuator
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assembly.
The actuator assembly is unitized and is removable from the body as
an integral unit, It consists of both an upper and a lower control -chamber.
Each basic valve can easily be configured, on-site, either as a
single -chamber con r l vale (Model 705/805), or a double -chamber
control valve (Model 700/800). The shaft sub -assembly, in both single
and double -chambered versions is center -guided, providing an
unobstructed seat area.
The Model 700/800 Basic double -chambered valve operation is
independent of valve differential pressure since the line pressure actually
serves as the actuator differential pressure. This develops maximum
_
power, ensuring immediatevalve response, 'The upper control -chamber
Diaphragm Actuated valve `
is pressurized to close, and vented to open the valve. The lower control -
chamber ispressurized
chamber is usually vented to the atmosphere, but ca also be
to power the valve open, I
The Model 705/805 Basic Valve uses valve differential pressure to power
the actuator open or closed. The lower control -chamber, which serves
to cushion the closing of the valve, is exposed to the downstream
pressure, through a fixed orifice connected to the downstream side of
the valve. The pressure in the upper control -chamber varies, usually
resulting from the combined action of a regulating pilot and a fixed
orifice. This varying pressure modulates the valve to open or close.
`
The Basic Hydraulic Valve is available in a wide range of materials, sizes,
-
pressure ratings, and end connections. Single or double -chambered
f
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versions are used as the main valve in all 700 and 800 Series applications.
f
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ISO PN 25; 25 bar# 03 0:6 psi
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Ductile iron EN 1563 (ASTM A-536)
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Stainless steel and bronze
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NSF 61 and WRAS approved
or Electrostatic Polyester Powder, RAL 6017 (Green)
WRAS approved
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Carbon steel (ASTM A-216-WCB)
Stainless steel 316 CFBM (316)
Aluminum
Nickel Aluminum Bronze
Titaniurn
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254 SN110
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Hastailoy C-276
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4�'ERMAD WatEpwopks
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460
815
1,250 1,850
1,990 3,310 3,430
3,550
Cv
49
58
64
133
230
530
940
1,440 2,140
2,300 3,820 3,960
4,100
Kv
36
43
47
98
170
391
693
1,063 1,573
1,692 2,814 2,916
3,018
Cv
41
49
54
113
200
450
800
1,230 1,820
1,950 3,250 3,370
3,490
Kv
46
55
61
127
2.20
506
897
1,375 2,035
2,189 3,641 3,773
NA
Cv
53
64
70
-146
250
580
1,040
1,590 2,350
2,530 4,210 4,360
NA
Kv
39
47
51
108
187
430
762
1,169 1,730
1,861 3,095 3,207
NA
Cv
45
54
59
124
220
500
880
1,350 2,000
2,150 3,580 3,710
NA
inch 24" 28"
3
G -Pattern
Kv 7,350 7,500
7,500 7,500
Flat Disc
Cv 8,490 8,670
8,670 8,670
Valve flow coefficient, Kv or Cv
Kv(Cv)=Q FG -f
VtIhere:
Kv = Valve flow coefficient (flow in r-n'!h at I bar Diff. Press.)
Cv = Valve flow coefficient (flow in gpm at Diff. Press. I psi)
0 = Plow rate (r-n"/h ; gpm)
AP = Differential pressure (bar; psi)
Gi = Liquid specific gravity ONater = 1.0)
Cv = 1.155 Kv

101
X00 Series
METAL BODY HYDRAULIC I ELECTRIC
CONTROL VALVES
TECHNICAL DATA
Specifications
• Valve Configuration:
Y -pattern and angle
• Sizes:
Y — Y -pattern: 11/2", 2" & 3"
A —Angle: 2"
• End Connections:
- 11/2" & 2": threaded NPT, BSP
— 3": female threaded NPT/BS or
flanged to ANSI/ISO/BS-D
• Operating Pressure Range;
10-150 psi (0.7-10 bar)
• Temperature Range:
Water up to 180°F (80°C)
• Materials:
Body: (11/2" & 2") Brass,
(3") Polyester -coated Cast Iron
Actuator: Plastic, Brass and
Stainless Steel
Diaphragm: Nylon -fabric,
Reinforced Natural Rubber
Seals: BNR and NR
Flow Chart
Aimensions and Weiahts
I W4 ■ r4fil W-11 U 9 4 WWRIM
Model 310
Electric Control Valve
Model 310 has a 3 -way solenoid pilot
valve with manual override.
Standard: N.C, (normally closed), requiring
electrical energy to open.
Option: N.O.

