NC0090174_Report_20221011

EAA Preparer's Name: Travis H. Brown
Mailing Address: [e-mail]
Phone Number: 919-800-9252
RECEIVED
OCT 1 12022
NDDEQ/DWW/NPDES

WATER
TREATMENT
A Division of Galene
CCS - 150I
RECEIVED
oct 1 1 2022
Project Submittal NCDEUDWRINPDES
Eagle Engineering
For
Carolina Development Services LLC— Cody Glass CCS WTP
Questions relative to this proposal should be directed to: Abel Castineyra
Tel: [phone]
E: [e-mail]

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Contents
I. INTRODUCTION 2
II. DESIGN PARAMETERS 4
III. LAYOUT 5
IV. CALCULATION 1
1. PRE-TREATMENT 1
COARSE SCREEN 1
EQUALIZATION TANK 1
2. BIOLOGICAL TREATMENT 2
CLARIFIER 7
CLEAR WATER TANK 9
AEROBIC DIGESTER 9
3. TERTIARY TREATMENT 10
FILTRATION SYSTEM 10
DISINFECTION 12
DISINFECTION SYSTEM 13
UV SYSTEM 13
V. EQUIPMENTS 14
PRE-TREATMENT/SLUDGE TANK 14
SECONDARY TREATMENT 16
TERTIARY TREATMENT 19
APPENDIX 1-SUBMITTAL DRAWINGS 23
APPENDIX 2-CUT SHEETS 23
1

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
I. INTRODUCTION
The following document is a description of the packaged wastewater treatment plant
to be supplied by G Water for the 31 5-unit,Carolina Development Services LLC -Cody
Glass private residential development, located in the city of Monroe,North Carolina.The
treated effluent will be directed to the nearby Richardson Creek, which ultimately flows
into nearby Lake Lee.
The designed CCS unit is a biological treatment system that uses the Modified
Ludzack- Ettinger(MLE)process in the extended aeration mode with IFAS integration to
treat up to 152K GPD ADF of residential sewage. The system is a manufactured biological
treatment facility in a packaged plant delivery modal. Factory ready packaged plants,
operating in the extended aeration mode, are preferred over alternative designs for their
ease of installation, best in class odor control, operational efficiency, small footprint and
can be easily landscaped.
The extended aeration, activated sludge process has been employed extensively
throughout US and the world in its conventional form and in its modified form, such as
integrating fixed film (IFAS), to reliably meet secondary effluent treatment limits for
surface discharge.
The main sequence of operations includes: Equalization -Anoxic Zone—Aeration
Zones and Post anoxic cycles—Clarification—Tertiary filtration-UV disinfection-Sludge
Retention and Concentration.
The raw wastewater will be pumped from the equalization tank to a splitter box where
the flow to be discharged into the anoxic tanks will be controlled by means of V weirs. The
excess flow will be returned to the equalization tank.
The water level in the equalization tank will be controlled by four float switches,configured
for Stop pump level (low water level), Start pump level (continuous work) and High level
(start second pump) and High critical level (alarm).
The anoxic zone is designed to starve the biology and denitrify the sewage(biological
denitrification). In this tank the influent wastewater, and nitrate-rich mixed liquor pumped
from the effluent end of the aeration tanks are mixed. The influent wastewater serves as the
carbon source for bacteria,and the anoxic recycle pumps provide nitrate as an oxygen source.
2

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
The aeration reactors use IFAS technology. IFAS combines the treatment benefits
of activated sludge with the inherent stability and ease of operation of attached growth film
systems, increasing capacity and/or level of treatment. An increase in system stability is
also realized due to the significantly higher concentration of attached biology within IFAS
modules that can absorb variations or minor shocks in influent parameters.
The aeration reactors with Wavtex modules will be operated with a cycling
oxic/anoxic environment by alternating the aeration of each module. This creates transient
anoxic zones within the aerated tank for further denitrification.
A Dissolved Oxygen (DO) sensor will sense the oxygen level in the aeration tanks
and control the blower motor operation by means of VFD's.
An ORP sensor device will be inserted into anoxic tanks to measure electrical
charges (expressed as millivolts) to control anoxic conditions, assuring an efficient
denitrification process. Based on ORP sensor sign the flow for the MLSS recirculation
pump will be adjusted by means of a VFD controlled from the PLC.
Phosphate removal will be achieved by chemical means and precipitation. Alum
sulphate will be injected prior to the clarifier and will be used as coagulant.Phosphates will
be precipitated in clarifier. The chemical injection will be activated based on equalization
pumps operation.
Following the aeration basin, the mixed liquor enters the clarification zone where
biological solids agglomerate and develop floc size particles with excellent settling
characteristics. This floc mass then settles by gravity in the clarifiers and is further
concentrated in the hopper sections. Clean and fully treated water overflows from the
clarification zone is directed to a clear water tank.To assure minimal laminar velocity,and
prevent floating material to pass, a weir and baffle is included in the clarifier.
Water from the clear water tank will be pumped to the AMF Zeo filters for further
tertiary polishing and through a UV system for disinfection. The water will be with an
approximate 20 PSI residual pressure for further disposal.
The multimedia filters, in zeolite form,will enhance the particle removal efficiency
resulting in higher final water quality.
3

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
ADVANTAGES—CCS SYSTEM
✓ US and local Rep office for quick deployment of accredited service personnel.
✓ Completely retrievable equipment, eliminating the need for draining tanks for service.
✓ Low energy consumption due to the high efficiency obtained by retractable
course fine bubble diffusers.
✓ Factory assembled equipment,tested prior to deployment to site.
✓ Lowest interconnecting tie-points in peer group. Rapid deployment requiring only a
slab and utility connection and minor inter tankage connections.
✓ Stable wastewater treatment with extended air and increased surge tank withstanding
hydraulic shocks.
✓ High flexibility for operation.
✓ Fast stabilization under extreme conditions.
✓ Highly adaptable system, with flexible configurations that includes
Denitrification and Phosphorus reduction (if required).
✓ Low excess sludge production
II. DESIGN PARAMETERS
The following is the design parameters used for the Cody Glass Waste Water
Treatment Plant design base.
Table 1. Flow characterization
Average Daily Flow gpd 152,000
Maximum Day factor 2.0
Home units 315
Design population habitant 1,260
Peak Hour Factor* 3.73
18+ 1.26
*Peak Hour Factor= 4+ 1.26 3.73
4

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
Table 2. Wastewater characterization (Influent and effluent concentrations)
pH S.U. 6-9 6-9
BOD5 mg/L 250 <20
TSS mg/L 200 max < 10
TN mg/L 40 max <5
TP mg/L 20 < 1
Note:
1. All design parameters are based on min water temperature of 10°C.
2. Design assumes no inhibiting substances in water that will alter biological growth
with only domestic sewage water characteristics considered.
III. LAYOUT
The layout includes two upfront surge/equalization(EQ)tanks with integral sludge
holding compartments followed by four parallel trains with a capacity of '/ of 152,000
GPD or 38K GPD/train.
Each single train includes an anoxic chamber (AN), an aeration zone (AE), two
hopper clarification zone (CLF)and final clear water tank.
After each parallel package plant scope, we have included our AMF-ZEO-200, a
duplex multi-media sand filter skid, in Zeolite form, to serve each dual train for tertiary
treatment required when achieving high suspended solids reduction.
The layout as proposed,will allow isolation or ramp up in approximately 38K GPD
increments of in- service vs out of service trains or a phase in approach to meet the
development's treatment needs.
Tanks will be installed above ground and is based on a steel structure. All G Water
supplied Units will require a slab not included in this scope. Any soil, civil or site
preparation work, if required,will be by others.
Note: See Appendix 1 for complete submittal drawings.
5

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
6

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
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1

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
IV. CALCULATION
1. PRE-TREATMENT
COARSE SCREEN
The CCS system includes an automated bar screen to assure no big solids are introduced
into the equalization (surge)tank. The bar screen is built into a channel located above the
tank, making the clean out very simple, reducing maintenance complexity.
Bar span: 5mm.
EQUALIZATION TANK
The equalization tank will have a hydraulic retention time of 8 hours for Average Daily
Flow.
Design Flow for each Equalization tank= 1/2 of 152,000 GPD
Q (Hourly Flow for Average daily flow) 3,167 GPH
HRT(at ADF) 8 hours
Volume (V)= Q (m3/hour) * HRT(hour)
Volume Equalization tank 25,336 gal
Dimensions
Maximum Water Level 120 in
Width 144 in
Length 340 in
Equalizer mixing:
Specific Airflow rate for mixing: 0.20 SCFM/ft2, (EDI design summary)
Bottom Area= 340.0 ft2
Airflow rate= 0.20 SCFM/ft2
Required airflow 68 SCFM
It will be aerated and mixed by means of three complete ballast based coarse bubble air

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
diffuser systems, completely retrievable for ease of maintenance and replacement.
Equalizer pumping rate:
The equalized flow will be pumped to the anoxic zone using a duplex (lead/lag) set of
submersible non-clog pumps installed within the EQ chamber.
The flow is pumped to a splitter box that ensures the ADF into the anoxic basins and the
excess is returned to the EQ chamber. This will reduce any peek flow events, and will
increase system stability.
The two upfront EQ tanks are tied on the top for overflow protection,as well as on the bottom
to assure equal flows run into each tank. Sectioning each EQ tank will be done by valves on
the tank connecting points as well as in the discharge point followed by the bar screen. To
separate pipes, controlled by valves will direct the flows into either tank depending on
operator requirement
Submersible pumps
Semi open-single vane impellers.
Flow= 52.8GPM
TDH= 14.80 feet
Each pump will have a PVC ball valve and a check valve.
2. BIOLOGICAL TREATMENT
ANOXIC TANK
An anoxic chamber located before the Aeration tank, will be provided for denitrification. In
this chamber influent wastewater, return sludge from the clarifier and nitrate rich mixed
liquor from the aeration tank are mixed together by means of a mixer. Further denitrification

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
will be achieved in the aerobic tank having on-off aeration cycles in the Wavtex modules.
Denitrification in Anoxic Tank
1. Active biomass concentration (based on heterotrofic biomass, AB volume and Oc )
Xb _r 919.21 mg/I
2. Internal recycle Irratio using the Nox and desired effluent NO3-N concentration
IR = Nox/Ne - 1 - R
Ne = 7 mg/I (7mg/I in order to meet a standard of 15mgTN/L)
IR = 2.9
3. Amount of nitrate fed to anoxic tank
Flow = IR Q + R Q
Flow = 567.8 m3/d
104.2 GPM
NOx fed = Flow x Ne
NOx fed = 3.97 kg/d
4. Anoxic Volume and configuration
HRT= 3 h Define HRT
Vanox = 17.98 m3
4749.48 gal
Single stage
5. F/Mb calculation based on 1.
F/Mb = 2.18g/gd
SDNR = 0.29 Using Curves for SDNRb
SDNRt = 0.26 Correction for T and IR
6. Amount of nitrate removed in the anoxic basin
Nor =Vanox * SDNR* MLVSS
Nor = 4.26 kg/d vs 4.0 kg/d to be reduced

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Volume Anoxic tank 4,750 gal
Dimensions
Maximum Water Level 120 in
Width 144 in
Length 64 in
Mixing for the anoxic zone
The mixing system will be designed based on the thrust value. The performance of a
submersible mixer is measured by the total amount of the installed thrust(N/Newtons)
produced, position and orientation of the mixer.
Wet area=347ft2+64 ft2 =411 ft2 =38.20m2
Thrust=3 N/m2 * 38.2m2 Thrust=115 N
AEROBIC TANK (Entex Technology Design Memo)
An Integrated Fixed-film Activated Sludge (IFAS) WavTex system, it provides several key
advantages. The microbiology present on the media allows for increased treatment capacity
with a reduced footprint and shorter HRT. In addition, the inherently long SRT of the fixed
biology on the EnTextile media sheets translates to less sludge being produced compared to
activated sludge only.
The WavTex design for Cody Glass was based on the empirical removal rates of BOD,
ammonia, and nitrate.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
BOD Removal
Influent BOD=250 mg/L, or 78.2 ppd per train
40%of the treatment occurs in the mixed liquor, based on the MLSS concentration of 2,500
mg/L. Therefore, 60%of the treatment will occur on the WavTex modules.
78.2 ppd * 60%=46.91 ppd BOD removal required via WavTex per train.
BOD Removal Rate at 10°C=0.1175 ppd/ft2 of EnTextile media(gross)46.91 ppd/0.1175
ppd/ft2= 399.3 ft2
One WavTex module at 10' SWD=4,551 ft2
399.3 ft2 /4,554 ft2 =0.09 modules per train
NH3 Removal
Influent NH3 =40 mg/L, or 12.5 ppd per train
40%of the treatment occurs in the mixed liquor,based on the MLSS concentration of 2,500
mg/L. Therefore, 60%of the treatment will occur on the WavTex modules.
12.5 ppd * 60%= 7.51 ppd NH3 removal required via WavTex per train.
NH3 Removal Rate at 10 °C =0.0052 ppd/ft2 of EnTextile media(gross) 7.51 ppd/0.0052
ppd/ft2= 1,443 ft2
One WavTex module at 10' SWD=4,551 ft2 1,443 ft2/4,554 ft2 = 0.32 modules per train
required

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
NO3 Removal
Influent NO3=40 mg/L,or 12.5 ppd per train(assume all NH3 is converted to NO3)Assume
that the pre-anoxic tank will reduce the NO3 to 15 mg/L or 4.69 ppd NO3 as presented above.
NH3 Removal Rate at 10 °C = 0.0052 ppd/ft2 of EnTextile media (gross). Note that the
denitrification rate equals that of the nitrification rate in the cyclic aeration approach. This is
because nitrification is the rate limiting step.
4.69 ppd/0.0052 ppd/ft2=902 ft2
One WavTex module at 10' SWD = 4,551 ft2 902 ft2 / 4,554 ft2 = 0.20 modules per train
required
It was concluded that one (1) aerated WavTex module per train would provide sufficient
microbiology necessary for treatment of both BOD and ammonia. One (1) additional
WavTex module per train can be added in order to meet TN limit of< 5 mg/L. Though the
calculations yielded less than one module for both aerated treatment and denitrification, a
quantity of two (2) per train or eight (8) total was chosen for conservatism. This allows for
process flexibility within the MLSS concentration. Additionally,by having two (2)modules
per train, this ensures that one module will be in aerobic operation while the second is in
anoxic operation at all times. This is essential for creating the transient aerobic and anoxic
zones required to consistently meet the TN limit.
Aeration Requirements
Each WavTex module will have an integrated coarse bubble aeration grid that will run at
approximately 122scfm per train which is sufficient for scouring of the unit, mixing, and
biotreatment.
Hydraulic Retention Time
IFAS systems for municipal waste which adhere to these standard loading values can achieve
full nitrification with HRTs of 8 hours at temperatures above 10 deg C.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Volume Aerobic tank 12,667 gal
Dimensions
Maximum Water Level 120 in
Width 144 in
Length* 191 in
Additional length is considered for recirculation pump installation.
CLARIFIER
A 2- hopper type clarifier each with a Q ADF capacity is included for each train. All pumps
in the clarifier will be based on Air Lift pumps and will include the RAS, the WAS and a
skimmer. Flow into the clarifiers are through a and baffle structure, reducing velocity and
assuring the minimal turbulence in the tank, for best settling conditions.
Design of the clarifier is based on following max design parameters:
Weir overflow rate <5000 GPD per lineal foot for ADF
<20,000 GPD per lineal foot at PHF
Surface Loading rate(SLR) <900 GPD/SF based on influent, at PHF and considering
Activated Sludge with chemical addition to Mixed Liquor for
Phosphorus removal.
Solids Loading rate 35 ppd/SF at peak solids loading rate, calculated based on the
design maximum day flow rate plus the design maximum
return sludge rate requirement and the design MLSS under
aeration.
HRT Above 3 hours

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Clarifier
Dimensions
Maximum Water Level 120 in
Width 144 in
Length 215 in
Area 215 sf
Calculated Surface Loading Rate per train (each train '/4 ADF = 38,000GPD)
PHF=ADF * Peak Factor
From Table 1, Peak Factor= 3.73
PHF= 38,000 gpd * 3.73 = 141,740 GPD
SLR=
215sf 141,74ocPn_660 gpd/sf < 900 gpd/sf(at PHF)
Solids Loading Capacity
MDF =2 * ADF
MDF=76,000 GPD (287.6m3/d)per train
IRt= IR ras + IR anox=3.9
Clarifier area=215sf(20m2)
287.677/3/d*2soomg*(1+3.9)
Solids load= 20m2*(1000) 176.15Kg-d/m2= 35.9 lb-d/sf
Hydraulic Retention Time (HRT)
Sludge hopper angle 060
H pyramid truncada 1/3 in 27.6
Major area in2 14,770
Minor area in2 144
1/3 Hopper volume gal 652.1
Cube volume gal 2,499.6

