WQ0033455_Engineering report calculations and product bulletins_20081119

WASTEWATER IRRIGATION
SYSTEM
CALCULATIONS ! PRODUCT
BULLETINS
PREPARED FOR:
THE CLIFFS COMMUNITIES
MR. DON NICKELL
3598 HIGHWAY 1 1
TRAVELERS REST, SOUTH CAROLINA 2969❑
ORIGINAL: OCTOBER 21, 2008
REVISED: NOVEMBER 1 9, 2008
®ROOKS ENGINEERING ASSOCIATES
PROJECT NO. 307808
17 Arlington Street
® Asheville, NC 28801
828.232.4700

1.1 Design Flow Table and Phasing Summary

BEA Project # 307808
The Cliffs at High Carolina
Design Flow Calculations
mase n
uzsvriwicaso_..--
141
81
31 1201
40,320 gpd
Site 8
site
8units
Phase Il
-
brl unit
flow/br
42
4 1201
20,160 d
Site 11
Phase it
Clubhouse Cottage SF
units
brl unit
flow/br
24
4 120
11,520 d
Site 12
Phase 11
SF Ridge Lots SF
unitsbr/unit
flow/br
40
4 120
19,200 g d
Site 14
Phase 11
I Village Lake Overlook
I Buildings I units
I brl unit
Iflow1br
_7t
4
31 1201
10,080 gpd
Prepared by: Matthew Rice Brooks Engineering Associates, PA 11/18/2008

1.2 VW/TP Head Calculations and Process Calculations &
Supporting Charts

PROCESS CALCULATIONS
The Cliffs at High Carolina
Aqueonics Treatment, Plant
I. PUMP HEADLOSS CALCULATIONS
A Equalization Tank
Average daily flow 100,000 gpd equalized at: 70 gpm for Phase I. Pumps to be replaced for
Phase II.
Total Dynamic Head ("TDH"):
Top of plant 100.00' Elev.
EQ Tank Floor (Pump Inlet) - 83.71_
16.29"
Inlet to head box + 3.00'
19.29' Static Head
Friction losses in pipe & fittings:
Fittings 1 - 2" — 90°ell
3 - 6" - 900ell
Pipe length = 16'- 2" 0
6'- 6110
Friction Loss/Ft. of Pipe
2" 0 loss =15.8'/100'
6110 loss= 0.1'/100'
Fitting loss in equivalent feet of pipe,
2" ell = 5.2'x 1 pc. =: 5.2'
6" ell = 15.3'x 3 pc. == 45.9'
Total frictional loss:
2" 0 = [16' + 5.2'] x 15.8/100 = 3.34'
6" 0 = [6'+ 45.9'] x 0.1/100 = 0.05'
Total Frictional Losses 3.39'
TDH = Static + frictional loss
Static
19.3'
Friction
+3.4'
Total
24.7'
Approximately 25'
TDH for pump sizing,
P. 1

B. Tower Pumps
Minimum Required Recirculation Flow Rate = 140 gpm.
Total Dynamic Head ("TDH"):
Static Head Losses:
(Phase I and Phase II)
Maximum Suction Head = 2.17' to top of slab
Maximum Lift = 20.50' to top of header
= 22.67' Total Static Head
Discharge Elevation 120.50' Elev.
Intake Elevation - 97.83'
22.67'
Friction losses in spray nozzle, pipe & fittings:
Distributor & Nozzle Headloss 5.00'
Fittings 2 - 4" — 90°ell
1 -4"—Tee
Pipe length — 28'- 4" o
Friction Loss/Ft. of Pipe = 4" o loss= 2.227100'
Fitting loss in equivalent feet of pipe,
4" ell = 10.2'x 2 pc. = 20.4'
4" Tee = 20.3 x 1 pc. = 20.3'
Total frictional loss:
4" 0 Pipe = 28 x 2.2'/100' = 0.616'
4" O Ell =20.4'x2.2/100' = 0.4488'
6" 0 Tee = 20.3' x 2.2/100 = 0.4466'
Nozzle & Header Loss = 5.00'
Total Frictional Losses 5.53 '
TDH = Static + frictional loss
Static 22.67'
Friction +5.531
Total 28.20'
Approximately 29' TDH for pump sizing
p. 2

Blowers No 2 & 3 (duplicate and backup for No. 11
'- Sludge Mixing & Digestion = 86 cfrn @ 7 psi
Sludge Thickening =10 cfin @ 7 psi
Floculation = 10 cfm @ 7 psi
Required = 107 cfin @ 7 psi
1.. Provided = 112 cfin @ 7 psi
B Primary Treatment
Raw influent = 350 mg/1 BOD, 60 mg/1 N
Removal in primary clarifier = 30% BOD, 20% N
Influent to aerobic Tower I =
0.7 x 350 = 245 mg/l BOD
0.8 x 60 = 48 mg/1 NH3-N
C Stap-e I (aerobic tower) -- BOD and Ammonia Reduction
Use minimum water effluent temperature = 13 degrees C
Forward flow through plant = 70 gpm
Surface area of tower = 12'x 12'= 144 ft2,
Application Rate = 70/144 or 0.486 gpm per square foot
Determination of the BOD removal fraction is performed, using B.F. Goodrich Information
Bulletin VC -5.0-477-1, by application of the Schultze Equation:
KOD
Qv2
Where Le is the effluent BOD
Lo is the influent BOD
K is the treatability factor, 0.07 for domestic sewage
0 is the thermal factor, 0.78 at 13 degrees C
D is the height of the column in feet, 20 feet
Q is the raw flow distributed on the top surface of the filter.
p. 4

II. WWTP PROCESS CALCULATIONS
A Sludge Processing
Influent = 100,000 gpd @ 350 mg/l BOD, = 2921bs/day of BOD.
Process Sludge Production
0 0.15 lb/lb x 2921b/day = 44 lbs/day at 4-1/2% solids.
o Gallons per day = 44 lbs/day/(8.34 lb/gal x .045) = 115 gallons/day.
Primary Tank Sludge Production
o Suspended solids = 210 lbs/day.
0 60% removed in primary clarification as primary sludge.
o Primary Sludge = 0.60 x 2101b/day = 126 lbs/day at 2.5%
o Sludge volume = 126 lb/day/(8.34 gal/lb x.025) = 606 gallons per day of primary sludge.
Total sludge Production
o Daily sludge production= 606 gal. + 115 gal.= 721 gpd
Aerobic Sludge Processing
o Sludge stabilized under aeration = 15 days,
o Concentrated in the sludge conditioning chamber yield = 7-1/2% solids
o Production of sludge for off-site disposal = 350 gallons per day
o Sludge Storage Days Available = 21,263 gallons/350 gpd = 60 days.
Air Requirements
Mixing Air Required = 3 cfm/If x 261f of chamber = 78 cfm
Aerobic Digestion = Oxygen requirements, = 30 cfm per 1,000 cubic feet of tank. 21,263
gallons /7.48 gal/cu.ft. = 2,843 cu.ft.
2,843/1000 = 2.843 thousand cu. ft. of tank
2.84 x 30 cfm = 86 cfm.
SPECIFIC BLOWER REQUIREMENTS
Blower No 1— Flow Equalization & Intermittent Airlift
Flow Equalization = 78 cfm @ max 7 psi
Airlift Pumps (2 max at a time) = 30 cfin @ 7 psi
Required = 108 cfm @ max 7 psi
Provided = 112 cfm @ 7 psi
p. 3

From this Table we see a 79% removal of BOD per stage in Phase I is accomplished.
BOD of effluent of Tower I =.21 x 245 = 51.45 mg/l.
Nitrification in Tower I
Minimal nitrification will occur because of the presence of a large BOD concentration
(loading) of the tower. Heterotrophic bacteria are a dominant species in comparison to
the autotrophic nitrifiers, and their rapid growth will inhibit the nitrification process. To
determine the degree of inhibition we must first compute the biological BOD loading.
The biological loading is:
= 245 g/106 g x 100,000 gal/day x 8.34 lbs/gal = 204 lbs/day.
There are 12'x 12'x 20'= 2880, cubic feet of media in the tower. Therefore the loading is
204/2.88 = 70.94 lbs/day/1000 W. This figure is important for computing the conversion of
Ammonia -Nitrogen to Nitrate -Nitrogen in each aerobic tower, since presence of BOD interferes
with the Nitrification efficiency as shown in Process Design Manual for Nitrogen Control. U.S.
EPA Technology Transfer. October 1975. (See Attached Figures from this publication and
BFGoodrich Information Bulletin VC -5.0-477-1).
Ammonia conversion to nitrate is obtained by first using Figure 4-15 (from the above reference)
which applies for minimal interference from BOD. Using the curve for 13 to 19° C, we see that
for ammonia -nitrogen concentrations above 2.5 mg/1, 3,800 ft2 of surface area is required for
conversion of one pound of ammonia -nitrogen to one pound of nitrate -nitrogen.
Theoretically, if we have 30 ft2 of surface area per cubic foot of media, we would have:
2880 ft3 x 30 ft2/ft3
3,800 ft2/lb converted/day (from Figure 4-15)
= 22.73 lbs/day of NH3-N removed if BOD were not also present in the influent
Because there is BOD present, the most conservative value for nitrification is 0%.
Therefore, a conservative view would credit no nitrification in Tower I, which we assume for
purposes of this computation. Actual conversion of ammonia -nitrogen to nitrate -nitrogen in
Stage I does occur from our experience when other than the most conservative data are selected,
otherwise use of the first anaerobic reactor would be moot. We plan to further enhance the role
of Anaerobic I by the recycling of fully nitrified liquor to tower I for enhancement of nitrification
capacity. Stage I influent nitrogen = 48 x 10-6 x 8.34 x 100,000 = 40.0 lbs/day
Effluent from Stageic treatment will be:
BOD = 51.45 mg/l or 42.9 lbs/day
Ammonia -nitrogen = 48 mg/1 or 40.0 lbs/day
Nitrate -nitrogen = 0 (worst case)
7
p. 5

Removal of nitrate -nitrogen in the subsequent anaerobic reactor is nearly complete, since
concentrations of BOD and bacteria are high; but we assume conservatively that no
further oxidation of BOD or ammonia -nitrogen occurs in any of the anaerobic reactors.
D Stage II - BOD Reduction (Iteration 1— no recycle)
Influent BOD = 51.45 mg/l BOD -- 42.9 lbs/day
= 48 mg/l ammonia -nitrogen or 40.0 lbs/day
BOD reduction = 0.21 x 51.45 = 10.8 mg/l in the effluent (Using Methods as per
Stage I & B.F. Goodrich Information Bulletin VC -5.0-477-1)
The presence of BOD that survives the aerobic process is essential to the final
denitrification process in anaerobic reactor III, and is an essential feature of the
Aqueonics process. That is a key reason in the Aqueonics process for use of fixed film,
as it places a limit on polishing of BOD through surface and contact time limitations.
Nitrification in Tower II
The desired ammonia effluent is 2.0 mg/l or more in this stage . Using 4-159 3,800 ft2 of
surface is required per pound nitrified per day. As in the calculation for Stage I, the BOD
loading is found to be 42.9/2.88 = 14.91bs/day/1000 ft2. From Figure 4-7 the most
conservative nitrification efficiency is 41%.
We find conversion o£ 2880 ft3 x 68 ft2/ft3 x 0.41 / 3,800 ft2/lb converted
= 21.1 lbs/day converted
Discharge from Aerobic II will therefore be:
BOD =10.8 mg/1, = 9.0 lbs/day
Ammonia -nitrogen = 481bs/d — 21.1 = 26.9 lbs/day
Nitrate -nitrogen = 21.1 lbs/day
The nitrate is consumed in the second anaerobic reactor (see anaerobic denitrification
discussion below)
E Stage III• (Iteration I — no recycle)
With minimal influent BOD, there will be no inhibition of the nitrification process by the
presence of BOD.
Tower III contains 2880 ft3 of media which has a total of 195,840 ft2 of surface area
(2880ft2 x 68 ft2/ft3).
p.
6