Simple Dag. Delive
3/4" LOW -FLOW PRESSURE REGULATOR
OUTLET PRESSURE VS. INLET PRESSURE AT 1.3 GPM
50
40
30
20
10
0
0 28 56 84 112 140
Inlet Pressure (psi)
Product Advantages
• Instant response to variations in pressure assures that outlet pressure will remain constant
regardless of inlet pressure.
• Pressure Regulators are preset with flows from 3.5 to 175 GPM.
• Manufactured from non -corrosive, high quality plastic and bross, to withstand all fertilizers
and chemicals in common use.
• Regulating unit has a stainless steel spring and screw.
• The EOPM rubber diaphragm creates a tight seal eliminating leakage.
• The rise versus the decline in outlet pressure has significantly decreased ensuring better
hydraulic perfomance,
• Sealed regulating unit is field replaceable and easy to maintain.
• Built-in operating indicotor visually shows when proper outlet pressure is achieved.
• New regulating units are compatible with existing Pressure Regulator bodies.
3/411 Lowit Flow
Pressure "ulator
• Improved in-line unit.
• Female threaded 3/4" x 3/4° connections
• One-piece sealed unit regulates accurately
at low flows.
• Silicon diaphragm and stainless steel
spring -- no leakage.
Applicafims
For use in drip and sprinkler irrigation
systems.
il
• Available in the following pre-set pressures:
9, 12, 15, 20, 25, 30, 35, 43, 50, 57 and 65 psi
314" Low Flow available in: 15, 20, 25,
35 and 43 psi
• Maximum operating pressure: 145 psi
4 "
NETAFIM USA
5470 E. Home Ave. • Fresno, C4 93727
888.638.2346 e 559.453 6800
FAX [phone]
www.netafimusa.com
" x 6
3" x 10
Applicafims
For use in drip and sprinkler irrigation
systems.
il
• Available in the following pre-set pressures:
9, 12, 15, 20, 25, 30, 35, 43, 50, 57 and 65 psi
314" Low Flow available in: 15, 20, 25,
35 and 43 psi
• Maximum operating pressure: 145 psi
4 "
NETAFIM USA
5470 E. Home Ave. • Fresno, C4 93727
888.638.2346 e 559.453 6800
FAX [phone]
www.netafimusa.com

3.5 8 12 1G 17.5
Flow Rate (per ngakiting unit)
PART NUMBERS
60
55
50
45
40
35
30
25
20
15
10
5
0
EXAMPLE:
• Given flow Rete = 63 GPM. Nominal
required pressure = 20 psi_
• ilsing Pressure Regulator Model 2" x 6
(6 regulating units) will result in 10.5 GPM
per reguloting unil.
• i0,5 GPM per regulating unit will result in an
output pressure of 18 psi. (See Regulated
Pressure vs. Flow Rate graph).
• Head loss of Pressure Regulator 2" x 6 at
63 GPM is 5 psi, (See Head Lass vs. Flow
Rate graph).
• Design pressure at inlet of Pressure Regulator
should he 18 + S = 23 psi_
.,� '����".Y'fi'a S'ir4��''n..���c uv ����� �✓�1�3iv.^s���)�i�u!rG�`� .✓r.,-�w�"!�`f�`n.�J.
HEAD LOSS vs FLOW RATE (3x10)
12;
10
2
90 105 120 135 150 165
175
Ftow Ruts (GAVI)