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Total volume per hopper gal 3.15 I.6
#hoppers ea 2.0
Total clarifier volume gal 6,303.2
Total clarifier Volume(gal) 6,303.20
HRT = = 3.98hours
Q( gal 1,583.3
hour)
CLEAR WATER TANK
One clear water tank will be provided for each train, each one with 15 minutes of Hydraulic
retention time for PHF (1.1 hrs for ADF). The clear water tanks will supply the filtration
system the required flow for final polishing prior to discharge.
Clear water tank 1,800 gal
Dimensions
Maximum Water Level 108 in
Width 144 in
Length 27 in
AEROBIC DIGESTER
Excess sludge from the clarifiers will be stabilized in an aerobic digester, aerated and mixed
by means of fine bubble diffusers. Stabilized sludge can be further dried to reduce volume
or otherwise disposed at an estimated 1.5% - 2% solid concentration, responsibility of the
client.
Px,tss=46.2 Kg
Sludge mass * (Kg)
Sludge tank Voume = Concentration % * days
46.2 Kg
Sludge tank Voume = * 20days =52.00m3 = 13,738ga1
2.0 ago

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Sludge tank 15,000 gal
Dimensions
Maximum Water Level 120 in
Width 144 in
Length 200 in
Sludge tank aeration/mixing:
Specific Airflow rate for mixing: 0.45 SCFM/ft2, (EDI design summary)
Bottom Area= 200.0 ft2
Airflow rate= 0.45 SCFM/ft2
Required airflow 90 SCFM
It will be aerated and mixed by means of three complete ballast based fine bubble air diffuser
systems, completely retrievable for ease of maintenance and replacement.
3. TERTIARY TREATMENT
FILTRATION SYSTEM
Two multimedia pressure filtration system one in operation and one in standby (Lead/Lag)
for redundancy purposes will be provided. Each having the capacity to filter the complete
flow of the plant.
During ADF operation one pump will send the water from the clean water tank to the
filtration system. The pumps will be controlled by three float switches, configures for Stop
pump level (low water level), Start pump level (continuous work) and High level (start
second pump).
The water flows into the top of the filter in a down-flow configuration. During this process,
the media removes the particles and impurities based on its design criteria.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
The filter includes two operating modes, a filtration mode and a cleaning (backwash)mode.
In filtration mode,the filtration media gradually accumulates impurities present in the water,
forming a layer of impurities. The accumulated impurities create a flow obstruction forming
a pressure differential between the inlet and the outlet.
In order to eliminate the obstruction and compensate the pressure differential, the filtration
system includes a backwash mode, achieving a complete filtration media wash. During the
process, an even lift up of the media is created by introducing clean water in a up-flow
process, discharging the dirty water through the drain (backwash line).
The backwash mode is activated automatically, when the inlet pressure and outlet pressure
switches sense a pressure differential of 7-10 psi (can be configured), or manually by the
operator. During backwash, clean water will be used from the second clean filter, assuring
clean water is used, and no additional pumps required.
Effluent from backwashing will be sent to the equalization tanks,
The schematic below shows the filter in operation and backwash mode. The G Water AMF
series filter vessel provides the industry's leading uniform distribution created by the unique
pattern of nozzle placement and disbursal on a specially designed lower plate configuration.
In the backwash mode,this pattern creates an even up flow of the media,reducing the particle
entrapment.
The pressure filter vessels will be designed with double flooring to assure high filtration
efficiency, reduction on backwash time, and reduction of"preferred channeling" effect on
the media.

Eagic Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Zeolite Design Parameters:
Filtration Rate (ADF) 12-20 GPM/SF for Zeolite
Backwash Rate 15-20 GPM/SF for Zeolite (30%bed expansion)
Media Gravel/Zeolite
Pressure loss 5-7 PSI
PHF = 196.9GPM
Each AMF-ZEO-200 includes:
Two 48"- diameter tanks (one for redundancy)
Area per tank= 12.56sf
Media: Gravel /Zeolite
Feed pumps= 100GPM @ 30PSI (One pump in operation and second in standby for PHF or
backwash requirement)
Calculation for PHF
Backwash
MODEL Flow Tank diameter Area rate* Backwash
PHF Tanks Qty Filtration rate flow
GPM (pig) (m) (m2) (sf) # gpm1tt2 gpm/ft2 (gpm)
AMF-Z-200 196.94 48 1.219 1.167 12.57 1 15.68 16.38 205
*for 30%bed expansion
FILTERING PROCESS BACKFLUSHING PROCESS
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DISINFECTION

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
DISINFECTION SYSTEM
UV SYSTEM
Two Ultraviolet systems are provided using 4 lamps/each for single pass disinfection of the
treated wastewater prior to discharging from the plant. Each dual train will be disinfected
using UV 254nm, installed after the MMF-Zeolite step.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
V. EQUIPMENTS
PRE-TREATMENT/SLUDGE TANK
1. Bar Screen-Automatic:
Model Tsurumi KW 5038 Flow up to 113m3/hr
Bar span: 5mm.
Slope 60°
Material: 304 Stainless Steel
Motor 0.09kW
Quantity: 1 unit.
2. Submersible Pumps in Equalization tank:
Submersible pumps shall be supplied for feeding the water to the splitter box.
Semi-open, single vane impeller. Solids handling 0.79"/20mm
Each pump shall be able to handle 100GPM @ 30PSI
Model Tsurumi TOS 50B2.75HS
Suction/Discharge: 2", flanged
Motor 1 HP/ 115 V/l ph
Casing, motor frame in Cast Iron, shaft stainless steel, on guide rail system for ease of
maintenance and replacement.
Each pump will have a PVC ball valve and a check valve.
Quantity: 4 units, 2 in operation and 2 in standby.
3. Level control:
Float switch, mechanically activated, wide angle.
Model SJE Pump Master WPS.
Electric: 120/230V
Quantity: 8 units (4 per tank)

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
4. Blowers for Equalization and Sludge tanks:
Model Gardner&Denver/ IQ Positive displacement model IQ4LDSL
Blower Capacity required 160SCFM @ 6PSI each one (part of the air will be used for the
sludge stabilization tank)
Motor 7.5HP/240V/60Hz/3ph
Includes inlet an outlet filter, check valve, pressure relief valve, ball valve and pressure
gauge connected to a stainless steel pipe.
Each Equalization+Sludge tank requires one Blower
Quantity: 2 units
5. Air diffusers:
Sludge tank
Model EDI 88S, Retrieval units. Fine bubble flexible membrane diffuser,
F1exAirTM MagnumTM high oxygen transfer efficiency.
Hose feeder airline, SS hose clamps, and concrete ballast.
Quantity: 6 units (3 per tank)
Equalization tank
Model EDI Max Air duplex, Retrieval units. Coarse bubble PVC diffuser,
Hose feeder airline, SS hose clamps, and concrete ballast.
Quantity: 6 units(3 per tank)
Air valves: each diffuser will have a ball valve for isolation.
Material: Stainless steel 304
Model 20SSTH Matco Norca
6. Sludge evacuation:
Includes a stand pipe with a quick coupling(Banjo) connection, 3" in diameter.
7. Airlift Decanter:
Model Airlift type, SCH80 pipe,2",with air hose pipe, and throttling ball valve.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe,NC
SECONDARY TREATMENT
1. Mixer for anoxic tank:
Submersible mixer type ABS XRW
Model 2121 60Hz Motor 2.4HP
Propeller diameter 210mm
Speed 1735 1/min
Thrust ISO 21630 255N
Installation Wall mounted on adjustable bracket
Quantity: 4 units (1 per train)
2. Blowers:
Model Gardner&Denver/IQ Positive displacement model IQ4LDSL.
Blower Capacity required 160SCFM @ 6PSI each one
Motor 7.5HP/240V/60Hz/3ph with VFD
Includes inlet an outlet filter, check valve,pressure relief valve, ball valve and pressure
gauge connected to a stainless steel 304 pipe.
Each Aeration basin ('/a of ADF)requires one Blower
Standby units installed will also serve as a Standby option for the EQ/SHT
Ouantity: 6 (1 per train and 2 in standby)
3. Wavtex Modules:
Textiles media for Integrated Fixed Film Activated Sludge IFAS system is produced from a
woven, three- dimensional fabric, has a specific surface area of 4,551ft2 approximately.
Dimensions 10feet long by 6 feet wide, by 9.5 feet tall.
Quantity: 8 units (2 per train)
4. Air diffusers:
(1 per Wavtex module) Coarse bubble aeration grid that run at 122scfm for scouring of the
unit,mixing and biotreatment.
Material: PVC
Ball valve per grid, diameter 3"Material: Stainless steel 304 Model 20SSTH Matco Norca

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
5. Sensors DO and ORP:
FDO, luminescence optical DO sensor, for continuous monitoring.
Model YSI IQFDO700 with sensor cap factory calibrated (or similar)
Measurement range: Oxygen concentration 0 to 20mg/1
Parameters measured: Dissolved oxygen and Temperature
Power consumption: 0.7 watts
Sensor Material: Housing-VA steel 1.4571; Sensor Cap and Locking Cap— POM
(Polyoxmethylene),, PVS, silicone, PMMA
Yoxmeth l Yene
Rating: IP-68; waterproof
Quantity: 4 units
ORP sensor
Model YSI IQSensoLyt(or similar)
Probe w/amplifier for stationary measurement for anoxic chamber to control anoxic
conditions.
Power Consumption: 0.2W
Housing: V4A Stainless Steel 1.4571 (SW version POM(Polyoxmethylene)),
protection cap PVC
Quantity: 4 units
6. RAS and WAS:
Model Airlift type,SCH80 pipe,2",with air hose pipe,solenoid and ball valve to be operated
automatically or manually. Automatic recirculation programmed in the control panel.
Quantity: 8 units (1 per clarifier)
7. Skimmer:
Model Airlift type,SCH80 pipe,2",with air hose pipe,solenoid and ball valve to be operated
automatically or manually. Automatic recirculation programmed in the control panel.
Quantity: 8 units (1 per clarifier)

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
8. Mixed liquor recirculation pump:
Submersible pumps shall be supplied for MLSS recirculation from Aeration basin to Anoxic
tank.
Semi-open, single vane impeller. Solids handling 0.79"/20mm
Each pump shall be able to handle up to 105GPM @ 14PSI
Model Tsurumi TOS 801321.5; Motor 2.0HP/240V/3ph with VFD
Suction/Discharge: 3", flanged
Casing, motor frame in Cast lion, shaft stainless steel, on guide rail system for ease of
maintenance and replacement.
The pump will have a PVC ball valve and true union check valve.
Quantity: 4 units(1 per train)
9. Dosing pump for coagulant:
Electronic Metering Pumps
Model PULSAtron Series A Plus LBC4 (or similar)
Capacity 7.6LPH Max pressure 50PSI
Piping '/a"FNPT
SPM 125
Power 115VAC/60Hz/lph 0.6Amps
Quantity: 4 units
Each pump includes chemical tank for coagulant preparation
10. Control Panel:
The control panel is equipped with a PLC and consists of an interface through the HMI screen
for visualizations and configurations of the equipment.
Factory build, Unitronics PLC prewired and programmed.
One main control panel (MCP)
Enclosure:NEMA 4 weatherproof
Electrical hardware inside MCP: I/O cards, CPU, back up battery, magnetic starters, relays,
VFD's, and protections.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
The HMI interface consists of access screens for:
Surge tank pumps
Blowers with VFD and DO sensor
Airlift WAS.
Airlift RAS.
MLSS Recirculation pump with VFD
Dosing pump
Filtration pumps.
Filter backwash.
Skimmer.
UV System
TERTIARY TREATMENT
1. Filtration vessels
Material of Construction:
All filters installed in the filtration systems are manufactured from robust carbon steel
ASTM-A570-GR36. They ensure long lasting system operating life.
Protective Coating:
The coating process provides products with maximum anti-corrosion protection.
For filters up to 60" (included)the coating process is performed in seven stages, as follows:
1st stage: Automated shot blast cleaning of products to a level of SA 2.5 as per
international standard ISO 8501.
2nd stage: Phosphatization.
3rd stage: Rinsing.
4th stage: Sealing.
5th stage: Drying.
6th stage: Epoxy phenolic 120 micron.
7th stage: Oven curing.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
This process creates a perfectly coated product with a protective layer of 120 micron.
Vessels internal distribution:
The filter vessels use a unique design of a double chamber, divided by a welded reinforced
steel plate. The upper chamber contains the media;the lower chamber is empty and collects
the filtered water. The plate is covered by"mushroom"type diffusers which are PP, slotted
conical units. They disperse the water uniformly, using the whole media volume effectively,
avoiding the occurrence of channeling or caking when operated correctly.
Size: 48"diameter
Quantity: 4 units(2 in standby)
2. Media:
The vessels are filled with garnet as support media and Zeolite as filtration media.
Zeolite physical properties:
• Color: Light tan to near white
• Dry Bulk Density: 50 lbs/cu.ft
• Specific Gravity: 2.2 g/cc
•Mesh Size: 14x30
• Effective Size: 0.55mm
• Uniformity Coefficient: 1.8
•Hardness: 4-5 (Mohs Scale)
Design criteria:
• Bed Depth: 24-36 inches
•Freeboard: 50%of bed depth
•Backwash Flow Rate: 15-20 gpm/sq.ft.
•Backwash Bed Expansion: 30-40%of bed depth
• Service Flow Rate: 12-20 gpm/sq.ft.
• A gravel support bed is required
3. Feed Pump:

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Two pumps per filtration skid will be supplied for feeding the water to the vessels.
Each pump shall be able to handle 100GPM @ 30PSI; Motor 5HP.
Suction/Discharge: 2", flanged
The pump shall be centrifugal type, Webtrol, Model FC (or similar).
Casing, Impeller Shaft Stainless Steel
Quantity: 4 units (2 per filtration skid)
4. Control Valves:
Solenoid controlled valve, opens and closes drip-tight in response to an electrical signal.
Material: Body, cover and plug Polyamid 6 & 30%GF
Diaphragm:NBR
Seals: NBR
Spring: Stainless Steel
Cover bolts: Stainless Steel
Tubing and fittings: Plastic
Solenoid voltage range: 24 VAC, 24 VDC
Quantity: 8 units (4 per filtration skid)
5. Woltman Turbine Water meter:
Magnetic drive register, Dry, IP68,NEMA 6P sealed register
"Reed switch" sensor allow one or two pulse outputs option
Body, cover: ductile iron
End Connections-Flanged: ANSI Class 150
Model: Turbo BAR-M,4"
Quantity: 1 unit.
6. Pressure Gauges:
Liquid filled pressure gauges with 4-1/2" diameter dials, and bronze bourdon tubes shall be
furnished for each vessel inlet and outlet.Each pressure gauge shall be furnished with manual
isolating valves.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
Quantity: 8 units(4 per skid)
7. UV system:
Germicidal ultraviolet lamps producing ultraviolet wavelength at 254 nm.
The water enters the stainless steel disinfection chamber and flows into the space between
the quartz sleeves and chamber wall where suspended microscopic organisms are exposed to
intense shortwave germicidal ultraviolet rays.
Translucent sight port and front panel indicator lights(not shown)provide positive indication
of germicidal lamp operation.
Manual wiper system facilitates routine cleaning of quartz sleeves without disassembly or
shutdown of disinfection systems.
Model Megatron M50
Nominal lamp length 1554mm
Power consumption 75 watts
Ultraviolet output 33 watts
Inlet/Outlet 2"NPT
Number of lamps 4
Power 120V
Dimensions 105 7/8" x 18 1/8" x 15 1/8"
Quantity: 2