`J
Since 26.4 lbs. of ammonia -nitrogen remain, we have available 7418 ft2 per lb. of influent
ammonia (19584W/ 26.41b). On first iteration, therefore, Figure 4-15 tells us that
approximately 1.5mg/l effluent ammonia concentration could be predicted, which is more
than the 1.0 mg/1 goal and indicates that recycle must be employed to achieve the goal .
Since the conversion from nitrite to nitrate is highly efficient and immediate because of
the action of nitrobacter, the presence of nitrite in effluent is not observed.
F Stage II; (Iteration 2 - recycle.)
By recycling flow from Aerobic stage III to the suction of stage I, the removal of BOD in
stage I is unaffected, since raw flow distribution does not change. In going to stage 2,
however, the composition of flow will be a mass balance betweeen stage I effluent and
recycle flow:
56.45 mg/l x 70 gpm + 2.27 mg/l x 74 gpm = 26.17 mg/1 x 144 gpm
26.17 mg/1 x 8.34 x.144 MGD = 31.43 #/d of BOD, or 10.92 lb/d/1000 cult.
Referring to figure 4-7 the removal efficiency for ammonia is 52%, and so the Tower II
discharge is:
2880 cu ft x 68 sq ft/cu. ft. x .52 / 3800 sf/lb = 26.8 lbs of ammonia removed.
BOD removal will be 67%, from information bulletin VC -5.0-477-1 based upon a raw flow rate
of 1.0 gpm/sq. ft., resulting in a discharge concentration of .33 x 26.17 = 8.63 mg/l
Tower II discharge
BOD = 8.63 mg/l, 10.361bs/day
Ammonia -N = 22.31 mg/l, or 21.2 lbs/day
Nitrate -N = 22.3 mg/1, or 26.81bs/day
G Stage III; (Iteration 2 recycle)
As in iteration 1, the ammonia discharge from Tower III will be minimally interfered with by
BOD concentration, and the slightly increased concentration of BOD will actually assist in the
Nitrate removal in Anaerobic III. The recycle has had the effect of removal of additional
ammonia, and reduction of the load on Tower III.
We now have a loading of 21.2 lb/day on 195,840 sf of media surface, or 9,237 sf /lb/day, which,
from Figure 4-15 will produce the desired 1.0 mg/l effluent.
Tower III discharge of BOD and ammonia will therefore be:
BOD < 8.63 x 0.33 = 2.8 mg/l, = 2.3 lbs/day
Ammonia -nitrogen < 1.0 mg/l, = 0.83 lbs/day
Nitrate -nitrogen = 22.3 -1.0 = 21.3 mg/1= 17.8 lbs/day
p. 7

In the third anoxic reactor, the nitrate is consumed by facultative bacteria. Both BOD residue
and nitrate are so low as to provide inefficient contact conversion. The same effect is noted in
Figure 4-15 for the nitrification process. To assist in the removal of nitrate in the relative
absence of BOD present, recycle capability has been made to return up to full flow of fully
nitrified liquor to the first anaerobic reactor, where significant BOD is present. This is done by
the now splitter/overflow weir located between Tower III and Anaerobic III. These facilities are
controlled by valving that allows the operator to control the amount of recycle coming from
Tower III, compared to that coming from Tower I. Submerged weirs in Anaerobic I and II, and
a surface weir in the Primary clarifier allows for gravity retrograde flow from the secondary
flow splitter to the suction of the Tower I recirculation pump.
Anticipated discharge from Anaerobic III will therefore be:
BOD < 2.3 mg/1, = 1.9 lbs/day
Ammonia Nitrogen < 1 mg/1= 0.83 lbs/day
Nitrite Nitrogen = 0 mg/1 = 0 lbs/day
Nitrate Nitrogen < 3 mg/l = 2.5 lbs/day
H. Anaerobic Calculations
The "anaerobic" reactors achieve three functions. First, as a tube settler for solids removal,
second, to create an anoxic environment to accomplish denitrification utilizing sewage as the
organic carbon source and, third, to achieve partial "anaerobic" digestion of biomass.
Each of the "anaerobic" reactors contain plastic media having a surface area of 30 ft2/ft3 placed
atop precast concrete hoppers on fiberglass beams within the tankage. Influent enters each
"anaerobic" unit beneath the media and flows in a serpentine fashion through the media. A
hydraulic retention time of 2 hours is maintained in contact with the media for completion of the
anoxic denitrification reaction. A surface overflow rate of 879 gpd /ft2 or less and presence of
the media makes these reactors extremely efficient clarifiers in addition to their primary function
in biological denitrification.
Denitrification conversion efficiency is limited only by minimal concentration of the nitrate
substrate with which the colonies of facultative anaerobe denitrifiers can be maintained. An
effluent consistently less than 3 mg/1 nitrate -nitrogen has been achieved in similar facilities
The process of anoxic denitrification is confirmed by EPA design data. (Process Design Manual
for Nitrogen Control. U.S. EPA Technology Transfer. October, 1975.)
Figure 5-13 shows that submerged high -porosity media reactors remove, at 13° C,
approximately 600 pounds N/1,000 ft3/day.
Aqueonics process removal efficiency with plastic media is calculated on a surface area per
cubic foot basis is the same as the EPA reference system that uses sand particles. Detail
calculations are available upon request.
The rate of removal is proportional to biomass contact (the reaction area), and 600 lb N/1,000
ft3/day has been shown to be removed in the fluidized bed. The proportionate plastic media
removal rate
a p. 8

Volume Denitrification Rate (fixed media)
= 0.116 x 600 (conversion factor to convert EPA's fluidized sand
bed reactor to a fix media reactor)
= 69.6 lbs /N /1,000 ft3/day of fixed media
= 0.0696 lbs N per ft3 of fixed -film media/day
= 0.069 lbs N /ft3 media using 30 ft2/ft3 media
= .00232 lbs N /ft2 media/day
In the present design, each anaerobic reactor has sufficient media to provide at least 2 hours of
detention time. Thus, we have a design capacity in each reactor of 0.33 ft2 or more of surface per
gpd, which is the nitrogen removal capacity of 0.002321bs N/ft2/day x .33 ft2/gpd = .00076 lbs
N per gallon per day.
However, the influent N concentration, at 60 mg/1, contains 0.0005 lbs of N per gallon (8.34
lb/gallon x 70.4 x 10-6 = .0005 lbs N per gallon). More than sufficient denitrification capacity
exists within each reactor to complete the process: ie, there is no process limitation anticipated as
a result of available surface area.
In order to take full advantage of the BOD present in Anaerobic I, it is advantageous to provide
for the recirculation of fully nitrified flow from Aerobic No. 3 to Anaerobic No. 1 to reduce the
BOD requirements of Anaerobic No. 3 by denitrifying the recycle sidestream. This function is
particularly useful where the aerobic portion provides excessive BOD consumption in the final
stages. The recycle sidestream is variable, and controllable up to a flow of R = (144 — Q) gpm,
where Q is the raw forward flow through the plant.
Operational control is required to retain sufficient retention time in the anoxic reactors I and II
when using recycle to assure completion of the anoxic reaction. Under conditions where R + Q
exceeds 70 gpm, retention time would be reduced to less than 2 hours, the nominal design
retention time. Above this flow, the operator must monitor the completion of the anoxic
reactions in Anaerobic I and II after making a change in recycle flow.
P. 9

FIGURE 4-7
EFFECT OF ORGANIC LOAD ON NITRIFICATION- EFFICIENCY
EFFECT OF ORGANIC °I OAD ON IIT IFI ATIMEFFICIENCY
OF Rf Y, TRICKLING FILTER
t
W
U.
tL
Lu
t
rx
Z
0
E
. Po 30 40 50
BOD5 LAD -- L B 1000 CU F7` DA
n

VC - 5.0-477-1 BFGoodrich Information Bulletin
a
9
OPGoodrich
General Products Division
DESIGN CALCULATION RESULTS
TREATABILITY FACTOR K20 =0.07
Influent Waste Temperature —' 0qC
a M A NVIAWIL Nk a
INFORMAR WN
BULLETIN
Akron, Ohio 44318
DevoftmOnl 041A, WH8-3
VINYL CORE"'
,Influent Waste Temperature — 13'0 C
%
BOD
ReMOVOCI
Media DepthExpressedT'I'31''IM)
media Depth
Flaw F12,w
Raw F
Expressed T6GPM/ft-' of Tower Surface Area
Feet
Feet
0.3
0.5
0..
U
0,a
0.9
10,
1.1
1,2
1.3
1.4
1.5
12
66,
57
54.
51
49
47,
45
43
42
41
40
39
1472
77
63
67
...69
r64,
56
61
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52
50
48
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46
50
44
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43
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16
1'8
80
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tid
61- 59 57
56;----94--63
55
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20
84
75
72
69
67
67
(3,5
' 61
60
58
57
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2-2
86
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16
63
62
60
59
59
89
81
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--7-674
76
72
70
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56
-65
63
62
24
24
91
92
84
86
81
83
79
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76
79
74
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72
75
71
73
69
72
68 -65
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- 9
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28
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93
---9-46-9-87
88
85
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—80
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f6----77
74
73
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72
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—94
34
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89
87
85
83
81
80
79
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88
—!�6-
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go
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go
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-40-96
89
94
92
, 91
—
89
88
86 �
85
84
82
81
80
,Influent Waste Temperature — 13'0 C
Hemovea
Media DepthExpressedT'I'31''IM)
Flaw F12,w
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f7-9u—r—faceArea
0
Feet
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83

FIGURE 4-15 SURFACE AREA REQUIRED FOR NITRIFICATION
FIGURE', 4-15
WRFACE AREA REOUIREMENTS FOR IIT RIFICA110N -
MIDLAND MICHIGAN
qj000
CA
Iq
4j
k.
to
w
�13 127000
N
W
0
Itiffuent DoM (moun)
ss 1� /I
Orgonic ,N I - 4 mg/l
N H4 N 8 - 418 ms./l
/ /TKt4 Id
7 to 11 C
113 1019C
Key
7 to, 11
0 T 13 10 19 C
Lo 4, o 4,0
CFFLUENr AMMOWA-N. mg/l
4-64
5-0 6:0
Q
10
0
Itiffuent DoM (moun)
ss 1� /I
Orgonic ,N I - 4 mg/l
N H4 N 8 - 418 ms./l
/ /TKt4 Id
7 to 11 C
113 1019C
Key
7 to, 11
0 T 13 10 19 C
Lo 4, o 4,0
CFFLUENr AMMOWA-N. mg/l
4-64
5-0 6:0

FIGURE 5-12 VOLUME DENITRIFICATION RATE
11
2000
40
r
61)
FIGURE, 5- 13
VOLUME DENITRIFICATION RATE FOR SUBMERGED
jfjCjH POROSITY FINE MEDIA COLUMNS (REFERENCE 39)
l.f

1.3 - Pump Curve for Irrigation Dose Pumps and Pump Curve
for Pumps in Series
6d
mad
4w