so gag
R
The Dorot Quick Reacting Relief (QR) Valve is a direct -sealing diaphragm valve activated by line pressure
and controlled by an adjustable pilot. When the network pressure exceeds the pressure setting of the pilot,
the valve fully opens instantly, When the network pressure decreases below the set point, the valve closes
slowly,
Standard FeatupeS (see diagram)
A. Self -Cleaning Filter
B, Needle Valve
C. Ball Valves
D. Quick Response Pilot (66-300)
E. Quick Response Relay 2" (for 6" and larger valves)
The 2" QR valve (bronze) is available in a globe or angle pattern. A
pilot (68-200) with a built-in needle valve ensures slow closure.
The QR valve is installed on a tee -junction in a pipeline and releases
excess pressure to protect the pipe network from dangerous surges.
The slow closing of the valve, adjustable with a needle valve,
prevents secondary surges,
design uonswepations
* The QR valve is not a modulating valve and should not be used to maintain a certain pressure in
the network. A pressure sustaining/relief valve should be used.
* A quick reacting pressure relief valve cannot prevent water -hammer caused by power failure, A
surge anticipating valve should be used.
* The use of an isolation valve is recommended at the upstream side of the QR valve.
0 A discharge pipe attached to the downstream side of the valve
must be sized for the maximum flow and not restrict the flow.
QR valves operate in case of emergency, usually for a short
time, The valve should be sized to accommodate 50%-80%
of the system's nominal flow rate.
Recommended Maximum Flow Rates (GPM)
C
Pilot Specs
Flow 450
1,100 1,700 4,000 7,000 10,000 15,000 28,000
Pilots
5
*The green spring is standard
8-30 PSI
for the 68-200 and the red
Green
spring is standard for the 66-300
14-100 PSI
Allot.
115-360 PSI
30-190 PSI
Black
N/A
68-200
66-300
For detailed information, material specifications and
dimensions,
see the Dorot Basic Valve brochure.
C
Qualify Works
NETAFIM IRRIGATION, INC.
WEST COAST: 3025E Hatt -,,Ion - Fresno, CA 93721
[phone] - FAX (POC) 442-3110
FAST COAST: 548N. Douglas Ave. - Altamonte Springs, FL 32714
(407) 788 _63
52 . FAX [phone]
Pilot Specs
68-200
66-300
apring
Yellow
8-30 PSI
8-30 PSI
Green
14-140 PSI
14-100 PSI
Red *
115-360 PSI
30-190 PSI
Black
N/A
100-360
1 Dimensions
Pori Size
Height
6 V�"
91,
Width
2"
3 112� "
Max. Press,
350 PSI
350 PSI
Materiols
Body bonnet
Brass
Brass
Plunger
St. Steel
St. Steel
Diaphragm
Not. Rubber
Not. Rubber
0 -rings
Nitrile
Nilrile
Qualify Works
NETAFIM IRRIGATION, INC.
WEST COAST: 3025E Hatt -,,Ion - Fresno, CA 93721
[phone] - FAX (POC) 442-3110
FAST COAST: 548N. Douglas Ave. - Altamonte Springs, FL 32714
(407) 788 _63
52 . FAX [phone]

ATTACHMENT I
Cut -sheets for Flow Meter

=CAM=CAMT TOTALIU
SEALED METER R r"('o F 1 K 1
SIZES 6 17
MOM L MI [ RAMOV iBE MANE E i d -id 1l iF a{ 10 91-a i ryhwk
;tl
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i
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tt ry
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thg
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t. c�.= wo „:u
% 0,01, F. o l i u3t, ",.s vionvans [
iz°".. .�> Y:3 S� 4 :!
in A
WER&vrrew; FLOWS
40 17
It Two 5 K€ MM i? -c h rf alit uS I
on am y 0 Wn map v"" 'x
�
DW mmxum
lay, a ti ,l, i:.. , n
I
n—i 11 only T, tF : oaf 3( to =Am
,&,,. ii ] iirI is Acv
�
4001 Eon: —140;'i iI ., i 7 1 �(.d his
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ff
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(€lt a! r
u to MA
,h
81 pay, plow was on,
fi kl i
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( 7
z
j
NV
SEALED METER R r"('o F 1 K 1
SIZES 6 17
ACCURACY RAC
POT a Mlkl I_ ., t r. rf mug4
s
i
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MAMMIUM, FLOWS
in A
WER&vrrew; FLOWS
40 17
cli !As! q
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ff
M..
M....A i y^ I FR1A -S
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low, A117011PYK40 n7 i,1
if
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f i'