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe,NC
APPENDIX 1 - SUBMITTAL DRAWINGS
APPENDIX 2 - CUT SHEETS

it WADE H.GRIFFIN
I BK.6624-665
DONNIE B 83057,
A JORDAN NOW OR FORMERLY
OB 057,PG A TAX PIN:0 924 70 124
NOW OR FORMERLY ZONED.R-20
TAX PIN:09-247-012B
ZONED:R-20
DONNIE B. BETTY AJORDAN
D:1291,PG 122
\ N. IN FORMERLY
SZONED:R-20
WWlP
LMLL1AM ANDREW 6 1
MILDRED MCNEISHI� :'
PLAT6,PG80 Es] EE
LOT P'
NOW OR FORMERLY
T. , y
ZONED:R-20
` I Deacnpson I September bet,2022
Scale Pmwu N.LAZO me Galene CCS-150 wIIFAS
Electrical P.QUEZADA Eagle EngineeringforCarolina Development Drawing V.GONZALEZ 9Cody 100 pment Services LLC
Glass Residential Development-VW I?
WWTPLOCATION WATER Drevenp 0000E „Av.., Sheet No Sheet rS REV.NO.
xu /'�� �
F 1'75D TREATMENTFOR 01 Al 1 L,?
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manweea...eeao.mn.reb,erener7rr.r..tie.e..e•a.,.....ra,eea
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Description I September 2nd,2022
Scale Process N.LAZO Title Galene CCS-150 w/IFAS
Electrical P.GUEZADA
PLAN VIEW Drawing V.GONZALEZ Eagle Engineering for Carolina Development Services LLC
SCALE 2.II Cody Glass Residential Development-VYWTP
P�'�• WATER Dravnng GENERAL LAYOUT Sheet No Vast See REV.NO.
'....✓TREATMENT FOR
00005 NCE., 05 Al I j 1 I 1
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Electrical P.OUEZADA Eagle Engineering for Carolina Development Services LLC
Drawing V.GONZALEZ
A Cody Glass Residents!Development-VOW?
MODEL NOW L@MW Tie Na0GLTY< MOO[TANS 0Eum n
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Electrical P.OUEZADA Galene CCS-150 w11FAS
IIIII Dnrrg V.GONUIEZ Eagle GI ennp tor Carolina Development Semces LLC
= I MI 1t'. - Po �" I Cody Class Residential Development-NNJTP
P ttr PtP' P,P Dra GENERAL LAYOUT Sheet No Sheet Srte REV.NO.
SECTION 1 SECTION 2 a PLATE €1.f TREATMENT ����p�.�REFERENCE�`�n� ��M°' T
PLAN VIEW SCALE t:7S SCALE 1:N toeF
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Desolation 1 September 2d,2022
Scale-Process N.LAZO Title Galene CCS-150 w/IFAS
Dial V. ADA
Drawing V.GON7 GOWAI F2 Eagle Engineering for Caroline Development Services LLC
Cody pen Residential Development-NANfP
WATER Drww g GENERAL AAYGUT Sheet No Sleet Sae REV.NO.
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SCALE t:a sins t:a SCALE t:fe
OaScnption I September 2rd.2022
Scale Process N.LAZO Title ElectricalP. A Galena CCS15O w11FA S
Drawing V.CONT.Fl Eagle Eni3neenng for Carolina Development ant Services LLD
Cody Glass Residential Development-WWTP
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_ _ter tt- style ProcessN.LAZO rrtle Galene CCS-150 w/IFAS
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J 4 . .'-J N4 Dnvnng V.GOWaI F7 Eagle Engineering for Caroline Development Services LLC
Cody Glass Residential Development-1NVVIP
PLAN VIEW /'' WATER Drawap GENERAL LAYOUT Sheet No Slwra® REV.NO.
WALE I:SO l..!TREATMENT 4-0111.F.ENCE ONLY aT At t j
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Description I September and.2022
sU.l.Pr.c... N.LA20 Title Galena CCS-150 w/IFAS
E3.a". P.OUEZAOA
[Sewing V.GONZALEZ Eagle Engineering for Caroline Development Services LLC
Cody Glass Residential Development-WVJrP
(�^ WATER GlON1e0 GENERAL LAYOUT slaw No ■' REV.NO.
C J TREATMENT gam" Da At 1 1 1 1 1
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Description I September btl,2022
SECTION "A" Seel°Process N.tA20 Title Galene CCS-150wIFAS
Dewing V.GON7ADA Eagle Engineering for Caroline Development Services LLC
SCALE 1:15 Dewing V.GOWar P� Cody Glass Residential Development-MIT
WATER Dr."'"GENERAL LAYOUT Sheet No She See REV.NO.
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Piixcellent corrosion resistance Efficient Elimination of Floating Solid Matters in Sewage.
Tsurumi bar screens are pre-treatment equipment that enables smooth water treatment in post-processes.
live tied metal parts are made of
Front Screen/ Type Applications
KS/KWE KI •Primary treatment of general industrial wastewater
ure of Screen(Example of Front Screen) >•Q
Rear Screen Type
•Treatment of wastewater from food processing factories
I ' _ KM/KM A/KMS •Treatment of kitchen wastewater from hotels,factories,hospitals,etc.
When installed in a ditch,the screen ! �Y�11 f\ �7 •Combined sewage treatment tanks(Johkasou/septic tank)
catches solid matters contained in ��// �, Motor
the sewage and allows water to pass. t°* w�j I Residue •Village wastewater treatment facilities
The solid matters caught by the screen Screen f QD
Collecting •Small-scale sewage treatment facilities
is raised with rakes,and collected 7/// Basket
in the residue collecting basket. i. .j,
Rake '4- `
Y.�
/ . z._,� Application in situations
��lt"'s�: ' ' �� with water level fluctuations
�t ffi ll
•The bar screen is compact and lightweight,making it easy to install in
,,.�, fi J U-shaped ditches,etc.With sealing rubber attached to the sides of the , '
T / frame,the screen snugly fits any width of waterway. cif^•
/// '
•During operation,the rakes always move through the slits of the screen, i
;f preventing the screen from being clogged with solids matter. `y
,,r „ ,,,( "". !� / "�, •The wetted metal parts are made of 304 stainless steel,which exhibits i/ ry
excellent durability even in harsh environments e.g.,outdoorscontinuously operated day and night etc.
I Abe
Maintenance is easy.Initial and running costs are low.
I,,
•The KS-series screens are equipped with an eccentric roll mechanism3g that prevents retraction and clogging of the screen bar front edge caused
Sealin Rubber by residue. KE
. •The KW-series screens incorporate a safety device that can stop the gear
4 motor immediately in the event of abnormal operation.
�L Ali Major Parts'Materials
>;. Screen Bars 304 Stainless Steel
`� �/y Rake 304 Stainless Steel
Chan and Sprocket 304 Stainless Steel Application
^'r; ,. Frame 304 Stainless Steel' in situations ,y
•Frame motional of KS-200Z Is 430 stainless steer
without water level fluctuations S
..,.,, , , Concrete Block for Fixing the Screen •The bar screen is compact and lightweight,making it easy to install in l filt.
a
U-shaped ditches,etc.With sealing rubber attached to the sides of the
Used for combined sewage treatment tank(Johkasou/septic tank)and small-scale sewage treatment facilities,etc. frame,the screen snugly fits any width of waterway.
t ^•„c,,; ,_.. -, _ •Since the rake chain(dry chain)is not in contact with liquid,dirt and ,
' ' • 1 Tr residue will not adhere to it.Therefore,it needs almost no maintenance. •'
-
,t i 4 . 'a •'M a •The wetted metal parts are made of 304 stainless steel which exhibits
"'�c� '
•�,,,. �. c�> rf excellent durability even in harsh environments,e.g.,outdoors,
+.
" ,. .e.- ., • continuously operated day and night,etc. i.
,", z ,
_ •The bar screen can be directly installed in a U-shaped ditch to eliminate -(`\ M r`,k1d40 0 dirt from the bottom of the ditch.It provides excellent treatment effect,and KM
r ��?�F � \ . �'=-�A I vJ y�- r m is advantageous both in terms of initial cost and running costs.
iii ���ti� !!! _.. ��
-a1 %- „aa,°
JA1fY�P- - <. V TSURUMI PUMP I 02
M r4 y.

KE/K 1 W -Front Screen-
Dimensions
The KE/KS/KW-series is a front screen type automatic bar screen designed for screening wastewater.The
wetted metal parts are made of 304 stainless steel.Two or more rakes travel behind the screen bars located KE•200S KS-200Z
at the front side of the unit.Since every rake tooth moves between the screen bars,it can remove solid KE-200M Ks-zoov
matters even though they lodge between the screen bars.In addition,the use of a small output motor KE-200L Ks-300v
enables to save the electricity.The bar screen is suitable for use in a waterway with varying water levels. 0 o
♦a mot_'t ' 21
/0/4 I i- /0/
, , , ,-1 L, i i
[ *, 1 , :.
j.= CAI I121I
KE - KS KW
KS-2005 KW-4027 KW-5027 KW-6027
KS-200M KW-4038 KW-5038 KW-6038
KS-200L KW-4049 KW-5049 KW-6049
Fine Screen(Bar Spacing:1.0-5.0mm) p
Model Motor 5m 2 mm Height Width a Ir[Angki0rt Dry It
Output Capacity m'Ri Height Waterway M91e Weight
vlrillkW 1.0min 2.0mm 2.5mm 5.0mm mm mm kg ;"
KE-200S 0.1 - 26 31 41 510 300-400 60' 32 't ,>N� =_" I` 0�
KE•200M 0.1 - 36 46 58 685 300.400 60' 38 r /` - -
KE-200L 0.1 - 49 62 78 865 300.400 60• 42 / •\
KS•2002 0.1 16 26 31 41 520 330-400 60• 33 ' ��
KS-2007 0.1 29 47 56 74 760 400-500 60° 49 w �,J
KS-300Y 0.1 43 70 84 110 760 500.600 60' 54 L `
KS-200S 0.1 17 28 31 47 800 330.400 45' 47 I I
KS-200M 0.1 25 41 48 70 920 330.400 45 52 n
B Ia C
KS-200L 0.1 32 55 63 93 1050 330.400 45' 62 C L
KW-4027 0.09 17 29 34 47 659 up to 400 60' 23.5
KW-4038 0.09 27 45 52 73 842 up to 400 60' 27.8 Unit.mm
KW-4049 0.09 39 66 76 105 1057 up to 400 60' 31.8 Max. Discherygc Overall
Effective Width of Overall Width of Max. Overall Level of Space Length of
KW5027 0.09 26 45 52 73 659 400.500 60' 27.0 Model Width Frame Width Upperp Water Level Height sow, Frame
KW-6038 0.09 41 69 81 113 842 400.500 60' 32.1 A 8 C 0 E F G 1 I.
KW-5049 0.09 60 101 117 164 1057 400.500 60' 37.1 KE-2005 191 254 460 330 210 510 300 480 577
KW-6027 0.09 36 61 70 98 659 500.600 60' 30.5 KE-200M 191 254 460 330 390 685 500 580 787
KW-8038 0.09 56 95 109 153 842 500-600 60• 36.5 KE-2001 191 254 460 330 510 865 680 690 992
KW-6049 0.09 81 138 158 223 1054 500-600 60° 42.3 KS-200Z 191 254 460 350 210 520 280 490 577
KS-2007 191 254 460 350 360 760 500 640 850
Coarse Screen(Bar Spacing:20-50mm) KS-300Y 282 345 550 500 360 760 500 640 850
KS-200S 180(187) 290(297) 500 400(410) 270 800 400 800 800
Model Motor Bar Spacing mm OveralWidth of Installation Dry KS-200M 180(187) 290(297) 500 400(410) 370 920 540 920 971
Output Capacity m'Ih Height Waterway Angle Weight
kW 20mm 30mm 40mm 50mm lain mm kg KS-2001 180(187) 290(297) 500 400(410) 470 1050 650 1040 1140
KS-2005 0.1 70 75 80 85 800 KW-4027 191 276 465 410 279 659 323 544 584
330.400 45• q7
KS-200M 0.1 104 111 119 123 920 330.400 45° 52 KW-4038 191 276 465 410 395 842 506 650 795
KS-200L 0.1 137 147 157 165 1050 330.400 45' 62 KW-4049 191 276 465 410 511 1057 722 774 1044
KW-5027 291 376 565 510 279 659 323 544 584
•Powered by three-phase totally-enclosed geared motor.
•Capacity is given as the maximum amount at clean water. KW5036 291 376 565 510 395 842 506 650 795
•Consult your dealer it the screen is to be installed in a waterway of a width exceeding that listed on the table. KW-5049 291 376 565 510 511 1057 722 774 1044
•When ordering,specify the desired bar spacing together with the model name. KW-6027 391 476 665 610 279 659 323 544 584
KW-6038 391 476 665 610 395 842 506 650 795
KW-6049 391 476 665 610 511 1057 722 774 1044
•Figure in( )are far the screens at timer or coarser bar spacing.
03 1 TSURUMI PUMP TSURUMI PUMP I D4

APR.00
BE-BLP1
497 TSURUM$ PUMP R-SERIES SPECIFIC ITlONS
SEWAGEii WASTEWATER PUMPS
—
■ FEATURES
1.Semi-open, Single vane,(1 HP-5 (2Hp.and above.), and •
Hp.),impellers with field adjustable further protected by an
/replaceable shear plate and, exclusionary oil seal(s),
Enclosed Multi-vane,(71/2- provides for the most durable _
300 Hp.), impellers,with field seal design available. -
adjustable/replaceable wear r
plate provides for high wear 5. Double shielded, permanently 4
resistance and enhanced solids lubricated, high temperature +�
handling capability. C3 ball bearings rated for a l - i'
B-10 life of 60,000 hours 1
2. Highly efficient, continuous duty provide for extended 1.
air filled,copper wound motor
with class E, B, F insulation operational life.
minimizes the cost of operation.
APPL ICATIONS ,
3. Built in thermal protection
prevents motor failure due to 1. Commercial, Industrial IMPELLER
overloading,accidental run-dry sewage,wastewater,or
and single phasing in three effluent transfer. ills
phase units.
ill
2. Decorative fountains and
4. Double inside mechanical seals aquiculture. �"" ` �`
with silicon carbide faces, running rx SHEAR PLATE
in an oil filled chamber, equipped 3. Raw water supply from rivers `� (2"-4") 16-
with an oil lifter,- or lakes. " LI
1.(111.1•092 Icy
EQUIPPED
■ SPECIFICATIONS ■ STANDARD ■ OPTIONS
Discharge Size 2"-32" (50-800 mm) Dry-Pit
Horsepower Range 1 Hp.-300 Hp. (.75 kW-220 kW)
Performance Range, Capacity 25-33,000 G.P.M. (.09-125 m°/min)
Head 6.6 Ft.-278 Ft. (2-84.7m)
Maximum water temperature 104°F. (40°C.)
Materials of Construction
Casing Cast Iron,ASTM 48 Class 35 304/316 SS(BQ-Series)
Impeller Cast Iron,ASTM 48 Class 35 304/316 SS(BQ-Series)
Shaft 403,420 Stainless Steel 304/316 SS(BQ-Series)
Motor Frame Cast Iron,ASTM 48 Class 30 304/316 SS(BQ-Series)
Fasteners 304 Stainless Steel 304/316 SS(BQ-Series)
Mechanical Seal
Upper Seal Silicon Carbide/Silicon Carbide
Lower Seal Silicon Carbide/Silicon Carbide
Elastomers NBR(Nitril Buna Rubber) Viton(BQ-Series)
Impeller Type Semi-open, Enclosed, solids handling.
Solids Handling Capability up to 6"non compressible
Bearings Pre-lubricated, Double Shielded
Motor Nomenclature
Type,Speed, Hz. Air Filled, 3600, 1800,1200,900,600, Nema 3R inverter available for
514, &400 Rpm, 60 Hz. 230 V.,1 Ph.operation from 2-5
Voltage, Phase 115 or 230 1 Phase(1 Hp) Hp.
208/230 or 460 V., 3 Phase
Insulation Class E, B, F
Accessories Submersible Power Cable 32'(10 m) Length as required.
TO/TOS Slide Rail System
Operational Mode , Manual Automatic or Alternating
( (1-5 Hp.)