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

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46 60
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0
WAT 7702766535 #439 Page 11/12
LC - 20953 Configured Curve
r 0 so 100 150 200 260 300 350 400 450 Soo 550 600 650 700
" I Capacity - USgpm
A,, 9.60 in Max
i..._.......__....
..... ..... .
.......
F.EE . .
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.
.........
. ......... . ........ . . ..... . . .......
. .................--_.t.__..,
)H:
350 ft
Tamp: 68.00 dog F
r 0 so 100 150 200 260 300 350 400 450 Soo 550 600 650 700
" I Capacity - USgpm
A,, 9.60 in Max
100
-90
80
,70
60
50
40
30
20
10
A
V
SD 100 1501 200 250 300 350 400 450 500 S50 600 650 700
40 Capacity - usgpm
'+U
p ,20
n.�
7:77 -
-A............_.
.....
.......... . .
- - - --------- ........ ............ . _........................_,
.........
9.S4 In Rated.
. .................--_.t.__..,
)H:
350 ft
Tamp: 68.00 dog F
Dis. Press:
*utoff Head:
........ .. .... ... .
S.C., 0.998
Diff. Press:
NPSHr
-------------
. ........... . . . ...... .
BHP- 303 hp
ip. Dia.,
9.54 In
Pump Eff.: 58.16
Efficiency
P% Of Stages,
I
IBEP: 426 USgpm_
Motor Data,
40
Voltage: 208-230/460
Eff;
Aiminal RPM:
----------
Phase: Three phase
. . ... . .......
dual RPM,
3500
Hz, 60
End,: ODP
......-----------
100
-90
80
,70
60
50
40
30
20
10
A
V
SD 100 1501 200 250 300 350 400 450 500 S50 600 650 700
40 Capacity - usgpm
'+U
p ,20
n.�
100 ISO 200 250 300 350 400 450 500 550 600 650 700
capaefty - Usgpm
Air
7:77 -
I . . ..I.. . ' .. ' .1. . . . . ..
I .
• Design Datai.,..,.".`
. I.-: : :;.. . . . ..'
.......... . .
- - - --------- ........ ............ . _........................_,
. .. . ............ ....... .......
Fluid: Water
Suct Press: 0.00_psi.a
)H:
100 ISO 200 250 300 350 400 450 500 550 600 650 700
capaefty - Usgpm
Air
7:77 -
I . . ..I.. . ' .. ' .1. . . . . ..
I .
• Design Datai.,..,.".`
. I.-: : :;.. . . . ..'
0
50
Fluid: Water
Suct Press: 0.00_psi.a
)H:
350 ft
Tamp: 68.00 dog F
Dis. Press:
100 ISO 200 250 300 350 400 450 500 550 600 650 700
capaefty - Usgpm
Air
7:77 -
I . . ..I.. . ' .. ' .1. . . . . ..
I .
• Design Datai.,..,.".`
. I.-: : :;.. . . . ..'
Qpw;
200 USqpm
Fluid: Water
Suct Press: 0.00_psi.a
)H:
350 ft
Tamp: 68.00 dog F
Dis. Press:
*utoff Head:
363 ft
S.C., 0.998
Diff. Press:
NPSHr
7.04 ft
Viso.: 1.00 op
BHP- 303 hp
ip. Dia.,
9.54 In
Pump Eff.: 58.16
P% Of Stages,
I
IBEP: 426 USgpm_
Motor Data,
40
Voltage: 208-230/460
Eff;
Aiminal RPM:
3500
Phase: Three phase
S.F.; 1.15
dual RPM,
3500
Hz, 60
End,: ODP

'0/1,6/2008 12:21pm WWSI
,ied:
R
r i
0
7702766535 #439 Page 12/12
MOTOR DRIVE
B'->, TP MS
Nominal RPM 3600 Eased on hreshr-Waterff-6B-dt q.., F
rr-r)perrei Dicrnetur; 6-3fT6"fTCT }`
50 75 100 125 150 1
CAPACITY IN U.S•. GA]A.014C5 PER MINUTE
25 250 275 3C
7,5
70 Z
�W
W
UU
65 U_(
W
60
LL'
W
10.0
U�
J_
QTJOTED -.BY--
TAS
.BY-TAS
Q UOTED Ta.
brooks job cliffs
SELECi',10W
CO'L` DI'TTOWi S'
Flow:
200.0 GPM
Priming Type;
Standard,
Total Dynamic Head:
140.0 feet
I*ottor Loading:
Stand"a rd
PUMP DESCRIPTION
Pump Model:
82TPMS
Priming Type:
Standard
Impeller Diameter:
6.188 in,
I•m•p-el-lar Material:
Iron
Suction:
2i/2"NPT
Discharge-
2"NPT
Shaft Seal:
Mechanicar
PUMP PERFaR2rfMANCR
Flow:
200.0 GPM
Po.wer._
Total Dynamic Head:
1 40. 6 feet
EffiePe-ncy-
73:4 -
Nominal Speed:
3600 RPM
NPSHR:
'14..2 feet
Shut -Off Head:
154.3 feet
Max Power:
T'T.O BH'P
Best Eff: 73.7 (99� 21.4.Gr Gt'1,4
MOTOR
Size:
10 HP
Enclosure:
TEFL
Voltage.: Corieull Catcrlog/Facto•ry
PRICE/ORDER
INFORMATION
Catalnc� No..,
Factory
Weigh L;
200 lbs.
QTJOTED -.BY--
TAS
.BY-TAS
Q UOTED Ta.
brooks job cliffs

1.4 Pump Curve and TDH Calculations for Return Pumps

BUNCOMBE COUNTY, NC THE CLIFFS AT HIGH CAROLINA PROJECT #307808
TDH = AH + hm
where:
AH = elevation head
hn, = major pipe losses, utilize Hazen Williams equation with equivalent lengths for fittings
hm = (4.727 U d4'87) (Q/C)1.85 where: Q in cfs, L in feet, d in ft.
" i { , no user input
1 user input req'd
Piping:
in,
g.
Diameter =�p inches (nominal) equals 2.047 inches (ID)
0.1705833 ft.
q
Q (gpm)
hm (feet)
TDH
PSI
Velocity
5
173.001
0.34
173.34
75.0
0.51
10
173.001
1.24
174.24
75.4
1.02
15
173.001
2.63
175.63
76.0
1.53
20
173.001
4.48
177.48
76.8
2.04
22
173.00
5.35
178.35
77.2
2.25
25
173.00
6.78
179.78
77.8
2.55
30
173.00
9.50
182.50
79.0
3.07
35
173.00
12.64
185.64
80.4
3.58
40
173.00
16.19
189.19
81.9
4.09
45
173.001
20.14
193.14
83.6
1 4.60
50
173.00
24.47
197.471
85.5
1 5.11
Brooks Engineering Associates, PA P. 1 of 1 10/21/2008

Part Number
H P
Voltage
Phase Amps
Stages
J
5030-0005
112
115
1 12.0
6
22-3/8"
5030-0006
112
230
J
6
10 GPM Models
5030-0007
19 GPM Models
115
R li
8
24-1/8"
5030-0008
1/2
230
1 6.0
8
24.1/8°
5030-0009
3/4
230
PUMP PERFORMANCE CURVE
12
28-7/8"
w
w
LL
PUMP PERFORMANCE CURVE
66
266
48
160
w
10 GPM
"0
140 1HP- 4STAGE
19 GPM
I sn _p ;t.J e° -y
40-
64
1114" NPT DISCHARGE
Q
2
120
11/" NPT DISCHARGE
32
3l4HP•35TAGE
;T
120
400
1 1
100
280
1 HP-9STAG E
2460
112
314 HP• 12 STALE
126
80
32
100
16
2d
60
104
360
60
72
240
314 HP —
t6
20
6
46
20
0
I I
i i I
96
320
10 20 30 40 s0 60
6
7 STAGE
GALLONS
LITERSl'
G11
-CNS
6 0 100 X40
0 40 80 120 160 200
UTEas
20 d6 66
FLOWPERMINUTE 015045
64
200
280
56
'. ..,.
S 80
112 HP- 8 STAGE
�
= 72
240-46
160
U
s4
200
40
1/2 HP
56
112 HP- 6 STAGE
120
5 STAGE
0 4s
160
32
40
0 24
80
Awl
120-
o
32
16-
24-
60
B
40
40
0
+.
s
I
5 10 15 20 25 30
2
4 6 8 10 12 14 1s is
GALLONS
LITERS
I—�--�—r—
GALLONS
0
20 40 60 80 100
uTFRs 0
e 16 24 32 40 48 ss 64
FLOW PER MINUTE
FLOW PER MINUTE
I;.....'.
015413
015414
Part Number
H P
Voltage
Phase Amps
Stages
Height
5030-0005
112
115
1 12.0
6
22-3/8"
5030-0006
112
230
1 6.0
6
22-318"
5030-0007
1/2
115
1 120
8
24-1/8"
5030-0008
1/2
230
1 6.0
8
24.1/8°
5030-0009
3/4
230
1 8.0
12
28-7/8"
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5031-0005
112
115
1
12.0
5
21-15116"
5031-0006
1/2
230
1
6.0
5
21-15/16"
5031-0007
314
230
1
8.0
7
25-1116°
5031-0008
1
230
1
9.8
9
28-118"
L
Part Number
H P
Voltage
'1
Stages
27 GPM Models '�� %i1 l
5032-0005
35 GPM Models
115
1 12.0
PUMP PERZORMMCECURVE s
21-1/8"
LL PUMP PERFORMANCE CURVE
112
230
11/4* NPT DISCHARGE t%4 -a2-
4
35 GPM
17
,6_320
11/2 HP- 106TAGE
1 8.0
2" NPT DISCHARGE
24.5116"
5032-0008
300
ss
160
7
se
5032-0009
1-1/2
1-12 HP- 5 STAGE
1 13.1
10
260
66
266
48
160
,rc
7Y
"0
140 1HP- 4STAGE
I sn _p ;t.J e° -y
40-
64
RIH
200 pp F
20D.
Q
2
120
32
3l4HP•35TAGE
60�
100
2460
V2 HP-2STAGE
126
60
32
100
16
2d
60
40
60
8
t6
20
6
46
20
0
I I
i i I
10 20 30 40 s0 60
6
5 1b is t6 zs 30 is da
GALLONS
LITERSl'
G11
-CNS
6 0 100 X40
0 40 80 120 160 200
UTEas
20 d6 66
FLOWPERMINUTE 015045
FLOW PER MINUTE 015044
I
L
Part Number
H P
Voltage
Phase Amps
Stages
Height
5032-0005
112
115
1 12.0
4
21-1/8"
5032-0006
112
230
1 6.0
4
21-118°
5032-0007
314
230
1 8.0
6
24.5116"
5032-0008
1
230
1 9.8
7
26-7/16°
5032-0009
1-1/2
230
1 13.1
10
31-7/8"
Part Number
H P
Voltage
Phase Amps
Stages
Height
5033-0005
112
115
1 120
2
19-7/16"
5033-0006
112
230
1 6.0
2
19-7116°
5033-0007
314
230
1 8.0
3
22-3116`
5033-0008
1
230
1 9.8
4
24-15116"
5033-0009
1-1/2
230
1 13.1
5
29-15116"
r:
© Copyright 2007 Zoeller Co. All rights reserved.

BUNCOMBE COUNTY, NC
THE CLIFFS AT HIGH CAROLINA
TDH = LH + hm
where:
4H = elevation head
h,,, = major pipe losses, utilize Hazen Williams equation with equivalent lengths for fittings
hm = (4.727 U d4.87) (Q/C)1.85 where: Q in cfs, L in feet, d in ft.
no user input
'US
er input req'd
Piping: �
Diameter equals 2.047 inches (ID)
0.1705833 ft.
PROJECT #307808
Q (gpm)
H
hm (feet)
TDH
PSI
Velocity
5
175.001
2.10
177.10
76.7
0.51
10
175.001
7.59
182.59
79.0
1.02
15
175.001
16.09
191.09
82.7
1.53
20
175.00
27.41
202.41
87.6
2.04
24
175.00
38.42
2.13.42
92.4
2.45
25
175.00
41.44
216.44
93.7
2.55
30
175.00
58.09
233.09
100.9
3.07
35
175.00
77.28
252.28
109.2
3.58
40
175.00
98.96
273.96
118.6
4.09
45
175.00
123.08
298.08
129.0
4.60
50
175.00 I
149.60
3-24.601
140.5
1 5.11
Brooks Engineering Associates, PA P. 1 of 1 10/21/2008