�e9 � 1
300 psi FLANGED TUBE METER
SEALED METER MECHANISM -- MAGNETIC DRIVE
INDICATOR -TOTALIZER
SIZES 3" thru 48
E - Bolt Circle
F - Number of Bolts
G - Size of Bolts
1
METER
& PIPE
SIZE
*LOWVELOCITY
CONSTRUCTION
MIN. - MAX:
FLOW RANGES,GPM
STANDARD HIGHVELOCITY
CONSTRUCTION CONSTRUCTION
MIN. - MAX. -INT. MIN. -MAX.
DIMENSIONS
SHIPPING
WEIGHT
POUNDS
A
Bi
82
C
D
E
I
F
G
H
K
3
40-250
45-250-350
N/A
18
81/4
5
11/8
7
6518
8
3/4
53116
9
85
4
50-500
55-500-700
200-700
18
10
63/16
1118
7
7718
8
314
53/16
9
122
6
90-1200
120-1200-1500
300-1500
22
121/2
81/2
13/8
9
105/8
12
3/4
61/4
9
167
8
100-1500
150-1500-2000
400-2500
24
15
105/8
19116
9
13
12
7/8
71/4
9
237
10
125-2000
180-2000-3000
500-3500
26
171/2
123/4
15/8
10
15114
16
1
81/2
11
310
12
150-2800
200-3000-3500
800-5000
28
201/2
15
113/16
10
173/4
16
11/8
91/2
11
� 400
14
250-3750
300-4000-4500
1000-6000
42
23
16114
115/16
12
201/4
20
11/8
10112
131/2
600
16
350-4750
400-5000-.6000
1200-7500
48
251/2
181/2
21/16
12
221/2
20
11/4
111;2
131/2
800
18
450-5625
700-6000-7500
1500-9000
54
28
21
23/16
15
243/4
24
11/4
121/2
131/2
1080
20
550-6875
850-8000-9000
2000-12000
60
301/2
23
27/16
15
27
24
11/4
131/2
13712
1260
24
800-10000
1000-10000.13500
3000-15000
72
36
271/4
211/16
18
32
24
11/2
173/4
23
2040
1200-15000
1800-15000-21000
4000-25000
84
43
35
215/16
18
391/4
28
13/4
203/4
23
3220
x-30
I 36
1500-20000
2000-20000-30000
5000-35000
96
50
42
33/16120
46
32
2
23314
23
4550
42
2000-28000
3000-30000-40000
6000-50000
108
57
507/16
37116
24
523/4
36
2
28
36
5900
48
2500-35000
5500-35000-50000
1 7000-60000
120
65
587116
38?16
24
60314
40
2
31
36
7200

h
Cut -Sheets for Disc Filtration System

MOMMM WOMM'.
Fully Automatic Disc Filters
For 50-800 GPM Flow Ranges
4
2" & 3" DISCALEEN FILTERS
Headloss
0.2
40 100 200 400 1000 2000
Flow Rate (GPM)
Product Advantages
• Quick Installation — factory assembled and tested, arriving on a pallet ready for hook-up
and immediate operation.
• Less Maintenance — molded spine, chemically resistant and performs reliable backflush.
Manual cleaning is practically eliminated.
• Filtration Grade Versatility — filtration discs can be changed quickly and easily from
40 mesh up to 200 mesh.
• Optimizes Irrigation — less backflush time means more uniform application of water in the
field.
• System Flexibility — each Disc-Kleen Battery is capable of handling a wide operational flow
range.
• Lasts Longer — manufactured from engineered synthetics to resist rust and corrosion from
chemicals and weather.
• Standard with installed polypropylene drain manifold.
Filtration Process
As dirty water travels through a
Disc-Kleen Filter, debris is captured
along the walls and in the grooves of
the channels in the filter element.
During the backflush cycle, the valve
changes position, the pressure in the
outlet manifold loosens the discs
automatically. A specially designed
nozzle system inside the filter stack
then sprays pressurized water against
the loosened discs, spinning them
clean quickly and efficiently. After
backflushing, the stack of discs
automatically compress to resume
filtration.
PART NUMBERS
�io R� �I°a.olrl
26A$KPP2A3
2"
3
4" GR
Filter Body:
Glass Reinforced
� ate:
Polyamide
Spine:
Polypropylene
0 -Rings and Seals: EPDM
26ASKPP3A4 XXX
3" r
9
b" G�; ,:
2bA5KPP3A5 XXIf
3"
5 !
OR
,6"
Subsfitute XXX for proper mesh size. GR = Grooved.
" Disc-Kleen
Filter Battery
Applicaflons
• For surface water containing algae and
other organic materials such as reservoirs,
canals, rivers and waste water applications.
• For well water containing light sand
(6 ppm) and other contaminants.
SpecificarHons
Includes installed drain manifold
Inlet and outlet connections: Grooved
Backflush valve flush port: 2" NIPT
Maximum operating pressure: 140 psi
Minimum backflush pressure required:
40 psi downstream of filter during backflush
Minimum backflush flow per spine: 35 GPM
Minimum pH: 5
Mesh sizes and color: 40 - Blue
80 - Yellow
120 - Red
140 - Black
200 - Green
Materials
Manifold:
Polypropylene
Filter Body:
Glass Reinforced
Polyamide
Spine:
Polypropylene
0 -Rings and Seals: EPDM
ME r K
NETAFIM USA
5470 E. Nome Ave. • Fresno, CA 93727
888.638.2346. 559.453.6800
FAX [phone]
www.netafimusa.com