Oct.00 00-PC-B-01
L7 TSURUMI PUMP B - SERIES PERFORMANCE
SEWAGE&WASTEWATER PUMPS CURVE
MODEL BORE HP KW RPM SOLIDS DIA LIQUID SG. VISCOSITY TEMP.
(TOS)50B2.75HS 2"/50mm 1 0-75 3300 0.79"/20mm Water 1.0 1.81 CST 60-F
PUMP TYPE PHASE VOLTAGE AMPERAGE HZ STARTING METHOD INS.CLASS
Sewage&Wastewater Pump Single 115/230 10.8/5.7 60 Capacitor-Start E
CURVE No. DATE PHASE VOLTAGE AMPERAGE HZ STARTING METHOD INS.CLASS
EFF. TOTAL HD. REMARKS:
% M. Ft.
55
16 -
100 - 50
14 -
90 45
80 - 12 - 40
TyQI
70 - 35
10 -
60 - . 30
8 -
50 - 25
40 - 6 - 20 '
30 - 15
4
20 10
2 -
10 - 5
—0 —0 —0
US GPM 0 5 10 15 20 25 30 35 40 45 50 55 60 65 70 75 80 85 90
CAPACITY
M'/min 0.00 0.05 0.10 0.15 0.20 0.25 0.30
SHAFT POWER
KW BHP
0.75 1.00 - — — — -
0.70 0.95 I I T 1P0WER
SHAF
0.90
0.65 -
0.85
—0.60 --080 11 1 1

Oct 00
60-PC-&04
L'7 TSURUMI PUMP B-SERIES PERFORMANCE
SEWA' E&WASTEWATER PUMPS CURVE
MODEL BORE HP KW RPM SOLIDS DIA LIQUID SG. VISCOSITY TEMP.
(TOS)80B21.5 3"/80mm 2 1.5 3485 1.38'/35mm Water 1.0 1.81 CST 60°F
PUMP TYPE PHASE VOLTAGE AMPERAGE HZ STARTING METHOD INS.CLASS
Sewage&Wastewater Pump 3 208/230/460 6.3/6.3/3.1 60 Direct On Line E
CURVE No. DATE PHASE VOLTAGE AMPERAGE HZ STARTING METHOD INS.CLASS
EFF. TOTAL HD. REMARKS:
% M. Ft.
55
16 -
100 - 50
14 -
90 45
80 12 40 -
ti,01
70 35
10 -
60 . 30
8-
50 25
40- 6 - 20
30- 15 -
4 -
20- - 10
2 -
10 - 5
-0-0-0
US GPM 0 25 50 75 100 125 150 175 200 225 250
CAPACITY . . ,
M'/min. 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9
SHAFT POWER
KW BHP
1.50 - 2.0
1.45 -
1.9
1.40 - SHAFT POWER
1.35 - 1.8
1.30 -
1.7
1.25 -
1.20 - 1.6 - - .
1.15 -
- 1.5

241/P'2020
Scan.Order.Done. F't1v1F'S
Details on page Al. Float Switches
Float *Dayt,„ 11.1.110�.
Switches •
tittk,GLANT.
•Normally closed.pump up •Normally open:pump down
for filling applications for dewatering applications
lather Float Pumping Float Ma, No.
Lenpoln Switch Wits Range Switch Loma Item JVA90 No. I t
Vallal a Amps Mtn.•Max.Cord Length Gauge Win Max Contact Nun Temp Brand No. i 1APP4 e e
I(U1 "It •i I.,- No t'Illy ryi , 11"I' F ayton 10A169
115VAC 1+ Inrt I Ito( Nr rally fe 111'i bzyto,, 106170 {
=`f0�— do Ir III( Ale malty rip I2!"f n.Ga 10490
_ 1',TA - "—'torn IA n 7516 e' tiro malty ripen 1259F the Gant 3VA90
� � li1A i1111 Ill Normally Otimi If0'T I;NM,Clarn 2P353
I',''Al 110 - If;h 18 1F5 Normally Open 12091 110L Plait 48150
i 1.3A - 15 n 1.1 P_ Normally Open l WI L11Ve t i+m 30020 ,
Oaths,
m 1 'Irto
a,„ tab, I to IA' 20 it 16 Ye OP Normally Ups _ 140°t D,iy1o, 6PNV7
15A 3'to la' 2511 14 to 28 Not_I r 1407 11411111 104174
�t0� 4. i7t--- p;28 Ncy ;34.r"T`,_L_1l$ NO, 3BY74
iD71 o18' `f l02§ Norm-4 Payton 3BY75
TA 'I3`tior8'_ 1 NOS Normal•)-Crpsed TOT_ 07ytoi 38Y78
3`ra B' 1 to 2R Normally Op 1 11111 Data 6PNU4
r� 1 8 r e28 Normally Qpet 140`r hryto, 6PNV6 No. No. No.
115VA0 '1 '"p i�( 628 41 tlalty0Pn1 IdiPr Qylor coop$ 45JV93 SAEPO 4aJZ56
1 to'1W_ 11. `-18 0 29 Nor Ill) t Ic ed 1.101r-- eaytoi 38Y80
-1 IV it- N- yr�� 771Q2a Normally Open 1,10°F tyaytm 6PNU7 Auto control pumps in sump/sewage and nnnpotable
--3`i ra' 1i --1[B' 7b2A W illy Open1401E Daytor 6PNV1
-28
`- i111P to Normally,arty pt. 11111- bayior 3BY85 include
water applications.
anuiCat sta All mounting strap.
switches
to A 1 ta"28 Not hall Open 140
mit
01
Me
fo err ,_"'1G 7 to 2a1 teu1 3 I 170 F north 6PNV6 adjustable strap.
i
__ a]iF 1 tyoouAr i r n 1,101E 11010 yWith limit ll Il1F1At UI WIIn9WIU;IirY1llairdclmtn
2'iOVAG �'- to 1E'- 1i.'"` rh iip 2A PI lmelfr I`tw. I t0`F taytml 6PNpe Vertical—Ideal for use in limited space.No.3VA90 can
-'1 II-,
Normally lip1101'f Daylo, coons he wiled for 230V
-7 tot '7trr1—"- 11 'to 28 !tortoni,Opel 11r?'f Day11n coons
15A' 3ro� ft I t to 211 11 II Ope 110'r itaylw 6PNV5
'�11Mr,bib Mil Diaphragm—Water-pressure activated,Control pumps
11,l 1C 1 yA--"'3tnIgr—'311 tl 1 I 111u 00 Norm,111y I p n I tt.1 D4y1<p 10A17S 11 m 10'.9 HP at 120VAC.
'21OVA.t� 15A Troll) -antl 11 I?toGO NotttIAOpen l.irr Paylol 1gA176 r
11,`fi'll I r ?'to m I;It II ,In 78 Normally Oleo 221'f Daytn1 10A1/3 Tether,Daylong,Normally Closed—Switches turn
i isvAc •7A 3 tr,yr o:,tt u• 7 to 28 Nor malty Open lur'F Daymt 38Y81 on(close)when the float drops 45°below horizontal.
TOOL C1wMaMedstaul
1 t3vA1. 17A J in IN' 19 p 10 7 to 34 Normally Oikn 1dil T DayIol 38Y82 Signaling a low level,and turn ott(open)when the float
•',A ,m'Itt A it In 7 It.34 Not many Oran 1.10'I Daytm 3BY83 rises 45'above horizontal
'1 ' 1r 1 16 i to 34 NM Iliad''nimn 1,1111 Oaylgt 36084
Tathsr,Control Pa ai Nilat Daly Tether,Chemical-Resistant—Mechanical blue
I, NI if, - Normally OlMn 140'1 Oaytol 10A172
m ,or 1 a' 20 Ft 18 Normally Omni Lill Drylot 30y79 switches have ABS float and 115V or 220V series plugs.
Dual Km weed - o Notr I b e RAY w11n,monat;ais lzvnpatilee w1111 twtiol mmsborhral
I - r1 Ft� L1h II AAp>.Slat)r FJurnmiBr open h"}t'F harm IAPPd
toll 1y1 9dlustallo Formally Open ICI*I MCC Pro Seri, 38c748 Tether Control Panel/Mot
e Who tingleDuty—No.10A172 is
SA PwnpM.nt-IA i1 to 2J IA h IA Tlido Nnlmpll�Cltued 140'1 51F nanml u: 45Jz4B mechanically-activated with tether clamp.No.1079 is
I SA__3,4", i5 h 16 Np1me y Open 14n'F SA'Rh, 1 ,. 454209 merctlrv-BClIVated WI111preset tether length
12t1t23UVAcI
R ifi 36 Normpally 0pan NV-
tti°F fi lr t`l l . ',VI?
9
7f'--tE ��"TT in 31+ Normpll�yt Ch>s,i I'Y+r"' S t 1u I s 45Jz42
4'' t6 7ia,36 NnmlalTyOpen f4tNF' SJCPtn L 4slz11 SJE PumpMaster°—Wide-angle pump switches are
n 16 7fg Ntml'soe( 14h'r $Jr Rnml 111, +slz24 mechanically-activated and can automaticady control
0Y t 4' t3h 1 Tl 3 1loEn COpen 14l SJt-nhotnI ; 45Jz25 Dums upt0 43 HP at 120 VAC antl 1 HP at 230 SAC.
110VAC 1' ISd Te Nann• Open Tang 83F,Roennus 45JY92
•23 ,_ T rfi �ldArne t9rad S.IF Rhn 6u, +53226
SJE PumpMasterW Plus-These rnechaeticalty-acti-
3A- to 4 .._ tf A�� 'bunt(ma p tr 13r 5 E•Rilnml us 45JY93 voted.pon7 switches can aatomaticatl Control pumps
11A 1 0411 elooga 1401E SJE-Rhombus 45J227 P Y
'+A 4"-- .3 r p -t dmr SJF-Rhanhne 45JY94 up to 3'4 HP at 120 VAC and 2 HP at 230 VAC
_ ''�pr'lify.rikiil`"140T -Womb,
VIo li 4slz44 SJE AmpMasterm Plus-Mechanically-activated
' A 3 e t4 11----N� TfoMi Mil if Nog 'Jar SJt--Wo 1 I > 454Z45
154 11 io .P - it ;_-7kk. Norm y Op n 1417r s -ntmml,e 45.1213 Pump switches can automatically control pumps up to
3Yor23OVAC t 4'm B Noringlfyylosed rgo'F S rF atir-o : 45Jt46 1 v2 HP at 125 VAC and 3 HP at 250 VAC.
- Q Whir Opperi ierr s ii rI n h o- d5Jz14
PF I I' h: Normatl Qusad ,i 0'F Sf(Fh, t 45Jz47
,- to T-Igh -14--- ro�B Normal�ynpen i 0.r Sir rt; t i, 45Jz15 central switches,SJE SlgnalMasterm-These
-1,., 10 f h 4 fo lbormally Open .1 F SI.cootto., 45JY95 mechanically-activated control switches are designed
-F. t5 fi IT• r le Nntnlaliy Open 1( sp.-phi.ton, 45JY96 In activate pump control panels and alarms.Normally
12oVAC _,1 2nii 14 '7896 Nmmall Glossa T I( Sal In 45Jz30
4' 30 n I 1 7-inT6 Normally Open "1'ii sdt r"u,I , 45JY97 open thigh level)switches turn on(close)when the float
14.-4' ni it 14 7tp 36 Normally Open I SJF Rno rous 45098 lips slightly above horizontal signaling a high level,turn
230VAC 15A a1 1n 24' .ill n 14 7In 31, Normally Olen 140'
1 SJF-Rbomldhs 45287
SJE AmpAlasier►hts Tether oft(open)when float drops below horizontal.Normally
1, ':I, ?to?4 Nan ally nimi. 120'f • t 5AFF0 closed(low level)switches turn on(close)when the
J Nally lit r 120'r 36 ,,,r, WW1
'I tint malty Ibl 1 190"F i suuP2 float tips slightly below horizontal signaling a low level,
rrnn -I N,many Spot on' C,, .-4 5AFP3 turn ON(open)when float drops above horizontal.
Control Bwitebes SJE SignalMastet Nartnw Angle
1 nlully Open 140 I 'JEF 45J216 Control dlfferenual i Si vi'above Nt below honzofttal.
, 1 mall fi 1R1 14111 S1 us 45J2a8
r' n rltn, 14n" I • SJE PumpMastere WPS,Potade Water-
125t25oVA3' LI i' 20 n- Ii _ Normaly O e, 140'r ',tr'mmh o 45Jz_t Mechamcall activated control switch can control
Aln tit Nornian) pert Ian 1.1 . Y-
,t a 'M IN - Nomlallyy�Closed""140'r c0-Rhombi., 453253 pumps up10:";HPat120 VAC and 1HPat230 VAC,of
I' Florniattylliall 140'r Sit-nhl s +5JZ22 Controls
brine pti m, ..Tgm- 8.17.144.311m, 45223 applications as low as t 20 VAC,t t10 mA,Motel
SJE Pan,pMasle, WOO Poi hie Wahl,Wide Angle can be wired to work to either pump down(normally
i 0 A - ,,,,, tJorrnAly'Onani I III S4F'uo ,t,na 53c041 open)of pump up(normal) closed)applications(single
a 4ugnc Nermahy C rich I P I Y PP q
hem pole,double throw).Switch can be used b1 food grade
osserlpUu m t r Use With Brand Na. and potable water applications.
7, ACcei,orlc -
9m kl "F1wla wii6lB�2�18 t 7 1gt�-SJOW `dyer rd`s 57E•Rh I54261
,,
e�V in .urmnmad-ales W lea IMF f9716'3 rt2"i reaFd Lae -81rRI1,11i 45.256• Swlk:h Arxeasorks-No 45JZ57 can mount up tO
Se ActtnnmorlatesS 1ri7JiW 1ar7'1513 tfwThip'-r412 f{3'W0i 4idiSSe 821Ch lml 45JZSd 4 float cables No 45JZ58 seals off cables coming into
'Ca a damp'" 14na ie"ft'a a Rhomh r 45.260 an enclosure.Nos.45JZ59 to 45JZ61 can mount a float
-C`alfrn Noll: - W pa 4ViieiGa 1fie .- `" '"—� Rhomhhs 48J260
'Caole gamy In ga Awl 16 oa Wire/Cabli SJE-ilhamlnw 45259 cable to PVC pipe
/-800-GRAINGER{4z2-4643) WARMS:Use only wall nonflammable uglncs compatible with 2629
Any cont6Mvt materials and in nnnthamwable/nonexplostve alm0sohery=.
1/1

SPEARS TRUE UNION 2000 STANDARD BALL VALVES
// )
Features — PVC, CPVC
Economical, low profile quarter-turn shutoff valve is
excellent for general purpose and many O.E.M applica-
tions. PVC and CPVC valves are available in IPS sizes
1/2"through 4" with socket,regular thread, SR threaded
(Special Reinforced), flanged or spigot end connectors.
• Chemical & Corrosion Resistant PVC or CPVC
Construction
• Interchangeable with all True Union 2000 Valves,
Mates with Union 2000 Pipe Unions
• High Impact Polypropylene Handle
• Schedule 80 Full-Bore Design
• Strong, Buttress Thread Union Nuts
• Spears®Single 0-ring Safe-T-Shear®Stem Design
• Spears®Safe-T-Blocked®Seal Carrier
Sample Engineering Specification
• Replaceable PTFE/HDPE Floating Seat Design
All thermoplastic ball valves shall be True Union 2000 • EPDM or FKM 0-rings
Standard type manufactured to ASTM F 1970 and constructed
•from PVC Type I, ASTM D 1784 Cell Classification 12454 Sizes 1/2" 2" pressure rated to 235 psi @ 73°F
or CPVC Type IV.ASTM D 1784 Cell Classification 23447. • Sizes 2-1/2" - 4" and all flanged pressure rated to
All 0-rings shall be EPDM or FKM. All valves shall have 150 psi @ 73°F
Safe-T-Shear'' stem with 0-ring stem seal. All handles shall • EPDM valves NSF®Certified for Potable Water use
be polypropylene. All union nuts shall have Buttress threads. • Suitable for Vacuum Service
All seal carriers shall be Safe-T-Blocked'". All EPDM valves • Assembled with Silicone-Free, Water Soluble
shall be certified by NSFn International for use with potable Lubricants
water. All 1/2"-2"valves shall be pressure rated to 235 psi,all • Manufactured to ASTM F 1970
2-1/2" -4" and all flanged valves to 150 psi for water a,733F,
as manufactured by Spears' Manufacturing Company.
Quick-View Valve Selection Chart Optional Accessories*
Valve 0-ring PVC Part Numbers Pressure •Retro-Fit End Connector
Size Material Socket Threaded SR Threaded Flanged Spigot Rating Sets for Valve Replacement
EPDM 3629-005 included 3621-005SR 3623-005 3627-005
1/2 FKM 3639-005 included 3631-005SR 3633-005 3637-005 •Split-Nut Repair Kits for
EPDM 3629-007 included 3621-007SR 3623-007 3627-007 235 psi Union Nut Replacement
3/4 Non-Shock
FKM 3639-007 included 3631-007SR 3633-007 3637-007 Water •Supplemental End
1 EPDM 3629-010 included 3621-010SR 3623-010 3627-010 ©73°F Connectors
FKM 3639-010 induded 3631-010SR 3633-010 3637-010 •Round Safety Handles
1-1l4 EPDM 3629-012 included 3621-012SR 3623-012 3627-012 (Flanged
FKM 3639-012 included 3631-012SR 3633-012 3637-012 150 psi •Stem Extension Kits
EPDM 3629-015 included 3621-015SR 3623-015 3627-015 Non-Shock) •Square Operator Nuts
1-1l2 FKM 3639-015 included 3631-015SR 3633-015 3637-015 Water G p
EPDM 3629-020 included 3621-020SR 3623-020 3627-020 73°F •Multi Mount Valve/
2 FKM 3639-020 included 3631-020SR 3633-020 3637-020 Actuation Mounting Kits
EPDM 3622-025 3621-025 3621-025SR 3623-025 3627-025 •Mini-Mount Actuation
2-1/2 FKM 3632-025 3631-025 3631-025SR 3633-025 3637-025
150 psi Mounting Kits
3 EPDM 3622-030 3621-030 3621-030SR 3623-030 3627-030 Non-Shock *See"BALL VALVE ACCESSORIES"
FKM 3632-030 3631-030 3631-030SR 3633-030 3637-030 Water section for details of individual products.
EPDM 3622-040 3621-040 3621-040SR 3623-040 3627-040 @ 73°F
4 FKM 3632-040 3631-040 3631-040SR 3633-040 3637-040
1:For CPVC valve,add the letter"C"to the part number(e.g.,3629-005C,3621-005CSR)
NOT FOR DISTRIBUTION OF COMPRESSED AIR OR GASES
22