FLOW PER MINUTE
015413
Part Number
PUMP PERFORMANCE
DISCHARGE11/4" NPT
Voltage
Phase Amps
Stages
!
■■■'
112
—
1 12.0
6
22-318'
5030-0006
112
230
1 6.0
6
22-318"
moon
_
115
060
8
„
5030-0008
1l2
230
■''W.�■1
8
24-118"
5030-0009
314
230
1 8.0
12
28-718"
120
NH
32
0 24
80
16
40
8-
FLOW PER MINUTE
015413
Part Number
HP
Voltage
Phase Amps
Stages
Height
5030-0005
112
115
1 12.0
6
22-318'
5030-0006
112
230
1 6.0
6
22-318"
5030-0007
1/2
115
1 12.0
8
24-118"
5030-0008
1l2
230
1 6.0
8
24-118"
5030-0009
314
230
1 8.0
12
28-718"
7 GPM Models
PUMP PERFORMANCE CURVE Ipm
27 GPM
11/4" NPT DISCHARGE
36 320 71/7 HP -18 STAGE
306
1 HP- 7 STA -
226
fi4 314 HP
206 '. BSTAGE
56 780
U
S40 186
ta0
� d0 '1f2 HP -d STAGE
770
GALLONS
UTERS
FLOWPERMINUTE
no
21 17M
015045
Part Number
HP
Voltage
Phase Amps
Stagesr317/8
PUMP PERFORMANCE CURVE
5032-0005
112
115
1 12.0
4
5032-0006
112
230
1 6.0
4
5032-0007
3/4
230
1 8.0
6
5032-0008
1
230
1 9.8
7
5032-D009
1-112
230
1 13.1
10
015414
Part Number
H P
19 GPM Models
Phase Amps
LL
PUMP PERFORMANCE CURVE
5031-0005
112
19 GPM
1 12.0
5
1"W NPT DISCHARGE
5031-0006
zeo
80
5
72
240
230
1 8.0
7
64-
5031-0008
1
230
200
9
56
5033-0009
1-1/2
0
46
160
5
U
a 40
120
NH
32
0 24
80
16
40
8-
0
5 10 15 20 25
GALLONS
LITERS 0 20 40 60 80 10(
FLOW PER MINUTE
015414
Part Number
H P
Voltage
Phase Amps
Stages
Height
5031-0005
112
115
1 12.0
5
21-15116'
5031-0006
112
230
1 6.0
5
21-15116"
5031-0007
314
230
1 8.0
7
25-1116"
5031-0008
1
230
1 9.8
9
28-118"
35 GPM Models
w PUMP PERFORMANCE CURVE
35 GPM
2" NPT DISCHARGE
56 180.
1-12 HP- 5 STAGE
48
160-
140 1 HP-4STAG
E
40
120-
2 3/4 HP -3 STAGE
100-
z
O
24 s6 12HP-2 STAGE
O
60
16
40
8
20-
13--
10
0010 20 30 40 50 60
GALLONS
LITERS 0 40 80 120 160 200
FLOW PER MINUTE 015044
Part Number
H P
Voltage
Phase Amps
Stages
Height
5033-0005
112
115
1 12.0
2
19.7116"
5033-0006
112
230
1 6.0
2
19-7116"
5033-0007
3/4
230
1 8.0
3
22-3116'
5033-0008
1
230
1 9.8
4
24-15/16'
5033-0009
1-1/2
230
1 13.1
5
29-15116'
© Copyright 2007 Zoeller Co. All rights reserved.

Uzi
1.5 Return Pump Tank Sizing Calculations
i
Uio
4,
7

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

BEA Project #
307808
TANK SIZING CALCULATIONS
Return Flush Pump Tank
1850 gallon Pump Tank Selected
Minimum dose (gal)
700
Total Height
63 inches
Storage (gal/ft)
355.51
Storage (gal/in)
29.63
min pump submergence
21 inches
min dose volume
23.6 inches
space lost due to float spacing
12 inches
emergency storage
6.4 inches
Emergency Storage (gal)
188.77
Net On/Off
PT -298 Length (ft) Width (ft) Height (ft) Gal/ft Volume (gal) Setting (inches)
Pump Tank 1 9.83 4.83 5.25 355.51 1866.4 23.63
In/ft.
29.63
Brooks Engineering Associates, PA p.1 of 1 10/21/2008

f
Pressure and Flow Anal
77
Zone Y
1.6 Irrigationsis
MOM

PRESSURE ANALYSIS .
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d4-87) (Q/C)185
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 1A-1
No. Laterals:
7
Tubing: ID in
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
3616
Design Flow (Qpm):
18.68
Supply Manifold Elev. 1A-SM2
Return Manifold Elev. 1A-RM2
Run Run
Lateral Run Elev. Length
2
3
4
5
6
7
Brooks Engineering Associates, PA
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
35
43
48
62
83
114
123
129
132
131
115
73
71
71
82
76
74
72
70
65
51
32
Application Flow gpm :
18.7
Min. Design Scour Vel. (ftts)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)'
2.30
Re 'd Flush Rate (qpm)':
34.8
Dose
Flow (gp
0.3
0.4
0.4
0.5
0.6
0.9
1.2
1.3
1.3
1.4
1.4
1.2
0.8
0.7
0.7
0.8
0.8
0.8
0.7
0.7
0.7
0.5
0.3
PA of 3
Lateral Lateral Min. Flush
enoth (ft) Dose (aom) Flow Wpm)
474
2.4
4.7
522
2.7
5.0
492
2.5
4.8
594
3.1
5.4
584
3.0
5.3
348
1.8
4.1
34.8
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1A-1
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 e
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2 Total Segment Headloss (ft) = Friction + Elev.
Inputs Dose Flow a Flush Flow (b
0.016 0.014
12.016 12.014
10/20/2008
Hydraulic Unit
H.U. Elev Mom
3 Headloss from H.0 (ft J3
_--
Supply Force Main Friction Losses
H.U. to J1
l
Segment Flow Rate (gpm)
r �'rti
Line Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft)
3.058
2.778
Minor Losses (ft)
0.306
0.278
I
Line Velocity (ft/s)
2.27
2.16
J1 to J2
141
Segment Flow Rate (gpm)
=,
Line Length (ft)
Line Size ID (in)s
5 Friction Headloss (ft)
0.434
0.902
Minor Losses (ft)
0.043
0.090
Line Velocity (ft/s)
1.16
1.73
J2 to 1A-SM2
Segment Flow Rate (gpm)
1•
Line Length (ft)
1
Line Size ID (in)5
6 Friction Headloss (ft)
1.512
4.770
Minor Losses (ft)
0.151
0.477
Line Velocity (ft/s)
1.25
2.33
Supply Farce Main Elevation Delta
H.U. to Manifold
82
Wit
7Elevation (ft) from
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
r
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.700
3.213
9 Total Segment Headloss (ft) = Friction + Elev.
-26.300
-30.787
N
Return Force Main Friction Losses
1A-RM2 to J2
Segment Flow Rate (gpm)
Line Length (ft)
606
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
10. 131
Line Velocity (ft1s)
2.5544
J2 to J1
..4
Segment Flow Rate (gpm)
Line Length (ft)
490
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
1.853
Line Velocity (ft/s)
2.03
J1 to WWTF
Segment Flow Rate (gpm)
h
Line Length (ft)
1000
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
3.782
Line Velocity (ft/s)
2.03
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Fmj
Brooks Engineering Associates, PA p.2 of 3
€dam
10/20/2008

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

0,
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1A-2
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
Inputs
Dose Flow (all Flush Flow (b)
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 e
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.016
0.014
2 Total Segment Headloss (ft) = Friction + Elev.
12.016
12.014
Hydraulic Unit
H.U. Elev NNW
3 Headloss from H.0 (ft.)3
$
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
3.058
2.778
4 Friction Headloss (ft)
Minor Losses (ft)
0.306
0.278
Line Velocity (ft/s)
2.27
2.16
J1 to J2
Segment Flow Rate (gpm)
mmmmmm
t�
Line Length (ft)
Ij
Line Size ID (in)5
5 Friction Headloss (ft)
0.434
0.902
Minor Losses (ft)
0.043
0.090
Line Velocity (ftts)
1.16
1.73
J2 to 1A-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
1.078
3.426
6 Friction Headloss (ft)
Minor Losses (ft)
0.108
0.343
Line Velocity (ft/s)
1.92
3.58
Supply Force Main Elevation Delta
82
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in ddp system from supply manifold to return manifold
-
Feed Manifold to Bottom Lateral
Feed
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
50
Line Size ID (In)"
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
0.933
3.504
9 Total Segment Headloss (ft) = Friction + Elev.
-42.067
-46.496
Return Force Main Friction Losses
1A-RM1 to J2
Segment Flow Rate (gpm)--
Line Length (ft)
606
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
0.438
Line Velocity (fits)
1.50
1.50
J2 to J1
Segment Flow Rate (gpm)
Line Length (ft)
490
Line Size ID (in.)
Minor Losses (ft)
1.853
Friction Headloss (ft)
Line Velocity (fUs)
3.66
3.66
J1 to WWTF
FF�-
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft) 3.782
Line Velocity (ft/s) 2.03
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Enaineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d487) (Q/C)1.es
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
R E uaIs the Required Flush Rate plus the Dose Flow Rate
Zone: 1A-3
No. Laterals:
13
Tubin : ID (in)
0.79
Emitters h :
0.62
Emitter S adn ft
2
Total Footage:
7736
Design Flow (gpm):
39.97
Application Flow (gpm):
40.0
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID in
0.787
Residual Flow for Scour pm)e
2.30
Req'd Flush Rate (gpm)':
69.9
Supply Manifold Elev.
1A-SM1
Return Manifold Elev.
1A-RM1
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Len th
# Emitters Flow (g m)7
Length (ft)
Dose(gpm)
Flow pm)8
1 1
73
0.8
594
3.1
5.4
2
72
0.7
3
74
0.8
4
78
0.8
2 5
79
0.8
608
3.1
5.4
6
70
0.7
7
73
0.8
8
62
0.8
3 9
81
0.6
586
3.0
5.3
10
68
0.7
11
68
0.7
12
76
0.8
4 13
153
1.6
606
3.1
5.4
14
150
1.6
5 15
155
1.6
610
3.2
5.5
16
150
1.6
6 17
153
1.6
604
3.1
5.4
18
149
1.5
7 19
148
1.5
586
3.0
5.3
20
145
1.5
8 21
148
1.5
590
3.0
5.3
22
147
1.5
9 23
147
1.5
582
3.0
5.3
24
144
1.5
10 25
148
1.5
596
3.1
5.4
26
150
1.6
11 27
150
1.6
600
3.1
5.4
28
150
1.6
12 29
149
1.5
594
3.1
5.4
30
148
1.5
13 31
146
1.5
580
3.0
5.3
32
144
1.5
7736
3868
40.0
40.0
69.9
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

9
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1A-3
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
Inputs Dose Flow Flush Flow (b)
1 Operating Head from Pump Curvet
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.016
0.014
2 Total Segment Headloss (ft) = Friction + Elev.
12.016
12.014
Hydraulic Unit
H.U. Elev MUM
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm)
fR
f?
Line Length (ft)
Line Size ID (in)s
4 Friction Headloss (ft)
3.058
2.778
Minor Losses (ft)
0.306
0.278
Line Velocity (ft/s)
2.27
2.16
J1 to J2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
5 Friction Headloss (ft)
0.434
0.902
Minor Losses (ft)
0.043
0.090
Line Velocity (ft/s)
1.16
1.73
J2 to 1A-SM1
Segment Flow Rate (gpm)
"
1+
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.081
0.254
Minor Losses (ft)
0.008
0.025
Line Velocity (ft/s)
0.47
0.88
Supply Force Main Elevation Delta
Manifold
82
7 Elevation (ft) from H.U. to
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.801
5.166
9 Total Segment Headloss (ft) = Friction + Elev.
-43.199
-46.834
Return Force Main Friction Losses
1A-RM1 to J2
Segment Flow Rate (gpm)
1`
Line Length (ft)
317
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
0.229
Line Velocity (ft/s)
1.30
J2 to J1
Segment Flow Rate (gpm)
€,
Line Length (ft)
490
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
1.853
Line Velocity (ft/s)
2.03
J1 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
3.782
Line Velocity (ft/s)
t' D It
2.03
Return Lme Eleve on e a
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d487) (Q/C)t es
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
S Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 1 B-5
No. Laterals:
15
Tubing: ID in
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
7732
Design Flow gpm);
39.95
Application Flow (gpm):
39.9
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)a
2.30
Re 'd Flush Rate ( m)B:
74.7
Supply Manifold Elev.
1B-SM1
Return Manifold Elev.
IB -RMI
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Length
# Emitters Flow gpm)7
Length ft)
Dose (pm)
Flow pm)'
1 1
27
0.3
410
2.1
4.4
2
53
0.5
3
55
0.6
4
70
0.7
2 5
78
0.8
602
3.1
5.4
6
71
0.7
7
71
0.7
8
81
0.8
3 9
106
1.1
438
1.9
4.2
10
113
1.2
4 11
120
1.2
492
2.4
4.7
12
126
1.3
5 13
133
1.4
538
2.8
5.1
14
136
1.4
6 15
138
1.4
556
2.9
5.2
16
140
1.4
7 17
143
1.5
574
3.0
5.3
18
144
1.5
8 19
145
1.5
584
3.0
5.3
20
147
1.5
9 21
149
1.5
592
3.1
5.4
22
147
1.5
10 23
145
1.5
576
3.0
5.3
24
143
1.5
11 25
135
1.4
524
2.7
5.0
26
127
1.3
12 27
107
1.1
396
2.0
4.3
28
91
0.9
13 29
84
0.9
594
3.1
5.4
30
75
0.8
31
70
0.7
32
68
0.7
14 33
63
0.7
440
2.5
4.8
34
58
0.6
35
52
0.5
36
47
0.5
15 37
42
0.4
416
2.6
4.9
38
35
0.4
39
31
0.3
40
25
0.3
41
23
0.2
42
21
0.2
43
17
0.2
44
14
0.1
7732
3866
39.9
40.2
74.7
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