2" x 2 FILTERS
WATER SOURCE MAXIMUM FLOW RATE (GPM)
3" x 3 FILTERS
WATER SOURCE MAXIMUM FLOW RATE (GPM)
M:t In
r ra
2" x 3 FILTERS
WATER SOURCE MAXIMUM FLOW RATE (GPM)
CIEMBIM00
Good 270 24,0„„.� 20 , 180.;
3” x 4 FILTERS
WATER SOURCE MAXIMUM FLOW RATE (GPM)
:e a r ar
2” x 4 FILTERS
WATER SOURCE MAXIMUM FLOW RATE (GPM)
Good * 3b s. + 320 ...24Q 240 ,
g Ye ,.PaoE � ,.� i1bA -� 4Q •�12Q , 80
3" x 5 FILTERS
WATER SOURCE MAXIMUM FLOW RATE (GPM)
AYera e
IMPORTANT NOTE: We have categorized water quality as a guideline for filtration requirements. Be aware all water quality categories shown above are general. Your water quality may vary. If your water
contains more than two paras per million of sand, a sand separator is recommended. If in doubt, consult an authorized Netafim USA dealer.
r--7
a E -
� e
F
r a �
x�
If ,
3" DISC-KLEEN FILTER BATTERY DIMENSIONS
6
4j4,P= � X34 baa iD 3ja '41 �jn�, � a/a 22 � 4p7 fbs 72 allons
5qf? ., 4 3, a ;w, 34 rjta : Sfl 3%{ , ' 4 T �js 7 ?/e 23 46716s 40 galfans x .,
I- G
9
r
�
I- G

ATTACHMENT K
Cut -Sheets for Rainbird Rain Gauge

Rain Bird Rainfall Gauge
The Rain Bird Rainfall Gauge customizes the
weather data gathering features of
Maxicomz by providing site-specific rainfall
measurements. The central controller
retrieves this information daily, adjusting
station runtimes using the site-specific
weather data. The Rainfall Gauge may be
used to automatically interrupt Maxicomz
during an irrigation cycle if it starts to rain.
If enough rainfall occurs, further irrigation
will be cancelled. If only a small amount of
rainfall occurs, irrigation will resume,
adjusting runtimes for the amount of
rainfall that occurred.
Features
• Identifies localized rainfall and adjusts
system operation accordingly
• Watering cycle can be interrupted or
cancelled when rainfall commences
• Provides site specific rainfall
measurements in increments of 0.01"
(.025 cm)
• Heavy-duty construction, with a gold
anodized aluminum collector funnel and
white baked enamel coated aluminum
sensor housing
• Filter screen for capturing debris
• Integrates into the Maxicom2 system
using the Rain Bird pulse decoder for
two-Mre CCU systems, or directly to the
sensor input on ESP -Site and MAXILink
satellite controllers
Specifications
• Resolution: 0.01" (.025 cm)
• Accuracy: 1.0% at 1" (2.5 cm)/hour or less
• Average switch closure time: 135 ms
• Maximum bounce settling time: .75 ms
• Maximum switch rating: 30 VDC @ 2 A,
115VAC @lA
• Temperature limits: +32° F to +125° F
(0° C to +52° C)
• Humidity limits: 0 -100%"
• Height: 4.5" (11,4 cm)
• Weight: 1.5 pounds (0,68 Kg)
• Receiving orifice diameter: 3.80" (9, 7 cm)
Cable: 60 feet (18 meters)
Model
• RAINGAUGE
Rain Bird Anemometer
(Wind Speed Meter)
The Rain Bird Anemometer provides
additional customization to the Maxicomz
Central Control system by providing site-
specific windfall measurements. Local wind
speed is captured by the Wind Speed Meter
and input to the Cluster Control Unit (CCU).
The CCU can interrupt irrigation when wind
velocity reaches a programmed set point.
Interrupting a watering cycle during windy
conditions saves water, avoids property
damage, and improves sprinkler distribution
uniformity.
Features
• Precision three -cup anemometer for
measuring wind velocity
• Balanced rotor and low friction bearings
detect wind speeds from 4 MPH to
80MPH (6,5 to 128 km/h)
• Electronics supplied with a weather tight
enclosure exceeding NEMA 4 and 6
specifications
• Mounting bracket and 20 feet (6 meters)
of cable
• Identifies localized wind speed and
adjusts system operation accordingly
• Watering cycle can be interrupted during
windy conditions
• Integrates into the MaxiCom'- system
using the Rain Bird pulse decoder for
two -wire CCU systems, or directly to the
sensor input on ESP -Site and MAXILink
satellite controllers
Specifications
• Power supply. 5 to 24 VDC
• Current draw: 3 to 7 mA
• Output signal: K = 1.6965, offset of +0.059
• Cable: 20 feet (6 meters)
• Weight: 1.3 Lbs (0,6 Kg)
• Dimensions: 22"L x 8"W x 8"H (56 cmL x
20cmVV x 20cmH)
Model
• ANEMOMETER (Wind Speed Meter)
Rainfall Gauge
Anemometer
ANEMOMETER