TRUE UNION 2000 STANDARD BALL VALVES
4 E -
) ri/7 oe,er.jivrillar
0 0 0 0 0 0 0 0
0 Replacement Parts
m
No. Component Qty. Material
0 1 Seal Carrier 1 PVC/CPVC
0 i�„„ 2 Body 1 PVC/CPVC
F►I ,
D . •NaK ����„�jm9� 3 Carrier 0-ring 1 EPDM/FKM
'';, 4 Stem Bearing 1,2 1 PP
,; 5 Stem 1 PVC/CPVC
• y ' ' /; 6 Handle 1 PP
A F 7 Stem 0-ring 1 EPDM/FKM
8 Ball 1 PVC/CPVC
% '%` 9 Seat 2 PTFE/HDPE
,,,,, „, /,';!� %�r�rl 10 Union Nut 2 PVC/CPVC
%'/,j%
g- ► ��� 11 End Connector 0-ring 2 EPDM/FKM
' � 12 End Connector 2 PVC/CPVC
C' 1:0-Ring up to 2"
2:PTFE Thrust Bearing:2-1/2",3"8 4"
I G -
Dimensions, Weights, Operating Torque & Cv Values
Nominal B1 C Approx.Wt. Oper.2 Cv Values3
Size A D E F G (Lbs.) Torque
Soc/Thd Spigot Socket Thread Spigot PVC CPVC(in.lbs.) SoclThd/Spig Flanged
1/2 1-7/8 2-7/16 2-7/8 4-3/16 3-13/16 4-5/8 1-5/8 2-1/2 3-1/2 2-31/32 .33 .35 12 29 18
3/4 2-1/4 2-3/4 3-1/4 4-3/4 4-1/4 5-1/4 2 3 3-7/8 3-5/16 .51 .54 20 63 39
1 2-1/2 2-7/8 3-1/2 5-1/8 4-11/16 5-3/4 2-5/16 3-7/16 4-1/4 3-5/8 .71 .75 25 120 73
1-1/4 3-1/16 3-1/4 3-13/16 5-3/4 5-3/16 6-5/16 2-13/16 3-9/16 4-5/8 3-31/32 1.12 1.17 35 243 151
1-1/2 3-1/2 3-1/2 4 6-1/4 5-7/16 6-3/4 3-1/16 3-7/8 5 4-3/8 1.47 1.53 45 357 223
2 4-1/4 4-3/4 5-13/16 7-3/4 6-3/4 8-1/4 3-3/4 5 6 5-1/4 2.62 2.75 94 599 395
2-1/2 6-3/16 7 7-13/16 10-1/2 8-1/2 11-3/8 5-7/8 7-5/8 7 6 7.42 7.70 120 856 579
3 6-3/16 7 7-13/16 10-11/16 9-3/4 11-9/16 5-7/8 7-5/8 7-1/2 6-13/16 7.46 7.81 120 1416 974
4 7-5/8 7-1/2 8-1/4 12-1/16 10-1/4 12-3/4 6-3/4 6-3/4 9-1/16 7-1/2 12.35 12.48 336 2865 1952
1:Valve Lay Length
2:Torque required at valve maximum internal pressure rating,5ft/sec.Flow velocity;due to adjustment differences during installation,actual valves may vary.
3:Gallons per minute at 1 psi pressure drop.Valves calculated from laying length,based on derivative of Hazen-Williams equation with surface roughness factor of C=150.
'Temperature Pressure Rating
System Operating 100 110 120 130 140 150 160 170 180 190 200 210
Temperature°F(SC) (38) (43) (49) (54) (60) (66) (71) (77) (82) (88) (93) (99)
PVC 235 211 150 75 50 -0- -0- -0- -0- -0- -0- -0-
1/2"-2" (1.62) (1.45) (1.03) (.52) (.34) (-0-) (-0-) (-0-) (-0-) (-0-) (-0-) (-0-)
Valve 235 219 170 145 130 110 90 80 70 60 50 -0-
Pressure CPVC (1.62) (1.51) (1.17) (1.00) (.90) (.76) (.62) (.55) (.48) (.41) (.34) (-0-)
Rating
psi
a) 150 135 110 75 50 -0- -0- -0- -0- -0- -0- -0-
(MP 2-1/2"-4 PVC (1.03) (.93) (.76) (.52) (.34) (-0-) (-0-) (-0-) (-0-) (-0-) (-0-) (-0-)
CPVC 150 140 130 120 110 100 90 80 70 60 50 -0-
(1.03) (.97) (.90) (.83) (.76) (.70) (.62) (.55) (.48) (.41) (.34) (-0-)
NOT FOR DISTRIBUTION OF COMPRESSED AIR OR GASES
23

1
SPEARS Utility Swing Check Valves )PVC White
Std Mstr Disc
Size Socket Thread SR Threaded Pk Pk Code
'' 1/2 S1520-05 51520-05F S1520-05FSR 35 0 026
' -,, 15.85 15.85 18.49
"-.,: 314 S1520-07 S1520-07F S1520-07FSR 35 0 026
16.36 16.36 20.12
Ns
1 S1520-10 S1520-1OF S1520-1OFSR 20 0 026
- 17.04 17.04 22.28
_ S1520-12 S1520-12F S1520-12FSR
1-1/4 12 0 026
17.70 17.70 26.11
S1520-15 S1520-15F S1520-15FSR
1-1/2 12 0 026
18.76 18.76 33.12
2 S1520-20 S1520-20F S1520-2OFSR 15 0 026
29.12 29.12 44.70
'`g 21/2 S1520-25 51520-25F S1520-25F5R 5 0 026
48.44 48.44 64.02
3 S1520-30 51520-30F S1520-30FSR 4 0 026
53.83 53.83 95.47
4 S1520-40 S1520-40F S1520-40FSR 2 0 026
76.21 76.21 119.36
6 S1520-60 S1520-60F 51520-6OFSR 1 0 026
• Engineered for Maximum Flow,Quick Response& 160.13 160.13 211.21
S1520-80
Positive Shutoff 8 --- --- 1 0 026
297.47
• Excellent for Pool&Spa,OEM and General Purpose
Applications PVC Clear
• Compact, Space-Saving Design
Std Mstr Disc
• PVC White or Clear Sealed Unit Size Socket Thread SR Threaded Pk Pk Code
• All Plastic Construction-No Metal Parts 1/2 S1520005 51520005F S1520C05FSR 35 0 026
• Angled Seat and Weighted Flapper for Low-Pressure Seal 21.55 21.55 24.18
• High Grade EPDM Seat 3/4 S1219707 S1210977F S1522578FSR 35 0 026
• Suitable for Horizontal or Vertical Up-flow Installations 51520C10 S1520C1OF S1520C1OFSR
• Socket,Threaded,or SR Threaded End Connections 1 22.39 22.39 27.64 20 0 026
1 114 S1520C12 S1520C12F S1520C12FSR 12 0 026
General Installation Information: Swingcheck valves23.51 23.51 31.89
are 1-1/2
51520C15 01520C15F S1520C15FSR 12 0 026
designed for horizontal installations, but may be installed in up-flow25.55 25.55 39.93
only vertical position. Check valves MUST be installed with the 2 S1520C20 S1520C20F S1520C2OFSR 15 0 026
valves FLOW arrow pointing in the direction of the flow. Do not 36.78 36.78 52.36
install valve upside down. Flow velocityshould not exceed 5 S1520C251.31S152.31 S1520C25FSR
p 2-1/2 61.31 61.31 85.47 5 0 026
ft./sec.Minimum opening pressure less than 0.5 psi. 3 S1520C30 S1520C30F S1520C3OFSR 4 0 026
68.13 68.13 109.76
4 S1520C40 S1520C40F S1520C4OFSR 2 0 026
134.83
Pressure Rating73°F 23°C ,Water s1.71 91.71 2OC6O
( ) 51520060 51520060F S1520C60FSR
Full Flow(open) 150 psi 6 189.55 189.55 240.64 1 0 026
( p ) 8 S1520080 --- --- 1 0 026
Back Pressure(closed) 75 psi 316.63
Maximum Service Temperature
140°F(60°C)
Temperature/Pressure De-ratings Apply
NOT FOR USE WITH COMPRESSED AIR OR GAS
Page 1 Spears®Manufacturing Company
Progressive Products from Spears® Innovation and Technology

Utility Swing Check Valves ■SPEARS '
Technical Information
miammiellime 111141711.1Thbilimp
A D Iiiiii!hi A I
momcm.jrim. dill4C•0•7111°
g i e
c
FLOW
Dimensions
Dimension Reference(inches,±1116)
Nominal Size B
A Socket ThreadedlSR Threaded C D
1/2 1-3/8 2-19/32 2-5/8 4-3/32 2-1/8
3/4 1-3/8 2-5/32 2-1/16 4-1/16 2-1/8 -
1 1-11/16 2-5/16 2-15/16 4-9/16 2-5/8
1-1/4 2-1/16 2-15/16 3-5/8 5-1/2 3-3/8
1-1/2 2-7/16 3 3-11/16 5-5/8 3-3/8
2 3 3-5/8 4-3/8 6-3/8 4-1/4
2-1/2 3-9/16 4-3/8 5-1/4 7-7/8 5-1/8 -
3 4-5/16 4-11/16 5-5/8 8-7/16 5-3/4
4 5-1/4 6 7-1/16 10-1/16 6-3/8
6 7-11/16 8-1/2 11-5/16 14-9/16 9-1/4
8 9-7/16 11-3/16 N/A 19-1/4 11-15/16
NOT FOR USE WITH COMPRESSED AIR OR GAS
Made in the U.S.A. Page 2
Progressive Products from Spears® Innovation and Technology

SULZER
Submersible mixers
type ABS XRW 210 and 300
,,,..._
,,
5
.. .\ ,
•
ULZ
i . ,
1
1
1
i
O
P�t'
C
\ ..„, . y •
7�� �

Main industries and applications
The submersible mixer type ABS XRW is a compact and versatile mixer with a wide range of applications,
including use in aggressive and abrasive liquids.
Its design makes it particularly suitable for mixing and stirring applications in sewage treatment plants and
industrial areas such as:
• Equalization of sewage
• Biological processes (aerobic, anoxic and anaerobic)
• Selector(contact zone)
Also applicable for homogenization of highly concentrated sludge and slurries such as:
• Primary, secondary and digested sludge in storage and buffer tanks
• Lime and mineral slurries
Hazardous locations: �� O'
• Certification for ATEX(Ex II 2G Ex h db IIB T4 Gb), 0 O::�
FM and CSA available as an option
Water and General Pulp,paper
wastewater industry and board
Features and benefits
The following features and benefits apply to the 210 and 300 models of the submersible mixer
type ABS XRW, which are used for mixing at high speeds.
Energy-saving, Premium Efficiency 1E3 asynchronous motor
• Ensures the lowest possible energy consumption
• Keeps operating temperature low for longer product life
Large, long-lasting bearings
• Offer true reliability with a calculated lifetime of more than 100'000 operating hours
• Need no maintenance—lubricated for life
Pre-loaded upper bearing
g
• Prevents spinning through the design of the outer ring
• Eliminates backlash
• Ensures longer bearing life
Large rotor shaft
• Keeps shaft deflection to a minimum through heavy-duty construction
When you choose our
submersible mixer XRW, you
choose the market's best
ongoing energy performance.
You also get the best lifecycle
cost, from initial purchase to
ongoing operation.

Sealed connection chamber with quick-connection block
• Simplifies mixer maintenance
• Safeguards the motor to ensure high reliability
Triple seal system with dual oil chamber
• Improves motor protection
Enhanced mechanical seal protection system
• Keeps the mechanical seal clog-free
• Greatly extends the life of the seal
Hydraulic-optimized investment-cast propeller
• Ensures the highest possible mixing performance
• Reduces maintenance through self-cleaning
Abrasion-resistant, galvanically insulated mast bracket and suspension
• Reduces the risk of electrochemical corrosion
TCS (Thermo Control System)
• Provides a warning or switches off the motor automatically before the permissible temperature limit is
exceeded, whether due to high-temperature medium or another problem source
Q Premium Efficiency 1E3 motor
® Lower bearing
Q Upper bearing
Q Rotor shaft
Q Sealed connection chamber `-
0 Dual oil chamberi 9
[ • 11 w
0 ,....-
Or� gowslo© _
� x
e c gp
. 4
i
e
)1605
Q Mechanical seal
0 Propeller
0 Mast bracket
CI Suspension
Q TCS(Thermo Control System)

2 Technical data
The maximum noise level of the units of this series is 5 70 dB(A). In some types of installation it is possible that
the noise level of 70 dB(A)or the measured noise level will be exceeded.
Additional technical information is available in the XRW technical data sheets which can be downloaded from
www.sulzer.com > Products> Submersible Mixers.
2.1 Technical data XRW 210 and 300
a is" a"
i
`] a) a' o
a�
c E a) 3 o c o .Q
1° a�i a n am 3 E r
v
.2 N 0. O d d -0 .c N o C N
2 co o c = a) I- O co o 5
a o m co •X u
2 2 a) o cc a1
a co c ao
50 Hz [mm] [1/min] [kW] [kW] [A] [N] [kW] [kW] [kg]
2121 210 1424 PA 08/4 0.9 0.8 1.8 156 0.7 0.8 33
2131 210 1437 PA 15/4 1.8 1.5 3.7 207 1.0 1.2 41
2132 210 1437 PA 15/4 1.8 1.5 3.7 285 1.2 1.4 41
2133 210 1437 PA 15/4 1.8 1.5 3.7 304 1.5 1.7 41
2141 210 1424 PA 08/4 0.9 0.8 1.8 - - - 39
2151 210 1437 PA 15/4 1.8 1.5 3.7 - - - 47
2152 210 1437 PA 15/4 1.8 1.5 3.7 - - - 47
2153 210 1437 PA 15/4 1.8 1.5 3.7 - - - 47
3021 300 958 PA 15/6 1.8 1.5 3.5 289 0.9 1.1 62
3022 300 958 PA 15/6 1.8 1.5 3.5 350 1.2 1.4 62
3023 300 958 PA 15/6 1.8 1.5 3.5 409 1.3 1.6 62
3031 300 971 PA 29/6 3.5 2.9 7.3 456 1.6 2.1 82
3032 300 971 PA 29/6 3.5 2.9 7.3 564 2.2 2.6 82
3033 300 971 PA 29/6 3.5 2.9 7.3 695 2.7 3.2 82
3041 300 958 PA 15/6 1.8 1.5 3.5 - - - 73
3042 300 958 PA 15/6 1.8 1.5 3.5 - - - 73
3043 300 958 PA 15/6 1.8 1.5 3.5 - - - 73
3051 300 971 PA 29/6 3.5 2.9 7.3 - - - 93
3052 300 971 PA 29/6 3.5 2.9 7.3 - - - 93
3053 300 971 PA 29/6 3.5 2.9 7.3 - - - 93
60 Hz [mm] [1/min] [kW] [kW/hp] [A] [N] [kW/hp] [kW/hp] [kg/Ibs]
2121 210 1735 PA 18/4 2.1 1.8/2.4 3.5 255 1.1/1.5 1.3/1.6 41/90
2131 210 1735 PA 18/4 2.1 1.8/2.4 3.5 310 1.7/2.3 _ 2.0/2.7 41/90
2141 210 1735 PA 18/4 2.1 1.8/2.4 3.5 - - - 47/102
2151 210 1735 PA18/4 2.1 1.8/2.4 3.5 - - - 47/102
3021 300 1153 PA 18/6 2.2 1.8/2.4 3.4 484 1.7/2.3 2.1/2.8 62/131
3022 300 1169 PA 35/6 4.1 3.5/4.7 6.9 565 2.1/2.8 _ 2.6/3.4 82/181
3023 300 1169 PA 35/6 4.1 3.5/4.7 6.9 660 2.3/3.1 2.8/3.8 82/181
3031 300 1169 PA 35/6 4.1 3.5/4.7 6.9 717 3.1/4.1 3.6/4.9 82/181
3041 300 1153 PA 18/6 2.2 1.8/2.4 3.4 - - - 73/162
3042 300 1169 PA 35/6 4.1 3.5/4.7 6.9 - - - 93/206
3043 300 1169 PA 35/6 4.1 3.5/4.7 6.9 - - _ - 93/206
3051 300 1169 PA 35/6 4.1 3.5/4.7 8.9 - - - 93/206
*50 Hz at 400 V;60 Hz at 480 V.
Starting.Direct On Line(D.O.L)
6

2.4 Dimensions (mm)
2.4.1 XRW 210
150 4
1 ill ----,
E
I N
iiiI 2 • •
- -
-Max.30 ! . ] 1
•/�/ w® Iiiij::f!r.
• • ' ''
II
Min.30' \ \ ` �,
A $ PPAA 01188//44,PPAA 188//44:44988 ..
. .
Min.450 :•'
i
I Vertical adjustment limits Wall mounted on adjustable bracket
Floor mounted on adjustable bracket Floor mounted on concrete base
1
& .i
II
ii
I■if elm
���IIII�11�
N /
I A 11.II
G VA"
019.5 „toIOC
r _ Y
700
Figure 1:Dimensions XRW 210
9

15.0"
MAXAIR DIFFUSER (TYP)
o
'
21 .0" II I �I II
BALLAST FRAME ....
BALLAST
S.S. PIPE STRAP (TYP)
FEEDER AIRLINE TO
AIR LATERAL
63.41 "
- • • • • • • • f I (0) t.,
5.0"
NOTES: -
1 . STAINLESS STEEL COMPONENTS (BY EDI) BALLAST FRAME
TO BE CAST IN CONCRETE.
2. BALLAST USES CONCRETE WITH A
DENSITY OF 145#/ CU.FT. MIN.
' 1 /ENG.BY: DWG.BY: ENVIRONMENTAL DYNAMICS INC.
MAXAIR DUPLEX DIFFUSER ASSEMBLY TEM PARTS ROAD
WITH PLASTIC BALLAST FORM REV DATE , 5AL COLUMBIA,MISSOURI 65202
TYPICAL INSTALLATION DETAIL. B 10-3-08 ..,,✓rvMtO
PHONE:[phone]
DATE: SCALE: DWG NO: FAX:[phone]
5-11-94 N.T.S. J ` 5889 WWW.WASTEWATER.COM9