r-1
_. 3
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 18-5
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev OEM
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J1
o
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
3.058
2.776
4 Friction Headloss (ft)
0.306
0.278
Minor Losses (ft)
Line Velocity (ft/s)
2.27
2.16
J1 to J3
'
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID 0n)s
0.081
0.278
5 Friction Headloss (ft)
0.008
0.028
Minor Losses (ft)
Line Velocity (ft/s)
1.11
2.16
J3 to1B-SM1
�x•� �--
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (1n)5
4
1.415
4.454
6 Friction Headloss (ft)
Minor Losses (ft)
0.142
0.445
Line Velocity Ws)
1.75
3.24
Supply Force Main Elevation Delta
70
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold°
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.491
4.759
9 Total Segment Headloss (ft) = Friction + Elev.
-49.509
-53.241
Return Force Main Friction Losses
1 B -RMI to J3
34.5
Segment Flow Rate (gpm)
Line Length (ft)
360
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
3.072
Line Velocity fts)
0.38
J3 to J1
--
Segment Flow Rate (gpm)
Line Length (ft)
100
Line Size ID (in.)
Minor Losses (ft)
0.419
Friction Headloss (ft)
Line Velocity (ft/s)
2.15
J1 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
KA; sses (ft)
M' L
4.192
Friction Headloss (ft) 2.15
Line Velocity (ftls) 2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 1 B-5
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
190.5
82.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
309.5
134.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
448.5
194.1
Flush Pressure at backwash tank for Min. Flush Rate
445.5
192.9
PRV NEEDED? YES
ZONE SUMMARY W1 PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
309.9
51.2
Pressure at manifold before PRV
469.0
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
45.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
16.0
6.9
Flush Pressure at W WTF for Min. Flush Rate
82.3
35.6
Hioh Pressure Check: Emitter P on Bottom Lateral at Dose Flow
146.5
63.4
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

7
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d" $') (Q/C)t •ss
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 E uals the Required Flush Rate plus the Dose Flow Rate
Zone: 15.5
No. Laterals:
10
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2-
Total Footage:
5022
Design Flow pm):
25.95
Application Flow (gpm):
25.9
Min. Design Scour Vel. (fUs)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour pm)6
2.30
Re 'd Flush Rate(gpm)8:
48.9
Supply Manifold Elev.
1 B-SM2
Return Manifold Elev.
1 B-RM2
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Len th
# Emitters
Flow (g m)7
Length (ft)
Dose ( m)
Flow (g m)
1 1
11
0.1
532
2.7
5.0
2
15
0.2
3
19
0.2
4
24
0.2
5
31
0.3
6
49
0.5
7
55
0.6
8
62
0.6
2 9
62
0.6
582
3.0
5.3
10
69
0.7
11
79
0.8
12
81
0.8
3 13
102
1.1
420
2.2
4.5
14
108
1.1
4 15
113
1.2
462
2.4
4.7
16
118
1.2
5 17
123
1.3
504
2.6
4.9
18
129
1.3
6 19
131
1.4
528
2.7
5.0
20
133
1.4
7 21
136
1.4
548
2.8
5.1
22
138
1.4
8 23
140
1.4
566
2.9
5.2
24
143
1.5
9 25
145
1.5
582
3.0
5.3
26
146
1.5
10 27
83
0.9
298
1.5
3.8
28
66
0.7
5022
2511
25.9
25.9
48.9
Brooks Engineering Associates, PA p.1 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Friction Headloss (ft) from Pump to H.0 2 0.016 0,014
2 Total Segment Headloss (ft) = Friction + Elev. 12.016 12.014
Hydraulic Unit
H.U. Elev Now
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J1
ROME
Segment Flow Rate (gpm)
Line Length (ft)
y
Line Size ID (in)5
h=.
4 Friction Headloss (ft)
3.058
2.778
Minor Losses (ft)
0.306
0.278
Line Velocity fts)
2.27
2.16
J1 to J4
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
0.597
2.042
Minor Losses (ft)
0.060
0.204
Line Velocity (ft/s)
1.11
2.16
J4 to 1B-SM2
Segment Flow Rate (gpm)
1
25.91
48.9
Line Length (ft)
a
Line Size ID (in)5
6 Friction Headloss (ft)
0.324
1.047
Minor Losses (ft)
0.032
0.105
Line Velocity (ft/s)
1.13
2.13
Supply Force Main Elevation Delta
Manifold
82
7 Elevation (ft) from H.U. to
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold "4
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.280
1.519
9 Total Segment Headloss (ft) = Friction + Elev.
-24.720
-30.461
Return Force Main Friction Losses
1 B-RM2 to J4
Segment Flow Rate (gpm)
23.0
Line Length (ft)
185
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
5.983
Line Velocity (ft/s)
3.63
J4 to J1
Segment Flow Rate (gpm)
MOMIM
Line Length (ft)
735
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
1.178
Line Velocity (ft/s)
1.28
J1 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
_
Minor Losses (ft)
Friction Headloss (ft) 4.192
Line Velocity (fUs)
2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
q
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 1 B-6
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
195.9
84.8
Low Pressure Check: P at Min. Flush Flow at Return Manifold
304,1
131.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
412.3
178.5
Flush Pressure at backwash tank for Min. Flush Rate
464.3
201.0
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
zi'.I
. I.
Pressure at manifold before PRV
469.6
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
32.5
14.1
Flush Pressure at WWTF for Min. Flush Rate
111.1
48.1
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
133.2
57.7
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d4'87) (Q/C)'•as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 3A-7
No. Laterals:
18
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
9620
Design Flow g m :
49.70
Application Flow m):
49.7
Min. Design Scour Vel. ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour g m e
2.30
Req'd Flush Rate (gpm)8:
91.1
Supply Manifold Elev.
3A-SM1
Return Manifold Elev.
3A -RMI
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Length
# Emitters
Flow (gpm'
Length (it)
Dose (gpm)
Flow (gpm)
1 1
23
0.2
554
2.9
5.2
2
33
0.3
3
42
0.4
4
50
0.5
5
58
0.6
6
71
0.7
2 7
90
0.9
378
2.0
4.3
8
99
1.0
3 9
108
1.1
432
2.2
4.5
10
108
1.1
4 11
111
1.1
448
2.3
4.6
12
113
1.2
5 13
115
1.2
462
2.4
4.7
14
116
1.2
6 15
118
1.2
476
2.5
4.8
16
120
1.2
7 17
121
1.3
494
2.6
4.9
18
126
1.3
8 19
134
1.4
540
2.8
5.1
20
136
1.4
9 21
138
1.4
552
2.9
5.2
22
138
1.4
10 23
139
1.4
558
2.9
5.2
24
140
1.4
11 25
140
1.4
564
2.9
5.2
26
142
1.5
12 27
144
1.5
580
3.0
5.3
28
146
1.5
13 29
146
1.5
588
3.0
5.3
30
148
1.5
14 31
148
1.5
594
3.1
5.4
32
149
1.5
15 33
150
1.6
600
3.1
5.4
34
150
1.6
16 35
150
1.6
600
3.1
5.4
36
150
1.6
17 37
150
1.6
600
3.1
5.4
38
150
1.6
18 39
150
1.6
600
3.1
5.4
40
150
1.6
-
9620
4810
49.7
49.7
91.1
Brooks Engineering Associates, PA p.1 of 3 11/18/2008
A

F
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
i
ZONE 3A-7
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev HINN
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
0.005 0.016
12.005 12.016
H.U. to J1
Segment Flow Rate (gpm)
NEENEEMM
Line Length (ft)
Line Size ID (in)5
rtk
4 Friction Headloss (ft)
0.959
3.178
Minor Losses (ft)
0.096
0.318
Line Velocity (ft/s)
1.21
2.32
J1 to J6
Segment Flow Rate (gpm)
NEW
Line Length (ft)
Line Size ID (in)"
5 Friction Headloss (ft)
1.017
3.369
Minor Losses (ft)
0.102
0.337
Line Velocity (ft/s)
1.21
2.32
J6 to 3A-SM1
Segment Flow Rate (gpm)
REEMEMINIME
Line Length (ft)
Line Size ID (in)'
6 Friction Headloss (ft)
0.816
2.653
Minor Losses (ft)
0.082
0.265
Line Velocity (ft/s)
1.63
3.08
Supply Force Main Elevation Delta
Manifold
96
7 Elevation (ft) from H.U. to
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
I'
) MEN
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.854
5.175
9 Total Segment Headloss (ft) = Friction + Elev.
-35.146
-38.825
Return Force Main Friction Losses
3A-SM1 to J6
Segment Flow Rate (gpm)
Line Length (ft)
325
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
2.478
Line Velocity (ft/s)
1.80
J6 to J1
Segment Flow Rate (gpm)
Line Length (ft)
1060
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
4.898
Line Velocity (ft/s)
2.26
J1 to WWTF
¢,f;
Segment' Flow Rate (gpm)
EM
MEN
Length (ft)
1000
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
4.621
Line Velocity (ft/s)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
11/18/2008

t9g
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3A-7
Ziu•o
a 1.z
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
211.2
91.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
287.8
124.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
409.1
177.1
Flush Pressure at backwash tank for Min. Flush Rate
470.1
203.5
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
Ziu•o
a 1.z
Pressure at manifold before PRV
469.9
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5d.Q,!
Low Pressure Check: P at Min. Flush Flow at Return Manifold
34.5
14.9
Flush Pressure a' WWTF for Min. Flush Rate
121,5
52.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
143.6
62.2
Brooks Engineering Associates, PA p.3 of 3
11/18/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 fl/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d° 87) (Q/C)1.as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 3A-8
No. Laterals:
8
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
4148
Design Flow (gpm):
21.43
Application Flow m :
21.4
Min. Design Scour Vel. (ft/s)
2.0
TubingID (in)
0.787
Residual Flow for Scour gpm)6
2.30
Reo'd Flush Rate (qpm)':
39.8
Supply Manifold Elev.
3A-SM1
Return Manifold Elev.
3A-RM1
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Len th
# Emitters
Flow (gpm)7
Length (ft)
Dose (gpm)
Flow m)8
1 1
15
0.2
510
2.6
4.9
2
17
0.2
3
19
0.2
4
21
0.2
5
24
0.2
6
26
0.3
7
29
0.3
8
31
0.3
9
34
0.4
10
39
0.4
2 11
41
0.4
598
3.1
5.4
12
45
0.5
13
100
1.0
14
113
1.2
3 15
127
1.3
512
2.6
4.9
16
129
1.3
4 17
128
1.3
508
2.6
4.9
18
126
1.3
5 19
124
1.3
494
2.6
4.9
20
123
1.3
6 21
122
1.3
488
2.5
4.8
22
122
1.3
7 23
120
1.2
450
2.3
4.6
24
105
1.1
8 25
87
0.9
588
3.0
5.3
26
79
0.8
2760
0.6
28
68
0.7
4148
2074
21.4
21.4
39.8
Brooks Engineering Associates, PA
p.1 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 3A-8
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. ElevRM
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to A
Segment Flow Rate (gpm)
01IMMEMIREl
antra •3� '
Line Length (ft)
a
Line Size ID (in)5
4 Friction Headloss (ft)
0.959
3.178
Minor Losses (ft)
0.096
0.318
Line Velocity (ft/s)
1.21
2.32
A to J6
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
1.017
3.369
Minor Losses (ft)
0.102
0.337
Line Velocity (fUs)
1.21
2.32
J6 to 3A-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.816
2.653
Minor Losses (ft)
0.082
0.265
Line Velocity (ft/s)
1.63
3.08
Supply Force Main Elevation Delta
from H.U. to Manifold
96
7 Elevation (ft)
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateralz
1.786
5.066
9 Total Segment Headloss (ft) = Friction + Elev.
-26.214
-29.934
Return Force Main Friction Losses
3A-SM1 to J6
Segment Flow Rate (gpm)
Line Length (ft)
325
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
2.478
Line Velocity (ft/s)
0.80
J6 to J1
-
Segment Flow Rate (gpm)
_
�
Line Length (ft)
1060
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
4.898
Line Velocity (ft/s)
2.26
A to WWTF
Segment Flow Rate (gpm)
_-•_ -'
Line Length (ft)
1000
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
4.621
Line Velocity (ft/s)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
IpiBrooks Engineering Associates, PA P.2 of 3 10/20/2008
H;v