RAIW*BIRDS.
Specifications
Model: RAINGAUGE
The rainfall gauge shall be a tipping bucket
type; with each tip of the tipping bucket
producing a momentary switch closure. The
rainfall gauge will be constructed of a gold
anodized aluminum collector funnel, white
baked enamel coated aluminum sensor
-- housing, stainless steel shafts, screws and
nuts, and brass shaft collars. The tipping
bucket will be injection molded plastic
providing rainfall measurements in
- increments of 0.01" (.025 cm). The rainfall
gauge shall have three mounting feet for use
- on flat surfaces as well as a side bracket for
mast mounting. The rainfall gauge shall
operate in temperatures ranging from +32° F
to +125'F (0° C to +52'Q. 60 feet (18
_ meters) of 2 -conductor cable shall be
included. This rainfall sensor shall be Rain
Bird Model RAINGAUGE.
Model: ANEMOMETER
The wind speed meter shall be a three -cup
anemometer providing wind speed
measurements from 4 — 80 miles per hour
(6,5 to 128 km/h). The wind speed meter
electronics shall be housed in a weather -tight
enclosure exceeding NEMA 4 and 6
specifications. The wind speed meter shall
include a mounting bracket and 20 feet (6
meters) of cable. This wind speed meter shall
be Rain Bird Model ANEMOMETER,
Rain Bird Corporation
Contractor Division
970 West Sierra Madre Avenue, Azusa, CA 91702
Phone: [phone] Fax.' [phone]
Rain Bird Corporation
Commercial Division
6991 East Southpoint Road, Tucson, AZ 85706
Phone: [phone] Fax., [phone]
Rain Bird International, Inc.
145 North Grand Avenue, Glendora, CA 91741
Phone: [phone] Fax: [phone]
Rain Bird Technical Service
[phone] (U.S. only)
www.rainbirdcom
[e-mail]
Rain Bird. Conserving More Than Water.
® Registered trademark of Rain Bird Corporation.
O 2002 Rain Bird Corporation 9102
D37238A

Drip Line Cut Sheets

U P-11!jA7AUF
Industry's Widest Flow Path
Self -Adjusting
Wider cross-section allows large
Diaphragm
particles through short flow path.
Continuously adjusts
to oaring water
pressures - crushing,
minimizing and
"I . . . . . . . . . . . . . . . . . .
flushing debris.
Large Filter Inlets,
Secondary Filtration
Reduces clogging and
maintains the essential
supply of water to the
dripper for constant
delivery of water flow.
Pressure
Compensating
Rath and Outlet
Delivers precise water
applications anywhere
in the field.
Increased Flow Path Velocity
Commonly used turbulent clappers have overlopping tooth patterns,
easily catching debris,
Turbonet Technology improves dripper performance by widening
the tooth pattern, maximizing flow path velocity, allowing
contaminants to pass easily through the dripper, virtually eliminating
plugging.
Product Advantages
• Wide pressure range (7 to 60 psi) produce uniform dripper flow roles - longer runs and steep
topographies are irrigated with high uniformity.
• Mechanical barrier prevents root intrusion - ideal for sub -surface irrigation (SDI).
• Lowest coefficient of manufacturing variability (Cv) in the industry.
• Seamless, one-piece construction prevents damage to drippers during installation and retrieval,
• Design flexibility and performance with various dripper flows and spacings allow for specific
application rates and controlling of wetting pattern in different soil types.
• Pressure compensating feature delivers precise water applications anywhere in the field,
Applications
• For sub -surface or surface applications.
• For tree, vine, row crops, greenhouse and
nursery.
• Multi -seasonal use.
• For undulating fields.
SpecMcations
Nominal How rates (GPH): 32, .42, 53,
.62-92
Common spacings: 24", 30", 36", 42.255", 48"
Recommended filtration: 1.20 mesh
Inside diameter: .540 - 16rnm (45 mil)
.570 - I'mm (45 mil)
.620 - 18mm (45 mil)
.690 - 20nun (48 n1il)
.820 - (35, 45 mil)
VineLline
C, Vineyard Solutions
Pre -Installed Adjustable Nipperline Ring
See back for details.