66.6
++ PVCM a xA 1 rTM
DEL PRODUCTO
aeration for life Difusor de burbuja gruesa
• Configuration simple o duplex.
Duplex • Disenado para una alta capacidad de flujo de aire.
• Disponible en longitud de 610 mm (24 pulgadas).
• ; • Diseno resistente a las obstrucciones con purga
• - automatics.
• Perimetro completo de liberation de aire de 1220
mm (48 pulgadas).
• Hay unidades estandar en el inventario disponibles
, para su envio inmediato.
• Unidades estandar con la parte inferior abierta y
Simplex con la parte inferior cerrada opcional disponibles.
• Construction de PVC u opcional de CPVC para
ofrecer la maxima resistencia quimica y termica.
• Descarga de aire de tres niveles para ofrecer una
operaciOn con un rango de flujo amplio.
• Completamente no metalico, resistente a la
corrosion.
SPECTRUM SADDLE MOUNT
LATERAL DE AIRE 1 (EL MODELO PUEDE VARIAR)
ORIFICIO DE SALIDA DE AIRE(TYP)
CUNA /*. —
MODELO CON PARTE INFERIOR MODELO CON DEFLECTOR 1
ABIERTA
SISTEMA METRICO SISTEMA INGL S
Tipo de Flujo de aire Longitud Tamano del Flotabilidad Peso Tipo de Flujo de aire Longitud Tamano del Flotabilidad de Peso
difusor de diseno del difusor orificio de operaciOn seco difusor de diseno del difusor orificio operaciOn seco
m3N/h mm m2 i kg kg scfm in ft2 I lb lb
Simplex 0-79 813 Disenado adec- 4.9 2.7 Simplex 0-50 32.0 Disenado adec- 11 6.0
uadamente para uadamente para
Duplex 0-158 1630 cada proyecto 7.7 5.0 Duplex 0-100 64.0 cada proyecto 17 11
Visite www.EnvironmentalDynamics.com o www.wastewater.com

Environmental Dynamics International
MaxAir PVC : Difusor de burbuja gruesa
Procesos:
AireaciOn biologica.
Procesos de lodes activados.
Zanja de oxidation. ---
...bur
Si
l Reactores discontinuos secuenciales
(SBR, por sus siglas en ingles).
�_. _ Reactores biologitos de membrane .
1 (MBR, por sus siglas en ingles).
Reactores biologicos de echo rnovil
(MBBR, per sus sighs en ingles). I. .... .........._
Digestion/estabilizacion de-----11112111111m :1 Plantar paquete.
�_....._
Aplicaciones: Industries:
0 p,
Aguas residuales municipales. .,, 4 Alirnentos y bebidas.
Aguas residuales industriales. Lacteos y queso.
Sistemas fijos a piso. l ) i:- Pulpa y papel.
Sistemas removibles. PetrOleo y gas.
Mezuado. Procesamiento animal.
Alta transferencia de oxigeno. Lixivados.
Perdida de carga baja. Energia y electricidad.
Farmaceutica.
El exito de EDI se ha demostrado en
mas de 7,000 instalaciones realizadas
en mas de 100 paises en todo el mun-
do, con to que se ha brindado servicio �-
a mas de 400 millones de personas. _= '" -,,
Comuniquese con la oticina local
�' que se indica abajo para conocer los
detalles de nuestros productos, `� .
sisten"ias y procesos comprobados. .,
ti.
EDI Europa America del Norte:Of icinas centrales intemacionales China
Diseno,fabrication y almacen Diseno,fabrication y almacen Oficina de diseno
Tel: [phone] Tel:[phone] Tel:[phone]
[e-mail] [e-mail] [e-mail]
Alemania Mexico JapOn
Oficina de diseno Oficina de diseno Oficina de diseno
Tel: [phone] Tel: [phone] Tel: [phone]
[e-mail] [e-mail] [e-mail]
Francia Singapur(SEA) India
Oficina de diseno Diseno y almacen Oficina de diseno y fabrication
Tel: [phone] Tel: [phone] Tel: [phone]
[e-mail] [e-mail] [e-mail]
©Environmental Dynamics International,Inc.,todos los derechos reservados.
Debido a nuestra polltica de desarrollo continuo de productos,Environmental Dynamics International,Inc.se reserva el derecho de modificar en una fecha posterior cualquier
especificacibn publicada sin previo aviso.
`'S ;,>: , ' Visite www.EnvironmentalDynamics.com o www.wastewater.com

FLOATING PE AIR
LATERAL
I I I I
ala
S.S. PIPE STRAP CONCRETE FILL I
Ci -- NOME Via'
mii
FLEXAIR MAGNUM U
TUBE (TYP) 80' ® I
ROPE SNAP
P.P. RETRIEVAL ROPE FEEDER AIRLINE P.P. RETIEVAL ROPE
(TIED OFF AT DUAL LEG
ANCHOR ON DIFFUSER)
S.S, H❑SE CLAMP ROPE SNAP DETAIL
J
PLASTIC BALLAST FORM
NOTES:
1, STAINLESS STEEL COMPONENTS 6 END.BY: DWG.BY: ENVIRONMENTAL DYNAMICS INC.
(BY EDI) TO BE CAST IN CONCRETE, FLOATINGMAGNUM DIFFUSER ASSEMBLY BLM TEM 5601 PARIS ROAD
2, BALLAST USES CONCRETE WITH A FOR 88S-24,88S-16,88F/S-16,44S-24,44S-16 REV DATE , COLUMBIA, MISSOURI 65202
DENSITY OF 13ft, TYPICAL INSTALLATION DETAIL F 10/30/13 4,N PHONE: [phone]
DM II. SCALE: DWG NO: �e FAX:[phone]
1/16/2007 N.T.S. 12234 ) WWW.WASTEWATER.COM�
3. TORQUE NUTS TO 20FT/LBS

66.6
ESPECIFICACIONES F I e x A irMagnum
DEL PRODUCTO Difusor con mmbrana flexible de burbuja fina
aeration for life
,
• Ideal para actualizaciones de burbuja gruesa.
• Su geometria eficaz permite aplicaciones con una den-
sidad alta y cobertura del piso superior al 65 %.
so ....,..
• Diseno no flotante para reducir el estres en la conex-
`` ion de montaje.
• Membranas de calidad premium disponibles en EPDM,
uretano y Matrix PIusTM para reducir la acumulacion
de residuos y requerir un mantenimiento minimo.
• Disponible en construction no metalica para ofrecer la
P `. maxima resistencia quimica, termica y contra los rayos
4 U V.
• Diseno con triple valvula de retention que reduce al
minimo el ingreso de liquidos y sOlidos en las tuberias.
Ideal para aplicaciones de encendido y apagado.
84P 42P
I 1 m I I 0.5 m---I
'EU' ''''''
CI
84P-4
1 r---------- 1 E
E
i d+
fr---- ' Int , ,
,„,,,
SISTEMA METRICO SISTEMA INGLES
Flujo de Longitud Peso Flujo de Longitud Peso
Modelo aire tipico total operational Peso seco Modelo aire tipico total operational Peso seco
m3N/h mm kg kg scfm in lb lb
42P micropore 0-16 1390 2.6 3.2 42P micropore 0-10 54.8 5.8 7.1
42P Alta cap. 0-28 1390 2.6 3.2 42P Alta cap. 0-18 54.8 5.8 7.1
84P micropore 0-32 2400 2.9 5.2 84P micropore 0-20 94.3 6.3 11
84P Alta cap. 0-55 2400 2.9 5.2 84P Alta cap. 0-35 94.3 6.3 11
84P-4 micropore 0-64 4880 16.6 10.4 84P-4 micropore 0-40 192 36.7 23
84P-4 Alta cap. 0-110 4880 16.6 10.4 84P-4 Alta cap. 0-70 192 36.7 23
• * Los valores indicados son para cada tuba,a menos que se especifique otra cosa.
• Se logra una optima eficiencia en la transferencia de oxfgeno cuando se opera desde el medio hasta el extremo inferior del rango del flujo de aire.
• La presiOn aproximada de operation en el difusor en el rango medio es de 25.4 a 57.15 cm(10 a 22.5 pulgadas)de H2O(de 2.5 a 5.6 kPa).
• Operar la unidad en el extremo alto del rango provocara un desempeno menor y una presiOn operativa mayor.
• Use el valor maxima de flujo de aire para operaciones de corto plazo coma las cargas pico o el mantenimiento del sistema.
Visite www.EnvironmentalDynamics.com o www.wastewater.com

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e,neu/.cac.o"»um/caua sin pev.oav/m.

Series 20SS Ball Valve SVF
Two-Piece Ball Valve,Full Port
Sizes 1/4" 3 t FLOW CONTROLS
The SVF Series 2055 full port ball valves are designed for general purpose performance in a
wide variety of utility applications. The 20SS is an economical, manually operated valve that
meets industry requirements for performance and dependability.
SERIES 20SS DESIGN FEATURES
./Designed&built for economical
performance
,/Pressure rated for 1000 WOG
✓Full Port flow path for maximum flow
✓316 Stainless Steel body,ball and stem
Ar
✓Threaded End Connections
./Vinyl grip handle
V Blowout proof stem adds safety&reliability
,/Lockable in the"Open"or"Closed"position
1/Oval handles available-Sizes 1/4"to 2"
MATERIALS OF CONSTRUCTION
ITEM DESCRIPTION MATERIALS SPECIFICATIONS
i
316 Stainless Steel
1 Body
- i (ASTM A351-CF8M)
End 316 Stainless Steel Oj
2 �:
Connector (ASTM A351-CF8M)
3 Ball 316 Stainless Steel4.
(ASTM A351-CF8M)
4 Stem 316 Stainless Steel
(ASTM A276-316)
5 ; Seat RTFE
cm
0
6 Body Seal RTFE
7 Stem Seal RTFE
What do you need today?' �NI
: 'atFLows
SVF Flow Controls•5595 Fresca Drive•La Palma,CA 90623•Tel:[phone]•[e-mail]
Specifications subject to change w/o notice.All Data Sheets on our website supersede prior publications•(5VFIOSS.0730)

Series 20SS Ball Valve
Two-Piece Ball Valve,Full Port
Sizes 1/4" - 3 " FLOW CONTROLS
DIMENSIONS,WEIGHT,C V
r ---
A B D L Weight
Size T Cv
in mm in. 1 mm in. mm in. mm lbs kg
in 1
1/4" 1.89 48 0.46 12 3.86 99 1.93 50 0.39 0.2 7
3/8" 1.89 48 0.49 13 3.86 99 1.93 50 0.39 0.2 8
1/2' 2.21 56 0.59 15 i 3.86 99 L 2.09 54 0.56 0.3 11
3/4" 2.56 65 0.79 20 4.73 121 2.48 63 0.87 0.4 21
1" 3.03 77 0.99 26 6.07 155 2,84 73 1.73 0.6 35
1-1/4" 3.55 90 1.26 33 6.07 155 3.05 78 ( 2.22 1.0 57
- - -
r--
11/2 3.86 98 1.50 39 7.25 185 ( 3.62 92 299 L 1.44 80
2" 4.77 121 1.97 50 7.25 185 3.98 102 5.16 2.3 150
2-1/2" 5.71 145 2.56 66 9.65 246 5.08 130 10.19 4.6 265
3" 6.54 166 i 2.88 74 9.65 246 5.48 140 15 45 7.0 415
20SS - PRESSURE/TEMPERATURE CHART
(69) 1000
(55) 600- f /e-I
_a iia
• 4- (41) 600 ems. _ JI
in
a 1 1 I
` _ i
= (28) 400 1 .. I\In
a -
(14) 200-
i
X (7) 100 i
cry;
1
mum,- 1 1 1 - N I - -. _ N
-40 0 50 100 200 300 400 i
(-40) (-18) (10) (38) (93) (150) (204) A
Maximum Temperature Fahrenheit(Celsius)
J
Class 400
Note:Maximum pressure&temperature is limited to the seat material rating
20SS Series Part Numbers
Size Part# Size Part#
1/4" 20SSTH01M 11/4" 20SSTHO6M
3/8" 20SSTHO2M 1-1/2" 20SSTHO7M
1/2" 20SSTHO3M 2" 20SSTHO8M
3/4" 20SSTHO4M 2-1/2" 20SSTHO9M
1" 20SSTHO5M 3" 20SSTH 1 OM
Note:Oval handle option available(PN:P2OLHOV13 sizes 1/4"to 1/2",PN:P20LHOV4 size 3/4",PN:P2OLHOVS6 sizes 1"to 1-1/4"and
PN:P2OLHOV78 sizes 1-1/2"to 2")
SVF Flow Controls•5595 Fresca Drive•La Palma,CA 90623•Tel:[phone]•[e-mail]
Specifications subject to change w/o notice.AN Data Sheets on our website supersede prior publications•(SVF.2055.0720)

ENT
echnologies
WavTex.' by ENTEX Technologies Engineering
Clean Water
a� Solutions
Mov►n • Flex Mc u r •
WavTex
Ff. >-"�
is a moving woven media system using � '•1. ' ;►;, '`+��• '` +
. :- _ Entex's patent pending EnTextile"media ' `r. "� ., e
p p g I�S+.,i .� 4. °"
in Integrated Fixed-film Activated Sludge „„e' ��; i' +2s4
, , -,, ft 7,
,,
' (IFAS) and Submerged Fixed-Film (SFF) i�'+�4 ..e4Y �, `�t
'%, AY is systems. �s. .4 ''+ i , #i0 .
40 4,1 4111k7 414t .fsf, .1
# ' % , , ; Independently moving EnTextile media r w '' ,
i"' V 4 % `It''*';‘;'.'+ sheets continuallywave111i11.``� - ` '410 �. " '� l
' in the aeration
F #$�° 40
E`, a'+a r�', basin in a random motion, ensuring 1 „'�1 `f :4 4 �.*� r
4�4w'• -4`3,'.;•,t excellent oxygen and substrate transfer. i ' 1I ".Akio. :y';#�
. ; .t ,air,. n. -<
;fie€ >'' -, t € .**'s k
WavTex is a cost-effective solution for
' WavTex means' +.. existing activated sludge plants that
Simplicity
,, 16 need more advanced treatment. Because
WavTex equires no in
little or no additional tankage is required,
�_` basin retention or
�" • . . WavTex is ideal for plants with limited
drain screens and
room for expansion"
can be used with
existing fine bubble
EnTextile Media It is also an excellent choice for space diffuser grids for
efficient, high performance new plant
EnTextile media provides an exceptionally maximum energy
designs.
efficiency and
high effective biological surface area, and
minimum retrofit
the narrow thickness of the media provides
costs.
excellent transfer of waste and oxygen to
Entex Technologies Inc
the thin biological film,providing high rate 400 Silver Cedar Court
Suite 200
treatment. Chapel Hill,NC 27514
919.933.2770 phone
919.287.2258
ertexinc"com