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3A-8
Zo' •o
"•`
Pressure at manifold before PRV
Feet
PSI
Total Headioss at Min. Flush Rate at Return Manifold
218.2
94.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
280.8
121.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
400.1
173.2
Flush Pressure at backwash tank for Min. Flush Rate
463.1
200.5
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
Zo' •o
"•`
Pressure at manifold before PRV
469.9
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.0'
Low Pressure Check: P at Min. Flush Flow at Return Manifold
27.5
11.9
Flush Pressure at WWTF for Min. Flush Rate
114.5
49.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
134.7
58.3
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones:)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U da.e7) (a C)t.es
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 E uals the Required Flush Rate Dlus the Dose Flow Rate
Zone: 1 B•9
No. Laterals:
3
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
1358
Design Flow (g m):
7.02
Application Flow(gpm):
7.0
Min, Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Req'd Flush Rate (gpm)':
13.9
Supply Manifold Elev.
1 B-SM3
Return Manifold Elev.
1 B-RM3
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Len th
# Emitters Flow (gpm'
Length (ft)
Dose (gpm)
Flow g m)8
1 1
11 0.1
398
2.1
4.4
2
16 0.2
3
89 0.9
4
83 0.9
2 5
82 0.8
470
2.4
4.7
6
153 1.6
3 7
70 0.7
490
2.5
4.8
8
67 0.7
9
58 0.6
10
50 0.5
7.0
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1B-9
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
In uts Dose Flow (a Flush Flow (b)
Rom
', ..
-11
summ
0.016 0.014
12.016 12.014
10/20/2008
Hydraulic Unit
H.U. Elev MEW
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft)
3.373
3.056
Minor Losses (ft)
0.337
0.306
Line Velocity (ft/s)
2.27
2.16
J3 to J4
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
•
5 Friction Headloss (ft)
0.503
0.620
Minor Losses (ft)
0.050
0.062
Line Velocity (ft/s)
1.11
1.24
J4 to 1 B-SM3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.071
0.231
Minor Losses (ft)
0.007
0.023
Line Velocity (ft/s)
1.01
1.91
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
46
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
;
Himi
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold'
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.769
2.542
9 Total Segment Headloss (ft) = Friction + Elev.
-18.231
-23.458
Return Force Main Friction Losses
1 B-RM3 to J4
Segment Flow Rate (gpm)
Line Length (ft)
50
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
Line Velocity (ft/s)
0.394
0.66
J4 to J1
Segment Flow Rate (gpm)
Line Length (ft)
620
Line Size ID (in.)
f
Minor Losses (ft)
0.993
Friction Headloss (ft)
Line Velocity (ft/s)
1.28
J1 to WWTF
,r",•
Segment Flow Rate (gpm)
��
SEEM
Line Length (ft)
1100
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
4.611
Line Velocity (ft/s)
2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d4 87) (Q/C)''85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 1B-10
No. Laterals:
4
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
1992
Design Flow m):
10.29
u
10.3
Return Manifoldw
2.0
Run
Run
Lateral Run Elev.
Lenath
Req'd Flush Rate (Qpm) :
19.5
13
14
2 15
$4
16
5.4
17
g
18
•
is
20
4 21
cs
Application Flow (gpm):
10.3
Min. Design Scour Vel. ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)'
2.30
Req'd Flush Rate (Qpm) :
19.5
Dose Lateral Lateral Min. Flush
nitters Flow (gpm)' Length (ft)_ Dose (gpm) Flow (gpm)
73 0.8
604
3.1
5.4
73 0.8
76 0.8
80 0.8
74 0.8
600
3.1
5.4
72 0.7
73 0.8
81 0.8
96 1.0
386
2.0
4.3
97 1.0
99 1.0
402
2.1
4.4
Brooks Engineering Associates, PA p.1 of 3
64
11/18/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1B-10
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
0.016 0.014
12.016 12.014
Friction Headloss (ft) 4.611
Line Velocity (ft/s) 2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
11/18/2008
61111
Hydraulic Unit
H.U. Elev
�j
3 Headloss from H.0 (ft.)3li
Supply Force Main Friction Losses
H.U. to J3
Segment Flow Rate (gpm)
Line Length (ft)
9yy
Line Size ID (in)sii
(
4 Friction Headloss (ft)
3.373
3.056
Minor Losses (ft)
0.337
0.306
Line Velocity (ftls)
2.27
2.16
J3 to J4
Segment Flow Rate (gpm)
NEEMENEMEM
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
0.503
0.620
Minor Losses (ft)
0.050
0.062
Line Velocity (ft/s)
1.11
1.24
J4 to 1 B-SM3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.071
0.231
Minor Losses (ft)
0.007
0.023
Line Velocity (ft/s)
1.01
1.91
Supply Force Main Elevation Delta
Manifold
46
7 Elevation (ft) from H.U. to
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
0.533
2.117
9 Total Segment Headloss (ft) = Friction + Elev.
-10.467
-15.883
Return Force Main Friction Losses
1 B-RM3 to J4
Segment Flow Rate (gpm)
Yiil
Line Length (ft)
50
Line Size ID (in.)
Minor Losses from Check Valve
(
Friction Headloss (ft)
0.394
Line Velocity (ft/s)
0.88
J4 to J1
Segment Flow Rate (gpm)
Line Length (ft)
620
t`
Line Size ID (in.)
Minor Losses (ft)
Friction' Headloss (ft)
0.993
Line Velocity (ft/s)
1.28
J1 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
7100
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft) 4.611
Line Velocity (ft/s) 2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
11/18/2008
61111

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 1B-10
295.5
51.2
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
162.9
70.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
337,1
145.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
434.1
187.9
Flush Pressure at backwash tank for Min. Flush Rate
430.7
186.5
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
295.5
51.2
Pressure at manifold before PRV
469.6
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
127.1
° 55.0` `
Low Pressure Check: P at Min. Flush Flow at Return Manifold
39.1
16.9
Flush Pressure at WWTF for Min. Flush Rate
87.1
37.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
130.5
56.5
Brooks Engineering Associates, PA p.3 of 3 11/18/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 2A-12
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE inputs jDose
Flow (a)l Flush Flow b
5
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
Line length (ft) from P.T. to H.0 .5
;gym
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.017
0.016
2 Total Segment Headloss (ft) = Friction + Elev.
12.017
12.016
Hydraulic Unit
�+
H.U. Elev Mom
3 Headloss from KLI (ft.)3
MEMEMN
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm) REMERMIMEMN
Line Length (ft)
Line Size ID (in)'
4 Friction Headloss (ft)
3.301
3.107
Minor Losses (ft)
0.330
0.311
Line Velocity (ft/s)
2.37
2.29
A to J7
Segment Flow Rate (gpm)
Wr
Line Length (ft)
Line Size ID (in)'
5 Friction Headloss (ft)
6.919
6.512
Minor Losses (ft)
0.692
0.651
Line Velocity (ft/s)
2.37
2.29
J7 to 2A-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
6 Friction Headloss (ft)
0.929
2.882
Minor Losses (ft)
0.093
0.288
Line Velocity (ft/s)
2.54
4.69
Supply Force Main Elevation Delta
Manifold 151
0
7 Elevation (ft) from H.U. to
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold'
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.854
5.175
9 Total Segment Headloss (ft) = Friction + Elev.
-30.146
-33.825
n
Return Force Main Friction Losses
2A-RM1 to J7
Segment Flow Rate (gpm)H
t.
d
Line Length (ft) 162
Line Size ID (in.)'t
Minor Losses from Check Valve
Friction Headloss (ft)
2.551
Line Velocity (ft/s)
3.70
J7 to J1
Segment Flow Rate (gpm)
Line Length (ft)
2096
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
8.786
Line Velocity (ft/s)
2.15
J1 to NM(fF
f
Segment Flow Rate (gpm)
( }
Line Length (ft) 1000
t
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
4.192
Line Velocity (ft/s)
2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to VWVfF
i
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