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4
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RAM Plow Rate vs, Pressure
a 10 20 30 ya 50 60
Pressure 6140
VineLine Vineyard Solutions
Pte -installed Adjustable Qripperline Ring
• Easily adjustable — moves from one end of the dripperline to the other preventing water migration
• Economical- saves labor costs
* Flexible options �- available with Ram or Triton Heavywall Dripperlines
* Available for 540, 620 and 690 sizes.
* Pre-installed at Netafim USA
Netafim USA - Delivering Total Growing Solutions
o Dripperlines -Filters e Valves s Air Vents -Sprinklers -Automation a Flow Meters
For Agriculture, Greenhouse & Nursery and Landscape
. r., w
Description ofRam's
Advanced re
Compensating Operation ............
Ram's self-cleaning pressure compensating
dripper is a fully self-contained unit welded
to the interior will of the dripper tubing,
Both tubing and dripper are manufactured
from high quality synthetic elastomers to
withstand chemicals and. fertilizers. The Ram
dripper contains a diaphragm that
continuously adjusts to varying water
pressure to ensure a constant flow rite. The
diaphragm allows particles to pass through
the dripper, promoting reliable performance
and a longer system life.
This continuous flushing feature and wide
flow path beep drippers flowing at optimal
rates without clogging or interrupting
operation.
Particles that may
p�
b " accumulate at the
dripper outlet can
cause a reduction of
flow.
Pressure above and
below the diaphragm
equalizes.
As the balance of
pressure is achieved,
i the diaphragm is
allowed to float freely,
r crushing, minimizing
and flushing out any
particles.
Dripper resumes "
normal operation.
f j Y
PRECISION IRRIGATION' -
For more information cat/ your Authorized
Netafim, USA Dealer or call Netafim USA
Customer Service at [phone],
AUT
tDrlpper Length
Deptlt, .Width'
Tuhingl,D.' Mil' .
Reel length
Weight
t �
r t r,a
k
Ila
rst'
VineLine Vineyard Solutions
Pte -installed Adjustable Qripperline Ring
• Easily adjustable — moves from one end of the dripperline to the other preventing water migration
• Economical- saves labor costs
* Flexible options �- available with Ram or Triton Heavywall Dripperlines
* Available for 540, 620 and 690 sizes.
* Pre-installed at Netafim USA
Netafim USA - Delivering Total Growing Solutions
o Dripperlines -Filters e Valves s Air Vents -Sprinklers -Automation a Flow Meters
For Agriculture, Greenhouse & Nursery and Landscape
. r., w
Description ofRam's
Advanced re
Compensating Operation ............
Ram's self-cleaning pressure compensating
dripper is a fully self-contained unit welded
to the interior will of the dripper tubing,
Both tubing and dripper are manufactured
from high quality synthetic elastomers to
withstand chemicals and. fertilizers. The Ram
dripper contains a diaphragm that
continuously adjusts to varying water
pressure to ensure a constant flow rite. The
diaphragm allows particles to pass through
the dripper, promoting reliable performance
and a longer system life.
This continuous flushing feature and wide
flow path beep drippers flowing at optimal
rates without clogging or interrupting
operation.
Particles that may
p�
b " accumulate at the
dripper outlet can
cause a reduction of
flow.
Pressure above and
below the diaphragm
equalizes.
As the balance of
pressure is achieved,
i the diaphragm is
allowed to float freely,
r crushing, minimizing
and flushing out any
particles.
Dripper resumes "
normal operation.
f j Y
PRECISION IRRIGATION' -
For more information cat/ your Authorized
Netafim, USA Dealer or call Netafim USA
Customer Service at [phone],
AUT