WavTex by ENTEX Technologies, continued
WavTex Increase capa ' , • High Per form ar
means
WavTex moving flex media provides Developed based on over 20 years of
Versatility
extensive surface area for biomass experience using attached growth media
growth. The attached biomass popula- for wastewater treatment, EnTextile
Unlike traditional tion can more than double the effective media provides high biomass surface
moving media MLSS concentration. The vigorous area designed to maximize random
systems, WavTex motion of the EnTextile media in the turbulence and open pathways to create
moving flex media aeration basin provides a high shear optimum conditions for substrate and
on the surface of the EnTextile media, oxygen transfer while maintaining bio-
can be used effectively
maintaining a thin biological film. The mass density control.
in both fine bubble
thin film provides for high rate biologi-
and coarse bubble cal kinetics.
Cost Effectiveness
systems,without
the need to remove WavTex improves water treatment
Eliminates Screen"
existing efficient with little or no addition of aeration
fine bubble diffuser Never worry about plugging of retention basins or clarifiers. It's a significantly
screens. The WavTex system also allows less expensive way to upgrade activated
systems.
for a broader range of tank dimensions, sludge plants.
; 1 .., `,a‘",::1,0:04 since the system eliminates the potential
•70 ,^` � i' � , •� for media "bunching"at the back end
`I i1„ sty so. '# gym'
'` �+ tY , *it.r � of long basins. Advanced Systems.Proven Solut .'
t.
'` ` ''''',u.t•p• •ll` 41- >S !'4 ENTEX engineers have been involved
..,`.�' .9 ►.•.� •aft .41 t
:.,q "•'# "' ;"'' :' Nitrification&Denitrification.:. in hundreds of plant installations.
•'4IP. *qv a�. '.r
We'd like to be involved in yours.
€.04 4.4 �., ° ,o.
.�. WavTex provides stable growth
10,•i 1,„y.,��; , A; •,*� platforms for slow growing nitrifiers.
4. '� � .,� +,; • �• Nitrifying plants perform better;
wOsor- 4, " non nitrifying plants are able to
1,7•,.., �..4, •q•,�r•'4; '4',r,.•'•� ,'_•1 nitrify. Plants needing to convert
+F:t' A.4, 2". Afc f to nitrification can do so at a far
. "• r , �. . 1` e,:11, lower cost than adding basins.
Technolo ies
'°P1/�...�y a\a.`,i,�Nyl�/L�•�' .tawT'j.A 's�iV4.1

s 1 r I a sI7 . I ' 1 ' JTION NH ST Y
ZONE - REV DESC DATE DWM , CHK
DISCHARGE 41.76 - - A RELEASED PER ECN 1042672 - -
4 8 NPT ADDED HF408,t041 B1 ADDED OTV AND
MODELS, O7 B2 ADDED SOHP MOTOR,
4.43 18.25 D3 B fA77T1 B3 AD E NOTE,1E6I B4 ADDED 01/19/09 MWS RNS
CHECK VALVE DISCHARGE SILENCER :X 1.18 X 51. SLOT NOTE,ECN 1044423
1.26
'
MOTOR 511 .
- (50HP SHOWN) L- --------
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I VIEW A—A R,�i
1 •NE 1/2-14 NPT DRAIN USED
1-6.77-- FOR DF4506 AND DF4509
THIS LOCATION •
E 36.23 E
NLET FILTER
DIFFERENTIAL PRESSURE INDICATOR
$ } M rINLET FILTER/SILENCER g
312. 4-
MOTOR JUNCTION BOX " :.'
-OTATION ARROW
0 ' u
BELT GUARD
BLOWER
(HF408 SHOWN)
_11 •IL LEVEL ' a
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AUTO BELT TENSIONER DISCHARGE IISCHARGE
PRESSURE GAUGE TEMPERATURE GAUGE
MOUNTING ISOLATORS At_—— —— —— — —_tA ::::: ,,..,..7.°4I -"7EZ3ri "a„"`
MEAT TREATMENT ra
/1,, THE MAXIMUM DIMENSION COULD BE 48.30 s ' ' °`ONMOM.0��E �� _ey G • F
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Quickpik.
Sutorbilt Legend - 4LDSL
Dear - --- .
:.--- :
Sincerely. , 1
Craig Bumess
Gardner Denver PHYSICAL
5491 Lucia Place
Weight ; 155 lbs.
Sarasota, FL 34238 - __,,... .Gear Diameter I , 4 in
Center Distance
Product Information ,
Connection Size 303d in I
CORRECTED VALUES ORIGINAL UNITS ENGLISH UNITS I METRIC UNITS ,- i
1
Case Length I 8 in
Ambient Pressure 14.696 PSIA 14.696 PSIA ' 1_013 bar a
WR:- 0.924 lb-
Elevation 0 ALTI-FT 0 ALTI-FT 0 altr-rn ff2-
net Pressure 14 696 PSIA 0 PSIG 0 bar a '
Orientation horizontal
__—
Inlet Pressure Loss I I 0.3 PSIG 0.300 PSIG ! 0 021 oar g PERFORMANCE
- i
-
inlet Temp 68 F 68°F I 20°C
i Ma k Delta P 7 PSI-
. , .,...... .
Inlet Flow 160 ICFM 160 ICFM 272 m3/h Max Temp 260'F
--,,--t-
Discharge Pressure i 6 PSIG I 6 000 PSIG 0.414 bar g I
Mw. Speed I 3600
RPM
Discnarge Pressure Loss 0 2 PSIG 0.200 PSIG 0 014 bar g
i
ME ASUNI I)VAt VI S ORIGINAL UNIT S L NGUSH UNIT S ME IRIC UNIT S Min SOCCa 055 RPM
PSIG
Speed 1433 RPM 1433 RPM 1433 RPM Max Case Pressure 25
Max Detta T 160"F
RPM 4.0 Or Ivta:= 40 40 40 1
- 1 Pov,er 7 5 HP 7 5 HP 5 593 kW
Discharae Tern 172°F 172"F 78'C
4 1
Temp%of Ma 66 66 66
Noise 79 79 dBa 79 dBa i 79 dBa
Pressure%of Max 93 93 93
,,... .4:
Adiabatic Efficiency 52.46% 52 46% 52.46%
Created 08-30-2022

VOL
. kpik-
GAS MIX:
100%
QUIC
'MEM A!r •
ENGLISH UNITS
kgikgmol
7,3 C 67
PARAMETERS
23 867 IDinilt11°1 - - 0,288 kJikg'K
r GAS
AMBIEN
53.522
1.200 kg/ma
moteRCuytaalluv:eight
Density 0 075fil.b.lbmffl:firns R
Performance Curves
_s se
t
Temperaturetm it Ri
ou
, ,
DEFINED-
ro104 F 5-:
1 -c
.alioRPM
3 500
•
300.-1
publish"Data
Defined
I
500
Conditions
i 0i,:li-'
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Flow
DEFINED CONDITIONS
IT ICIN
159 1CFM 600
400
RPM
pubtis 200
•:, .
Data
h"
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conditions
0
i oCii:
•
Created i 08_30_2022

Qu kpik
Performance Curves
Power
DEFINED CONDITIONS
7.5 HP
RPM
11111511M
Published Data
Defined
Conditions
Torque
DEFINED C ONDD ION 5
27.5 ft-lb
zo
RPM
IN= n
Pubhsfiecl Data
— Defined
Conditions
-10 -
1 000 20f. S0
Created: 08-30-2022

SPECIFICATIONS
DClCUK8ENTM102
axylem brand
YSU IQ SensorNet FDO*'
Optical Dissolved Oxygen Sensor
� The FD() isan optical, luminescent based O(} sensor for the
|(}SenoorNet system� During the biological nutrient removal
process at wastewater treatment plants, cooti uous �nd precis
e
measurement uf dissolved oxygen concentration isofvital
/ importance for optimal performance andtroub|e'fpea operation.
Efficiency and energy demand is mainly determined bythe
� performance of the aeration control system. The FD{} isa
/ reliable, proven, long-term Solution forcontinuous D{) data that
car) help optimize your process and lower- energy costs.
`
° Intelligent Sensor Cap
�
� The sensor cap is inclividua||y factory calibrated. Calibration
~
' data is stored ona chip that is embedded in the sensor cap.
PO008t9D� No need to enter ca|ibmdoncoe�ciemz. VVhona new cap ia
� instaUed.the coefficients are recognized and sent directly to
Uiou|vedUxy0eo(opdco|) the contrmUerterrnina| eliminating the need tomanueUyenter
Temye�tua information.
° Equal Path Reference System
The optical measurement and reference paths are identically
designed. This allows for identical aging nF the components
which enables accurate compensation and e|iminntns
calibrations. That's correct,there is no calibration required.
° Green Light Technology
~�-- 5mftec low-intensity excitation light increases the lifetime ofthe
The FDO',|o cap, This translates into a two year,warranty on the r,anJan]
energy
excitation technology
cap�
extends the sensor
cap lifetime.
.-
-' - - io
/
Learn More:
^ � Scan with o smart
06 � phone ortablet,
to
. � . .
006 angled sensor tip
o/m�uu�m�,»n
' Y�| /�y���
� pass by. ^ ^'"'�����' ' ��^�

IQ SensorNet FDO Optical Dissolved Oxygen General Specifications
Sensor Cap Replacement Yes;the cap,can be replaced.Automatic recognition by the sensor of the cap including the factory calibration.
Calibration Capability Yes;not required,factory calibrated
Interferences None
Minimum Flow Rate None;no flow requirement
Response Time at 25°C 70010 and 700 IQ SW-T90=<150 seconds;195=<200 seconds
701 IQ and 701 iQ SW-T90=<80 seconds
Signal Output Digital
Lightning Protection Yes
Power Consumption 0.7 watts
Maximum Pressure 10 bars(145 psi);with sensor connection cable
Electrical Connections 2-wire shield cable with quick sensor connection
Conformance/Certifications EN 61326,Class 8,FCC Class A;Intended for indispensable operation,CE,cETLus
Temperature Conditions Operating Temperature: 23 to 122`F(-5 to 50°C)
Storage Temperature: -13to122°F(-25to50"C)
Sensor Material: Housing-VA steel 1.4571;Sensor Cap and Locking Cap-POM(Poiyoxmethyiene),PUS,silicone,PMMA
Rating: IP-68;waterproof
Dimensions: 400 L x 40 D nvn(15.75 Ix 1.57 Din)
(length x diameter) 400 L x 59.5 D mm(15.75 Lx 2.34 D in)Salt Water version
Weight: 900 g(1.98 Ibs)
1,500 g(3.31 Ibs)Salt Water version
Warranty: 2 years
IQ SensorNet FDO Optical Dissolved Oxygen Technical Specifications
Dissolved Oxygen Range
Concentration Oto 20.00 mgil
Saturation 0 to 200.0%
Dissolved Oxygen Resolution
Concentration 0.01 mg?L
Saturation 0.1%
Temperature
Measurement 23 to 140°F(-5 to 60`C)
Compensation 32 to 140°F(0 to 60°C)
IQ SensorNet FDO Ordering Information (order 2020 XI terminal.modules,cables,sensors separately)
FDO 70010(#201 650Y) Optical DO sensor for monitoring and control;includes 1 factory calibrated sensor cap.
FDO 70010.SW(#201 652Y) Salt Water Design Optical DO sensor for monitoring and control;includes 1 factory calibrated sensor cap.
FDO 701 10(#201 660Y) Optical DO sensor for monitoring and control;faster response time;includes 1 fast response factory calibrated cap.
FDO 701 10 SW(#201 653Y) Salt Water Design Optical DO sensor for monitoring and control;faster response time;includes 1 fast response factory calibrated cap.
SC-FDO 700(#201 654Y) Replacement;universal factory calibrated sensor cap for FDO 70010 and FDO 70010 SW
SC-FDO 701(#201 655Y) Replacement;fast response factory calibrated sensor cap for FDO 701 10 and FDO 70110 SW
YSI
1725 Brannurn Lane,Yellow Springs,OH 45387
Tel[phone].897.4151 (US)
[e-mail] ••iiuom
YS I.co m •u.i•rii•
r_..
YSI and=DO are registered:trademarks. Y S
Specifications are subject to change.Please visit YSi.com to verify all specs. e
tw2012"Si
9 Printed in the USA.W102 May,2012 a xylem brand

■■iuumi SPECIFICATIONS
minsior
■.uuui■
;;;; •mil DOCUMENT#W1 1 8-02
YS1
YSI Digital SensoLyt® pH/ORP Sensor for the IQ Sensor-
a xylem brand Net System
The SensoLyt" is a rugged, online probe for measuring pH and
ORP concentrations using a combination electrode for the most
• accurate wastewater process monitoring.
The SensoLyt® probe is used within the IQ SensorNet system
and can therefore be networked with other probes and param-
eters for a complete process monitoring and control system. It
can measure and display pH or ORP.A built-in pre-amplifier and
temperature sensor with SensCheck function helps to monitor the
sensor.
The SensoLyt® is the ideal probe for quantitative measurement
of pH/ ORP in a wastewater treatment plant.Various SensoLyt'
electrodes(SEA/DWA/ECA/PtA) meet the needs of different ap-
plications.
Para meters:
• SensCheck function monitors sensors
pH
ORP • Electrodes are protected
• Electrodes can be removed and calibrated in the lab or in
the field
• Provides pre-amplification of the electrode signal
• Digital sensor stores calibration value
• Automatic temperature compensation
• Electrodes can easily be replaced without tools
• 2-year warranty on the probe, 6 months on electrodes
The SensoLyt'*sensor provides
continuous data to help with
operational improvement
;: decisions.

[e-mail]
From: Weaver, John C <[e-mail]>
Sent: Wednesday, August Au ust 31, 2022 3:42 PM
To: [e-mail]
Cc: Albertin, Klaus P;Weaver, John C
Subject: Fw: USGS response to DWR USGS Low Flows request# 2022-222 (dated 2022/08/23)
for Beaverdam Creek Union County...Re: [EXTERNAL] Low-flow request approval
Flag Status: Flagged
Mr. Brown,
Forwarded below is a response I just sent a few minutes ago concerning the low-flow request you recently
submitted for Beaverdam Creek. Somehow your email address was inadvertently incorrect, and I didn't catch
it before the email was sent.
Curtis Weaver
J. Curtis Weaver, Hydrologist, PE Email:[e-mail]
USGS South Atlantic Water Science Center Online:httns://www.usas.aov/centers/sa-water
North Carolina-South Carolina -Georgia
3916 Sunset Ridge Road
Raleigh, NC 27607
Phone: [phone] // Fax: [phone]
From: Weaver,John C<[e-mail]>
Sent: Wednesday,August 31, 2022 3:36 PM
To:[e-mail] <[e-mail]>; 'Matt Kirchner' <[e-mail]>
Cc: [e-mail]<[e-mail]>; Montebello, Michael J
<[e-mail]>; Dowden, Doug<[e-mail]>; Litzenberger, Kristin S
<[e-mail]>; Denard, Derek<[e-mail]>; Albertin, Klaus P
<[e-mail]>; 'Haley Hardin' <[e-mail]>; Weaver,John C<[e-mail]>
Subject: USGS response to DWR USGS Low Flows request#2022-222 (dated 2022/08/23)for Beaverdam Creek Union
County...Re: [EXTERNAL] Low-flow request approval
Mr. Brown and Mr. Kirchner,
In response to your inquiry about the low-flow characteristics for a location on Beaverdam Creek at NC Secondary Road
2139 (Griffith Road) near Monroe in southern central Union County,the following information is provided:
For the record: Initial location coordinates (34.9440460, -80.5682010) provided with the request submission placed the
point of interest on an unnamed tributary to Beaverdam Creek but with a different drainage area determined when the
low-flow request was initially pre-scoped. Via email correspondence dated 08/23/2022 with the requestor, the actual
point of interest was identified as being just upstream from another small unnamed tributary that enters Beaverdam
•

Creek also just upstream from Griffith Road. Correspondence with the requestor resulted in the final point of interest
being on the mainstem Beaverdam Creek where it crosses underneath NC Secondary Road 2139 (Griffith Road).
A check of the low-flow files here at the USGS South Atlantic Water Science Center (Raleigh office) does not
indicate a previous low-flow determination for the specific point of interest, identified by the fat/long
coordinates (34.94522, -80.55996) verified via email dated 08/23/2022 with the requestor following request
submission to the DWR USGS Low Flows portal.
No USGS discharge records are known to exist for the point of interest.
In the absence of site-specific discharge records sufficient for a low-flow analysis, estimates of low-flow characteristics at
ungaged locations are determined by assessing a range in the low-flow yields (expressed as flow per square
mile drainage area, or cfsm) at nearby index sites where estimates have previously been determined.
A basin delineation completed using the online USGS StreamStats application for North Carolina
(https://streamstats.usgs.gov/ss/) indicates the drainage area for the point of interest (StreamStats adjusted
coordinates 34.94502, -80.55976 NAD83) is 14.0 sqmi.
For streams in Union County, low-flow characteristics published by the USGS are provided in the following reports:
(1)The first is a statewide report completed in the early 1990's. It is USGS Water-Supply Paper 2403, "Low-flow
characteristics of streams in North Carolina" (Giese and Mason, 1993). An online version of the report is available
at http://pubs.usgs.gov/wsp/2403/report.pdf. The report provides the low-flow characteristics (based on data through
1988) via regional relations and at-site values for sites with drainage basins between 1 and 400 sqmi and not considered
or known to be affected by regulation and/or diversions.
(2)The second is a basin-wide report for the Rocky River basin published in 2003. It is USGS Water-Resources
Investigations Report 03-4147, "Low-Flow Characteristics and Profiles for the Rocky River in the Yadkin-Pee Dee River
Basin, North Carolina,through 2002" (Weaver and Fine, 2003). An online version of the report is available
through http://pubs.usgs.gov/wri/wri034147/. The report provides the low-flow characteristics (based on data through
2002)for continuous-record gaging stations and partial-record sites within the Rocky River basin. The report also
provides low-flow discharge profiles (7Q10, 30Q2, winter 7Q10, and 7Q2) for the Rocky River from its headwaters in
Mecklenburg County to its mouth.
(3)The third is a statewide report published in March 2015. It is USGS Scientific Investigations Report 2015-5001, "Low-
flow characteristics and flow-duration statistics for selected USGS continuous-record streamgaging stations in North
Carolina through 2012" (Weaver, 2015). The report is available online at http://pubs.usgs.gov/sir/2015/5001/. The
report provides updated low-flow characteristics and flow-duration statistics for 266 active (as of 2012 water year) and
discontinued streamgages across the state where a minimum of 10 climatic years discharge records were available for
flow analyses.
Low-flow characteristics estimated for point of interest:
Inspection of the above reports indicates the presence of nine (9) nearby selected USGS partial-record sites (8) and
continuous-record streamgages (1) across southern Union County in the general vicinity of the point of interest
where low-flow characteristics were published. Ranges for the low-flow yields among these 9 index sites are shown
below for the indicated flow statistics. Among these 9 index sites,the low-flow discharge yields for the indicated flow
statistics are as follows:
Annual 7Q10 low-flow yields ==>from 0 to 0.0055 cfsm (average about 0.00071 cfsm, median about 0 cfsm) (zero flow
at 7 of 9 index sites)
2