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

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d°.a�) (Q/C)1.as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 E uals the Required Flush Rate plus the Dose Flow Rate
Zone: 3A -13 -
No. Laterals:
14
Tubing: ID in
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
6586
Design Flow (gpm):
34.03
Supply Manifold Elev.
34.0
3A-SM2
2.0
Return Manifold Elev.
0.787
3A-RM2
2.30
Run
Run
Lateral Run Elev.
Length
# Emitte
1 1
5.3
150
2
149
2 3
446
147
4
1.1
145
3 5
113
6
2.2
110
4 7
108
8
1.1
109
5 9
4.6
110
10
111
6 11
450
112
12
1.2
113
7 13
114
14
2.4
115
8 15
115
16
1.2
115
9 17
4.7
116
18
117
10 19
466
118
20
1.2
119
11 21
116
22
2.4
113
12 23
109
24
1.2
99
13 25
4.7
92
26
87
14 27
416
45
28
1.0
40
29
38
30
1.8
32
31
30
32
0.5
24
33
5.1
23
34
16
35
15
Application Flow m):
34.0
Min. Design Scour Vel. (fUs)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Re 'd Flush Rate m)8:
66.2
Dose
-s Flow (gpm)7
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (gpm)
1.6
598
3.1
5.4
1.5
1.5
584
3.0
5.3
1.5
1.2
446
2.3
4.6
1.1
1.1
434
2.2
4.5
1.1
1.1
442
2.3
4.6
1.1
1.2
450
2.3
4.6
1.2
1.2
458
2.4
4.7
1.2
1.2
460
2.4
4.7
1.2
1.2
466
2.4
4.7
1.2
1.2
474
2.4
4.7
1.2
1.2
458
2.4
4.7
1.2
1.1
416
2.1
4.4
1.0
1.0
358
1.8
4.1
0.9
0.5
542
2.8
5.1
0.4
0.4
0.3
0.3
0.2
0.2
0.2
0.2
0.1
34.0
34.0
66,2
Brooks Engineering Associates, PA p.1 of 3 10/2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 3A-13
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
Line length (ft) from P.T. to H.0 .5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev Mom
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J6
Segment Flow Rate (gpm) Kfflmmmfflr7 r xri�.1r7:l+r..�Prr,
Line Length (ft)
Line Size ID (in)'
4 Friction Headloss (ft) 1.976 6.547
Minor Losses (ft) 0.198 0.655
Line Velocity (ft/s) 1.21 2.32
J6 to 2A -SMI
Segment Flow Rate (gpm) $r
Line Length (ft)
Line Size ID (in)'
5 Friction Headloss (ft) 0.161 0.552
Minor Losses (ft) 0.016 0.055
Line Velocity (ft/s) 0.42 0.82
2A-SM1 to 3A-SM2
Segment Flow Rate (gpm)'
Line Length (ft)
Line Size ID (in)'
6 Friction Headloss (ft) 0.663 2.276
Minor Losses (ft) 0.066 0.228
Line Velocity (fUs) 1.48 2.87
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 109
Drip System Headloss Results
s:
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Lateral' _
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2 0.000 0.000
9 Total Segment Headloss (ft) = Friction + Elev. -30.000 -37.000
Return Force Main Friction Losses
3A 0110 to 2A-RM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
Line Velocity (ft/s)
2A-RM1 to J6
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
J6 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (fUs)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
f�
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3A-13
Feet
252.3
PSI
51.2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
231.4
100.2
Low Pressure Check: P at Min. Flush Flow at Return Manifold
267.6
115.8
High Pressure Check: Emitter P on Bottom Lateral at. Dose Flow
390.9
169.2
Flush Pressure at backwash tank for Min. Flush Rate
477.7
206.8
PRV NEEDED? YES
ZONE SUMMARY W1 PRV
Pressure loss required (high pressure - 60 psi)
Feet
252.3
PSI
51.2
Pressure at manifold before PRV
469.9
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
45.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
16.0
6.9
Flush Pressure at WWTF for Min. Flush Rate
117.7
51.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
127.0
55.0
Brooks Engineering Associates, PA
p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U da.a7) (Q/C),.as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 E uals the Required Flush Rate plus the Dose Flow Rate
Zone: 28-14
No. Laterals:
9
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
4530
Design Flow (gpm):
23.41
Supply Manifold Elev.
23.4
26-SM1
Return Manifold Elev.
Tubing ID in
2B-RM1
Run
Run
Lateral Run Elev.
Length
1 1
2
3
4
5
6
7
8
2 9
10
11
12
3 13
14
452
4 15
4.6
16
5 17
18
6 19
20
7 21
22
436
8 23
4.6
24
9 25
13
16
20
24
28
33
38
45
53
60
68
89
129
134
134
134
135
136
137
137
138
138
139
139
Application Flow pm):
23.4
Min. Design Scour Vel. ft/s)
2.0
Tubing ID in
0.787
Residual Flow for Scourg m)6
2.30
Reo'd Flush Rate (gprnf:
42.5
Dose
Flow (gpm)'
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (gpm)
0.1
362
0.2
2.5
0.1
0.2
0.2
0.2
0.3
0.3
0.4
0.5
452
2.3
4.6
0.5
0.6
0.7
0.9
436
2.3
4.6
1.3
1.4
536
2.8
5.1
1.4
1.4
538
2.8
5.1
1.4
1.4
546
2.8
5.1
1.4
1.4
550
2.8
5.1
1.4
1.4
554
2.9
5.2
1.4
1.4
556
2.9
5.2
1.4
23.4
21.8
42.5
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 2B-14
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.Z
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ftJ9
too
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm)
j Line Length (ft) - t`
Line Size ID (in)5
4 Friction Headloss (ft) 3.301 3.178
Minor Losses (ft) 0.330 0.318
Line Velocity (ft/s) 2.37 2.32
J1 to J7
Segment Flow Rate (gpm)1`
Line Length (ft)
Line Size ID (in)5
6.919 6.662
5
Friction Headloss ft
O Minor Losses (ft) 0.692 0.666
Line Velocity (ft/s) 2.37 2.32
J7 to 26-SM7 � � ,.
Segment Flow Rate (gpm)!��+
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft) 0.342 1.303
Minor Losses (ft) 0.034 0.130
Line Velocity (ft/s) 1.12 2.32
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 179
Drip System Headloss Results
r 8 Total Headloss (ft.) in drip system from supply manifold to return manifold'
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold'
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
i Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
V Friction Headloss (ft) from Manifold to Bottom Feed Latera12 1.578 4.726
9 Total Segment Headloss (ft) = Friction + Elev. -22.422 -26.274
' Return Force Main Friction Losses
2B -RMI to J7
Segment Flow Rate (gpm);t
i Line Length (ft) 410
Line Size ID (in.)
Minor Losses from Check Valve 1.551
Friction Headloss (ft) 2.03
Line Velocity (ft/s) 2.03
J7 to J1
Segment Flow Rate (gpm)
Line Length (ft) Wb
Line Size ID (in.)
Minor Losses (ft)
928
Friction Headloss (ft) 2.03
Line Velocity (ft/s) 2.03
J1 to WWTF r
Segment Flow Rate (gpm)
Line Length (ft) 1000
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft) 3.782
Line Velocity (ft/s) 2.03
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 213-14
Feet
166.2
PSI
51.2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
301.2
130.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
198.8
86.1
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
304.8
131.9
Flush Pressure at backwash tank for Min. Flush Rate
543.6
235.3
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
166.2
PSI
51.2
Pressure at manifold before PRV
461.4
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
45.0 ."
Low Pressure Check: P at Min. Flush Flow at Return Manifold
18.0
7.8
Flush Pressure at WWTF for Min. Flush Rate
184.7
80.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
119.4
51.7
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ftts is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d"'87) (Q/C)t ee
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 2A-15
No. Laterals:
22
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
11548
Design Flow m):
59.66
Supply Manifold Elev. 2A-SM1
Return Manifold Elev. 2A-RM1
Run Run
r
l
�A
I Brooks Engineering Associates, PA
k
1 1
2
2 3
4
3 5
6
4 7
8
5 9
10
6 11
12
7 13
14
8 15
16
9 17
18
10 19
20
11 21
22
12 23
24
13 25
26
14 27
28
15 29
30
16 31
32
17 33
34
18 35
36
19 37
38
20 39
40
21 IM
22 45
46
47
Application Flow (g m):
59.7
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID in
0.787
Residual Flow for Scour ( m)6
2.30
Req'd Flush Rate (gpm)8:
110.3
Dose
Emitters Flow (gpm)'
Lateral
Length (ft)
Lateral
Dose(Qpm)
Min. Flush
Flow (gpm)'
139
1.4
556
2.9
5,2
139
1.4
139
1.4
554
2.9
5.2
138
1.4
138
1.4
550
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
137
1.4
548
2.8
5.1
137
1.4
138
1.4
552
2.9
5.2
138
1.4
138
1.4
554
2.9
5.2
139
1.4
139
1.4
554
2.9
5.2
138
1.4
138
1.4
552
2.9
5.2
138
1.4
138
1.4
550
2.8
5.1
137
1.4
137
1.4
546
2.8
5.1
136
1.4
134
1.4
534
2.8
5.1
133
1.4
132
1.4
528
2.7
5.0
132
1.4
131
1.4
524
2.7
5.0
131
1.4
131
1.4
490
2.5
4.8
114
1.2
110
1.1
426
2.2
4.5
103
1.1
99
1.0
392
2.0
4.3
97
1.0
87
0.9
606
3,1
5.4
73
0.8
69
0.7
74
0.8
76
0.8
340
1.8
4.1
48
0.5
27
0.3
19
0.2
5774
59.7
59.7
110.3
p.1 of 3
10/20/2008

Friction Headloss (ft) 4.192
Line Velocity (ft/s) 2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
[FRI
10/20/2008
Brooks Engineering Associates, PA p.2 of 3
i
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
€ice
ZONE 2A•15
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE Inputs Dose Flow a) Flush Flow b)
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.
0.017
0.016
2 Total Segment Headloss (ft) = Friction + Elev.
12.017
12.016
Irk
Hydraulic Unit
H.U. Elev FBIM
I"
3 Headloss from H.0 (ft.)s
`c
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm)
!.
Line Length (ft) l
Line Size ID (in)'
4 Friction Headloss (ft)
3.301
3.107
Minor Losses (ft)
0.330
0.311
Line Velocity (ft/s)
2.37
2.29
J1 to J7
M.. MM
Segment Flow Rate (gpm) "'°
Line Length (ft)
Line Size ID (in)6
5 Friction Headloss (ft)
6.919
6.512
Minor Losses (ft)
0.692
0.651
Line Velocity (fUs)
2.37
2.29
J7 to 2A -SMI
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.165
0.513
Minor Losses (ft)
0.017
0.051
Line Velocity (ft/s)
1.24
2.29
Supply Force Main Elevation Delta
H.U. to Manifold 151
P
7 Elevation (ft) from
Drip System Headloss Results
x
8 Total Headloss (ft.) in drip system from supply manifold to return manifold°
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
UAW
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.648
3.049
9 Total Segment Headloss (ft) =Friction + Elev.
-51.352
-55.951
t
Return Force Main Friction Losses
2A-RM1 to J7
Segment Flow Rate (gpm)
• - �'r)f
Line Length (ft)
165
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
0.692
Line Velocity (ft/s)
2.15
J7 to J1
1
Segment Flow Rate (gpm)
Line Length (ft)
2096
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
8.786
Line Velocity (ft/s)
2.15
J1 to WWTF
Segment Flow Rate (gpm)-
Line Length (ft) 1000
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft) 4.192
Line Velocity (ft/s) 2.15
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
[FRI
10/20/2008
Brooks Engineering Associates, PA p.2 of 3
i

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 2A-15
223.3
51.2
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
275.1
119.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
223.9
96.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
361.9
156.7
Flush Pressure at backwash tank for Min. Flush Rate
518.2
224.3
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
223.3
51.2
Pressure at manifold before PRV
461.6
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
` 4&110'
Low Pressure Check: P at Min. Flush Flow at Return Manifold
15.0
6.5
Flush Pressure at VWVfF for Min. Flush Rate
159.3
69.0
Hiah Pressure Check: Emitter P on Bottom Lateral at Dose Flow
148.3
64.2
Brooks Engineering Associates, PA
P.3of3
10/20/2008

=mal
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
I
! Brooks Engineering Associates, PA p.1 of 3 10/20/2008
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1
From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2
Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727
U d4'87)
(ojC)1.ee
3
From Wastewater Systems Inc. Data
4
Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5
From Engineering Drawings
6
Calculated from 0 = VA
7
Equals the # of emitters in the run times the individual
emitter flow rate in gpm.
8
Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 2B-16 I
ADolication Flow m :
67.8
No. Laterals: 26
Min. Design Scour Vel. (fVs)
2.0
Tubing: ID in 0.79
Tubing ID in
0.787
Emitters h : 0.62
Residual Flow forScour apm)s
2.30
Emitter Spacing ft 2
Re 'd Flush Rate ( m B:
127.6
Total Footage: 13132
Design Flow m : 67.85
Supply Manifold Elev._ 28-SM1
Return Manifold Elev. 2B -RMI
Run Run
Dose Lateral Lateral
Min. Flush
Lateral Run Elev. Len th # Emitters
Flow m)r Length (ft) Dose pm)
Flow pm)'
1 1 89
0.9 368
1.9
4.2
2 95
1.0
2 3 95
1.0 384
2.0
4.3
4 97
1.0
3 5 100
1.0 408
2.1
4.4
6 104
1.1
4 7 110
1.1 448
2.3
4.6
8 114
1.2
5 9 116
1.2 470
2.4
4.7
10 119
1.2
6 11 122
1.3 494
2.6
4.9
12 125
1.3
7 13 128
1.3 516
2.7
5.0
14 130
1.3
8 15 133
1.4 536
2.8
5.1
16 135
1.4
9 17 139
1.4 562
2.9
5.2
18 142
1.5
10 19 144
1.5 582
3.0
5.3
20 147
1.5
11 21 149
1.5 600
3.1
5.4
22 .151
1.6
12 23 151
1.6 606
3.1
5.4
24 152.
1.6
13 25 152
1.6 608
3.1
5.4
26 152
1.6
14 27 150
1.6 598
3.1
5.4
28 149
1.5
15 29 147
1.5 584
3.0
5.3
30 145
1.5
16 31 143
1.5 568
2.9
5.2
32 141
1.5
17 33 139
1.4 546
2.8
5.1
34 134
1.4
18 35 132
1.4 522
2.7
5.0
36 129
1.3
19 37 125
1.3 496
2.6
4.9
38 123
1.3
20 39 120
1.2 474
2.4
4.7
40 117
1.2
21 41 114
1.2 452
2.3
4.6
42 112
1.2
22 43 110
1.1 434
2.2
4.5
44 107
1.1
23 45 102
1.1 396
2.0
4.3
46 96
1.0
24 47 93
1.0 366
1.9
4.2
48 90
0.9
25
81
0.8 540
2.8
5.1
69
0.7
63
0.7
57
0.6
26
53 51
0.5 574
3.0
5.3
54 48
0.5
55 42
0.4
56 38
0.4
57 30
0.3
58 30
0.3
59 24
0.2
60 24
0.2
13132 6566
67.8
67.8
127.6
I
! Brooks Engineering Associates, PA p.1 of 3 10/20/2008