Annual 30Q2 low-flow yields =_>from 0 to 0.035 cfsm (average about 0.0079 cfsm, median about 0.0051
cfsm) (zero flow at 4 of 9 index sites)
Winter 7Q10 low-flow yields ==>from 0 to 0.016 cfsm (average about 0.0046 cfsm, median about 0.0018
cfsm) (zero flow at 4 of 9 index sites)
Annual 7Q2 low-flow yields ==>from 0 to 0.016 cfsm (average about 0.004 cfsm, median about 0 cfsm) (zero
flow at 5 of 9 index sites)
Average annual discharge yields ==>from 0.9 to 0.95 cfsm (average about 0.91 cfsm, median about 0.9 cfsm)
Application of the above range in yields to the drainage area (14.0 sqmi)for the point of interest results in the following
estimated low-flow discharges:
Annual 7010 low-flow discharges==>from 0 to 0.077 cfs (average about 0.0099 cfs, median about 0 cfs) 4 zero flow
Annual 30Q2 low-flow discharges ==>from 0 to 0.49 cfs (average about 0.11 cfs, median about 0.071
cfs) 4 use median value of 0.07 cfs
Winter 7Q10 low-flow discharges ==>from 0 to 0.22 cfs (average about 0.064 cfs, median about 0.025 cfs)
4 rounded down to zero flow
Annual 7Q2 low-flow discharges ==>from 0 to 0.22 cfs (average about 0.056 cfs, median about 0 cfs) 4 zero
flow
Average annual discharge discharges ==>from 12.6 to 13.3 cfs (average about 12.7 cfs, median about 12.6 cfs)
Please note:
(1)The estimated flows are provided in units of cubic feet per second (cfs).
(2)The low-flow yields provided above are rounded to 2 significant figures. Estimated low-flow discharges less than 1
cfs are rounded to 2 significant figures. If between 1 and 100 cfs,then rounded to 1 decimal place; if greater than 100,
then rounded to the nearest whole number(zero decimal places).
(3)The information provided in this message is based on a preliminary assessment and considered provisional, subject
to revision pending collection of future data and further analyses.
These provisional streamflow statistics are provided via the DWR USGS Low Flows cooperative agreement between
the USGS and the N.C. Department of Environmental Quality, Division of Water Resources.
Hope this information is helpful.
Thank you.
Curtis Weaver
J. Curtis Weaver, Hydrologist, PE Email:icweaverOusas.aov
USGS South Atlantic Water Science Center Online:httvs://www.usas.gov/centers/sa-water
North Carolina -South Carolina -Georgia
3916 Sunset Ridge Road
Raleigh, NC 27607
Phone: [phone] // Fax: [phone]
3

From: Albertin, Klaus P<[e-mail]>
Sent:Tuesday,August 23, 2022 10:45 AM
To:[e-mail] <[e-mail]>
Cc: Albertin, Klaus P<[e-mail]>; [e-mail]<[e-mail]>;
Weaver,John C<[e-mail]>; Montebello, Michael J <[e-mail]>; Dowden, Doug
<[e-mail]>; Litzenberger, Kristin S<[e-mail]>; Denard, Derek
<[e-mail]>
Subject: [EXTERNAL] Low-flow request approval
This email has been received from outside of DOI -Use caution before clicking on links, opening attachments, or
responding.
Your request has been approved and will be forwarded to USGS. A response from USGS usually takes 7 - 10 business
days.
Request Flow Statistic Approval
Request ID: 222
Requestor:Travis H. Brown
Requestor e-mail: [e-mail]
Requestor Phone: [phone]
Local Government:
Public Water Supply:
Consultant:
Contact:
Reason: Water Supply Water Availability/Safe Yield
River/Stream: Beavercreek damn WS-IV
Drainage Area (sq. mi.): 0.43
Latitude: 34.9440460
Longitude: 80.5682010
Other Information: Location is revised to a new location coordinates (34.94522,-80.55996) per the requestor. The new
point of interest is on the mainstem Beaverdam Creek(as opposed to the initial unnamed tributary)just upstream from
another small unnamed tributary. The analysis will use the location where Beaverdam Creek crosses underneath Griffith
Road (DA= 14 sqmi).
Statististics: ["7Q10","7010-Winter"]
4

Approved by: Albertin, Klaus P
5

Environmental Health
500 N. Main Street
Suite#47
Union County Monroe, NC28112
Government T. 704.283.3553
[e-mail]
LST. 1842 www.unioncountync.gov
Ben Russell
1214 Helms Shortcut Road
Monroe, N.C. 28112
September 12th, 2022
NOTICE OF IMPROVEMENT PERMIT/CONSTRUCTION AUTHORIZATION DENIAL
Property Location: 1214 Helms Shortcut Road (Cody Downs Lot# 39, 40, 49, 50, 51, 52,
53, 54, & 60)
Tax Code: 09-289-001
Property Owner: Ben Russell
Owner's Address: 1214 Helms Shortcut Road Monroe, N.C. 28112
The Union County Health Department, Environmental Health Division on August 2nd,2022 evaluated
the above reference property at the site designated on the plat/site plan that accompanied your improvement
permit application. According to your application the site is to serve a four bedroom home with a design
wastewater flow of 480 gallons per day. The evaluation was done in accordance with the laws and rules
governing wastewater systems in North Carolina General Statute 130-333 including related statues and Title
15A,Subchapter 18A,of the North Carolina Administrative Code, Rule.1900 and related rules.
Based on the criteria set out in Title 15A,Subchapter 18A,of the North Carolina Administrative Code, Rule
.1940 through .1948,the evaluation indicated that the site is UNSUITABLE for a sanitary system treatment and
disposal. Therefore,we must deny your request for an improvement permit. A copy of the site evaluation is
enclosed. The site is unsuitable based on the following:
❑ Unsuitable soil topography and/or landscape position (Rule.1940)
❑ Unsuitable soil characteristics(structure or clay mineralogy)(Rule.1941)
® Unsuitable soil wetness condition (Rule.1942)
® Unsuitable soil depth(Rule.1943)
CpU
!. �. .L
17-1
a w
,9ry ciA;••,`

❑ Presence of restrictive horizon (Rule.1944)
® Insufficient space for septic system and repair area(Rule.1945)
❑ Unsuitable for meeting required setbacks(Rule.1950)
❑ Other(Rule.1946)
These severe soil or site limitations could cause premature system failure, leading to the discharge of
untreated sewage on the ground surface, into surface waters,directly to ground water or inside your structure.
The site evaluation included consideration of possible site modifications,as well as use of modified,
innovative,or alternative systems. However,the Health Department has determined that none of the above
options will overcome the severe conditions on this site. A possible option might be a system designed to
dispose of sewage to another area of suitable soil or off-site to additional property.
For the reasons set out above,the property is currently classified UNSUITABLE, and no improvement permit
shall be issued for this in accordance with Rule.1948(c).
Note that a site classified as UNSUITABLE may be classified as PROVISIONALLY SUITABLE if written
documentation is provided that meets the requirements of Rule.1948(d). A copy of this rule is enclosed. You
may hire a consultant to assist you if you wish to try to develop a plan under which your site could be
reclassified as PROVISIONALLY SUITABLE.
You have the right to an information review of this decision. You may request an informal review by the soil
scientist or environmental health supervisor at the local health department. You may also request an informal
review by the North Carolina Department of Health and Human Services regional soil scientist. A request for
informal review must be made in writing to the local health department.
You also have the right to a formal appeal of this decision. To pursue a formal appeal,you must file a petition
for a contested case hearing with the Office of Administrative Hearings, 1711 New Hope Church Rd, Raleigh,
NC 27609. To get a copy of a petition form,you may write the Office of Administrative Hearings or call the
office at(919)431-3000 or from the OAH web site at http://www.ncoah.com/forms.html. The petition for a
contested case hearing must be filed in accordance with the provisions of North Carolina General Statutes
130A-24 and 150B-23 and all other applicable provisions of Chapter 150B. N.C.General Statute 130A-335(g)
provides that your hearing would be held in the county where your property is located.
Please note: If you wish to pursue a formal appeal,you must file the petition form with the Office of
Administrative Hearings WITHIN 30 DAYS OF THE DATE OF THIS LETTER. The date of this letter is September
12th,2022. Meeting the 30 day deadline is critical to your formal appeal.
If you file a petition for a contested case hearing with the Office of Administrative Hearings,
a � you are required by law(N.C. General Statue 150B-23)to serve a copy of your petition on
1 W I Q'
Page 2
H CpP:_

the Office of General Counsel, N.C. Department of Health and Human Services,2001 Mail Service Center,
Raleigh, N.C.27699-2001.
Do not serve the petition on your local health department. Sending a copy of your petition to the local health
department will not satisfy the legal requirement in N.C.General Statue 150E-23 that you send a copy to the
Office of General Counsel, N.C. Department of Health and Human Services.
If I may be of further assistance please feel free to call me at 704-283-3568 or
[e-mail].
Ty Yokeley
Registered Environmental Health Specialist
Signed: /c[ /31-e Date:09/12/2022
, 4.. 1842 o�),
J � t
<i
9 Page 3
yTj1 CAPO,

Environmental Health Sheet ( of 13
500 N.Main Street PROPERTY ID II: Del 20 91 00 I
COUNTY: lin Ism
Union County Suite#47
c.o rn rn p nt Monroe,NC 28112 SOIL/SITE EVALUATION
for ON-SITE WASTEWATER SYSTEM
(�n (Complete all fields in full)
J'OWNER: B( VSSt_I1 APPLICATION DATE 6/C1 f2`L
ADDRESS: IZl t4 F'ACIr•S S1.7“- -Cvi_ 12tra- DATE EVALUATED: g/Zh...Z
PROPOSED FACILITY: 5;F91L -fwr.,a►1 PROPOSED DESIGN FLOW(.1949): Li PQ 5 Pa PROPERTY SIZE: -1 5.4I (Crc,S
LOCATION OF SITE: 1119 HGIMS ShDQc v1 fLoaJ CCedt _owes bdSM ggyp/t1gt5o,5trS2,PROPERTY RECORDED: BIa414
WATER SUPPLY: 0 Private NI Public ❑Well ❑Spring 0 Other 53154/A 6 p) - t
EVALUATION METHOD: 0 Auger Boring TifPit 0 Cut TYPE OF WASTEWATER: ,Sewage 0 Industrial Process LiMixed
P
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SCAPE -
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STRUCTURE CONSISTENCE/ WETNESS/ SOIL SAPRO design &LTAR
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it &SLOPE DEPTH TEXTUREmottling,free (specify)
% (IN.) water,etc
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COMMENTS:
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500 N.Main Street PROPERTY ID II:
' U n i c t l G.(Ji e_i r1 t y Suite 1147 COUNTY:
G c,,r,e.rr r-s v-ri t r6 t ' oe,NC 28112 SOIL/SITE EVALU N
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OWNER: APPLICATION DATE
ADDRESS: DATE EVALUATED:
PROPOSED FACILITY: P OSED D GN FLOW(.1949): PROPERTY SIZE:
LOCATION OF SITE: PROPERTY RECORDED:
WATER SUPPLY: ❑Private ❑Publ. ❑Well ❑Spring ❑Ot
EVALUATION METHOD: ❑Aug oring ❑Pit ❑Cut TYPE OF�S4LTEWATER: ❑Sewage ❑Industrial Process ❑Mixed
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1

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(Coniimmtion Sheet-Complete ail field in full,) Sheet CI of 13
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PROPERTY ID#:
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(Continuation Sheet-Complete all field infull)
-
PROPERTY ID 9V:
WU A'X
•
o._ • .V . SOU., 1 P2HOLOyy OTHER -
(.1941) l'ROHJILE FACTORS'
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-- ` � , � .� A. ;OPEN SPACE:69`,�
Y - - 1.J`� _ \ 203,579 sq ft
_ ^\ -� ` _ 4.674 ac
•
` � r y �•� �4 L,\• , 23,373 sq f1
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r ,7 ;� _ _ _ -• - _ ` 0.531 ac 1 •'� ca 1J' •
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i•i 1� - ( ~�/` 083 sq R,-; / •• -.
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L LOT:36 'I, . /0.461 ac j, j - / $ �- _ �; rr
20,083 ft , { )�'
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f LOT:36 I 0.603 ac - - - -- ' T ='• { `'•
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0.935 ac - - r .,. - -

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/• _ • 23,340 sq fr f _ _ 24,630 sq ft `
j, .'; 0.536 ac ' ' 0.565 2c , - ,
\, _ 22,599 sq ft .
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f ""\ 0.493 ac
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n SITE PLAN(2 OF2) UNION COUNTY,NC
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LI FOR THE BENEFIT OF
CAROLINA DEVELOPMENT
AS WWI •4 q,1A, '•"'"';,,, SERVICES LLC

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"CODY DOWNS,sounr
RA-40 CLUSTER
AG E EUGINEERING
SITE PLAN(1 OF 2)
cn CITY OF MONROE,NC
-,° FOR THE BENEFIT OF: 2013411...m,ns
Nun MA IJC MN/
CAROLINA DEVELOPMENT
SERVICES LLC .

Ty Yokeley
From: Ty Yokeley
Sent: Monday, September 12, 2022 3:27 PM
To: '[e-mail]'; '[e-mail]'
Cc: Connie Adams
Subject: Applications
Attachments: Cody Downs 1ot49.png; Cody Downs Iot49 Application.pdf; Cody Downs_Soil_Site
Evaluation.pdf; NOTICE OF IMPROVEMENT PERMIT DENIAL (Ty Yokeley).pdf; 15a ncac
18a .1942.pdf; 15a ncac 18a .1943.pdf; 15a ncac 18a .1948.pdf; 15a ncac 18a 1945.pdf
Good afternoon,
Please review the attached documents and let me know if you have any questions.
For lot#49, I currently have a three bedroom septic system flagged off on the property. I have the GIS location attached
above as well. It shows the system running off the lot but the system is flagged off within the property boundaries and
meets the required setbacks in the field. If you would like to proceed with using this system please update the attached
application, sign, date, and scan back to me.
Thanks,
Ty Yokeley
Environmental Health Program Specialist, REHS I Environmental Health
T 704.283.3568
M 704.993.1613
[e-mail]
www.unioncountync.gov
UNION Union County Government
I:, COUNTY 500 North Main Street, Suite 47
north carotina Monroe, NC 28112
E-mail correspondence to and from this sender may be subject to the North Carolina
Public Records law and may be disclosed to third parties. If you are not the intended
recipient of this e-mail, please contact the sender immediately.
1

15A NCAC 18A.1948 SHE CLASSIFICATION
(a) Sites classified as SUTTABT,F,may be utilized for a ground absorption sewage treatment and disposal system consistent
with these Rules. A suitable classification generally indicates soil and site conditions favorable for the operationofagraund
absorption sewage treatment and disposal system or have slight limitations that are readily overcome by proper design and
installation.
(b) Sites classified as PROVISIONALLY SUITABLE may be utilized for a ground abs orption sewage treatment and disposal
system consistent with these Rules but have moderate limitations. Sites classified Provisionally Suitable require some
modifications and careful planning,design,and installation in order for a ground absorption sewage treatment and disposal
systemto function satisfactorily.
(c) Sites classified UNSUITABTF have severe limitations for the installation and use of a properly functioning ground
absorption sewage treatment and disposal system An improvement permit shall not be issued for a site whichis classed as
UNSUITABT P. However,where a site is UNSUITABLE,it may be reclassified PROVISIONALLY SUITABLE if a special
investigation indicates that a modified or alternative system can be installed in accordance with Rules.1956 or.1957 of this
Section.
(d) A site classified as UNSUITABLE may be used for aground absorption sewage treatment and disposalsystemspecificallyy -
identified in Rules .1955,.1956,or.1957 of this Section or a system approved under Rule .1969 if written documentation,
including engineering,hydrogeologic,geologic or soil studies,indicates to the local health department that the proposed
system can be expected to function satisfactorily. Such sites shall be reclassified as PROVISIONALLY SUITABIEifthelocal
health department determines that the substantiating data indicate that:
(1) a ground absorption system can be installed so that the effluent will be nonpathogenic,non-infectious,
non-toxic,and non-hazardous;
(2) the effluent will not contaminate groundwater or surface water,and
(3) the effluent will not be exposed on the ground surface or be discharged to surface waters where it could
come in contact with people,animals,or vectors.
The State shall review the substantiating data if requested by the local health department.
History Note: Authority G.S.130A-335(e);
Eff July 1,1982;
Amended Eff April 1,1993;January 1,1990.