p.2 of 3 10/20/2008
Brooks Engineering Associates, PA
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 28-16
TOP LOAD MANIFOLD PRESSURE ANALYSIS
k
INPUT
LINE Inputs I Dose Flow a Flush Flow b
1 Operating Head from Pump Curve'
i
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U?
0.017
0.016
rias
2 Total Segment Headloss (ft) = Friction + Elev..
12.017
12.016
Hydraulic Unit
_I
H.U. Elev
3 Headloss from H.0 (ft.)s
F
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)"
4 Friction Headloss (ft)
3.301
3.178
Minor Losses (ft)
0.330
0.318
-
Line Velocity (ft/s)
2.37
2.32
J7 to J7
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
fel
5 Friction Headloss (ft)
6.919
6.662
Minor Losses (ft)
0.692
0.666
Line Velocity (ft/s)
2.37
2.32
J7 to 2B-SM1
Segment Flow Rate (gpm)
l-
yt=8
Line Length (ft)
Line Size ID (in)s
6 Friction Headloss (H)
0.342
1.303
Minor Losses (ft)
0.034
0.130
2.32
Line Velocity (ft/s)
1.12
Supply Force Main Elevation Delta
179
%q
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
fq
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifoldto Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral'
1.708
4.940
9 Total Segment Headloss (ft) = Friction + Elev.
-53.292
-57.060
Return Force Main Friction Losses
2B-RM1to J7
Segment Flow Rate (gpm)
Line Length (ft)Met
410
Line Size ID (in.)
Minor Losses from Check Valve
- -
.Friction Headloss (ft)
1.551
Line Velocity (ft/s)
2.03
J7 to J1
Segment Flow Rate (gpm)
Line Length (ft)
2096
mei
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
7 928
Line Velocity (ft/s)
2.03
J1 to WWTF
Segment Flow Rate (gpm)
- EM
Line Length (ft)
1000
Line Size ID (in.)
la"
Minor Losses (ft)
3.782
Friction Headloss (ft)
Line Velocity (ft/s)
2.03
Return Line Elevation Delta _
Elevation (ft) from Return Manifold to W WTF
p.2 of 3 10/20/2008
Brooks Engineering Associates, PA

Brooks Engineering Associates, PA
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 2B-16
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
305.2
132.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
194.8
84.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
335.7
145.3
Flush Pressure at backwash tank for Min. Flush Rate
539.6
233.6
PRV NEEDED? YES
ZONE SUMMARY W1 PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
197.1
51.2
Pressure at manifold before PRV
461.4
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
14.0
6.0
Flush Pressure atWWTF for Min. Flush Rate
180.7
78.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
150.2
65.0
p.3 of 3
10/20/2008

I
Pi
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d4.87) (Q/C)1.85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 4A-17
No. Laterals:
7
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
3664
Design Flow (gpm):
18.93
Supply Manifold Elev. 4A-SM1
Return Manifold Elev. 4A-RM1
Run Run
1 1
2,
3
4
2
3 9
10
4 11
12
5 13
14
6 15
16
7
Brooks Engineering Associates, PA
3664
Application Flow (gpm):
18.9
Min. Desi n Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Re 'd Flush Rate (gpm)':
35.0
Dose
mitters Flow (gpm)'
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (gpm)
55
0.6
500
2.6
4.9
61
0.6
65
0.7
69
0.7
71
0.7
598
3.1
5.4
68
0.7
70
0.7
90
0.9
102
1.1
418
2.2
4.5
107
1.1
113
1.2
466
2.4
4.7
120
1.2
131
1.4
538
2.8
5.1
138
1.4
130
1.3
548
2.8
5.1
144
1.5
104
1.1
596
3.1
5.4
66
0.7
68
0.7
60
0.6
1832
18.9
18.9
35.0
p.1 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 4A-17
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
Inputs IDose Flow a Flush Flow (b
00-10011
0.007 0.016
12.007 12.016
H.U. tc J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft)
5.061
10.970
Minor Losses (ft)
0.506
1.097
Line Velocity (f /s)
1.51
2.30
J20 to J11
Segment flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
5 Friction Headloss (ft)
1.478
3.203
Minor Losses (ft)
0.148
0.320
Line Velocity (ft/s)
1.37
2.07
J11 to 4A -SMI
Segment Flow Rate (gpm)
Line Length (ft)
Line SizeID (in)5
6 Friction Headloss (ft)
0.346
1.112
Minor Losses (ft)
0.035
0.111
Line Velocity (ft/s)
1.24
2.34
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
229
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed LateralZ
1.831
5.139
9 Total Segment Headloss (ft) = Friction + Elev.
-12.169
-15.861
Return Force Main Friction Losses
4A-RM1 to J11
Segment Flow Rate (gpm)
—
Line Length (ft)
165
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
1.871
Line Velocity (ft/s)
2.41
All to J20
Segment Flow Rate (gpm)
Line Length (ft)
1314
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
6.072
Line Velocity (ft1s)
2.26
J20 to WWTF
--
Segment Flow Rate (gpm)
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (ft/s)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
17 Brooks Engineering Associates, PA p.2 of 3
I
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4A-17
112.0
51.2
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
357.3
154.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
141.7
61.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
250.6
108.5
Flush Pressure at backwash tank for Min. Flush Rate
578.2
250.3
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
112.0
51.2
Pressure at manifold before PRV
467.4
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
138.6
&0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
50.6
21.9
Flush Pressure at WWTF for Min. Flush Rate
259.5
112.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
143.8
62.2
Brooks Engineering Associates, PA
p.3of3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ da.e7) (Q/C)t.ea
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 4A-18
No. Laterals:
4
Tubing: ID in
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
1872
Design Flow (gpm):
9.67
Supply Manifold Elev. 4A-SM1
Return Manifold Elev. 4A-RM1
Run Run
2
3
4
8
9
Application Flow (gpm):
9.7
Min. Design Scour Vel. ft/s)
2.0
TubingID in
0.787
Residual Flow for Scour (gpm)6
2.30
Req'd Flush Rate (gpm)e:
18.9
Dose
Lateral
Lateral
Min. Flush
mitters Flow (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)
24 0.2
584
3.0
5.3
27 0.3
27 0.3
65 0.7
63 0.7
86 0.9
104 1.1
408
2.1
4.4
100 1.0
97 1.0
380
2.0
4.3
93 1.0
89 0.9
500
2.6
4.9
79 0.8
46 0.5
36 0.4
936 9.7
9.7
18.9
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

(°; I PRESSURE ANALYSIS
I TOP FEED MANIFOLD SYSTEM
ZONE 4A-18
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
i
H.U. EleElm
v
3 Headloss from H.0 (ft.toll )3
Supply Force Main Friction Losses
J20
H.U. to
Segment Flow Rate (gpm)3
if.
Line Length (ft)
Line Size ID (in)s
4 Friction Headloss (ft)
5.061
10.970
Minor Losses (ft)
0.506
1.097
Line Velocity (ft/s)
1.51
2.30
J20 to A 1
Segment Flow Rate (gpm)
YS
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
1.478
3.203
Minor Losses (ft)
0.148
0.320
Line Velocity (ft/s)
1.37
2.07
A I to 4A -SMI
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.346
1.112
Minor Losses (ft)
0.035
0.111
Line Velocity (ft/s)
1.24
2.34
Supply Force Main Elevation Delta
Manifold
229
7 Elevation (ft) from H.U. to
Drip System Headloss Results
r
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
?).
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.323
4.297
9 Total Segment Headloss (ft) = Friction + Elev.
-12.677
-16.703
Return Force Main Friction Losses
4A-RM1 to A 1
Segment Flow Rate (gpm)
Line Length (ft)
165
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
1.871
Line Velocity (ft/s)
2.41
J11 to J20
Segment Flow Rate (gpm)
M om
Line Length (ft)
1314
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
6.072
Line Velocity (ft/s)
2.26
J20 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (ft/s)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4A-18
Feet
112.5
PSI
51.2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
352.3
152.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
146.7
63.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
251.1
108.7
Flush Pressure at backwash tank for Min. Flush Rate
583.2
252.4
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
112.5
PSI
51.2
Pressure at manifold before PRV
467.4
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
138.6
60.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
55.6
24.1
Flush Pressure at WWTF for Min. Flush Rate
264.5
114.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
144.3
62.5
10/20/2008
Brooks Engineering Associates, PA p.3 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 fl/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d"-") (Q/C)' "
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 4A-20
No. Laterals:
8
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
4288
Design Flow (gpm):
22.15
Supply Manifold Elev. 4A-SM3
Brooks Engineering Associates, PA
Application Flow pm):
22.2
Min. Design Scour Vel. (fUs)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Req'd Flush Rate (gpm)8:
40.6
P.1 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 4A-20
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
Line length (ft) from P.T. to H.0 .5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev OEM
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
Jnn
Inputs IDose Flow a Flush Flow b)
0.007 0.016
12.007 12.016
H.U. to
Segment Flow Rate (gpm)
(,1
Line Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft)
5.061
10.970
Minor Losses (ft)
0.506
1.097
Line Velocity (ft/s)
1.51
2.30
J20 to J13
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
2.733
5.924
Minor Losses (ft)
0.273
0.592
Line Velocity (ft/s)
1.37
2.07
J13 to 4A-SM3
Segment Flow Rate (gpm)
._.
.
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.623
1.903
Minor Losses (ft)
0.062
0.190
Line Velocity (ft/s)
1.49
2.72
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
292
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.675
4.886
9 Total Segment Headloss (ft) = Friction + Elev.
-8.325
-12.114
Return Force Main Friction Losses
4A-RM3 to J13
Segment Flow Rate (gpm)
Line Length (ft)
165
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
3.531
Line Velocity (ft/s)
2.90
J 13 to J20
Segment Flow Rate (gpm)=-
Line Length (ft)
2430
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.228
Line Velocity (ft/s)
2.26
J20 to W WTF
Segment Flow Rate (gpm)
_
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (ft/s)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4A-20
Feet
43.5
PSI
51.2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
418.8
181.3
Low Pressure Check: P at Min. Flush Flow at Return Manifold
80.2
34.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
182.1
78.8
Flush Pressure at backwash tank for Min. Flush Rate
633.6
274.3
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
43.5
PSI
51.2
Pressure at manifold before PRV
465.7
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
138.6
60.0 ;
Low Pressure Check: P at Min. Flush Flow at Return Manifold
55.6
24.1
Flush Pressure at WWTF for Min. Flush Rate
318.7
137.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
139.9
1 60.6
Brooks Engineering Associates, PA
p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes .& Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d4 87) (Q/C)1 ea
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 5A-23
No. Laterals:
11
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spading ft
2
Total Footage:
4784
Design Flow (gpm):
24.72
Supply Manifold Elev. 5A-SM2
Return Manifold Elev. 5A-RM2
Run Run
Lateral Run Elev. Length
2
3
4
5
6
7
8
9
10
11
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
70
69
88
98
98
96
96
94
94
94
93
92
91
110
112
109
105
103
102
100
99
88
85
70
Application Flow (gpm):
24.7
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID in
0.787
Residual Flow for Scour (gpm)s
2.30
Req'd Flush Rate (gpm):
50.0
Dose
Flow (gpi
0.8
0.7
0.7
0.9
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
0.9
1.1
1.2
1.1
1.1
1.1
1.1
1.0
1.0
0.9
0.9
0.7
0.7
Lateral Lateral Min. Flush
:ngth (ft) Dose (gpm) Flow (gpm)
600 3.1 5.4
392
2.0
4.3
384
2.0
4.3
376
1.9
4.2
374
1.9
4.2
366
1.9
4.2
444
2.3
4.6
428
2.2
4.5
410
2.1
4.4
398
2.1
4.4
612
3.2
5.5
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

1
" PRESSURE ANALYSIS
1
TOP FEED MANIFOLD SYSTEM
ZONE 5A-23
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
Line length (ft) from P.T. to H.U'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2 Total Segment Headloss (ft) = Friction + Elev.
m
Brooks Engineering Associates, PA p.2 of 3 10/2012008
Hydraulic Unit
r
H.U. Elev MUM
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
rA
4 Friction Headloss (ft)
10.507
9.784
Minor Losses (ft)
1.051
0.978
f
Line Velocity (ft1s)
2.25
2.16
J20 to J15
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
6.678
6.218
Minor Losses (ft)
0.668
0.622
Line Velocity (ft/s)
2.03
1.95
J15 to 5A-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.391
1.348
c
Minor Losses (ft)
0.039
0.135
Line Velocity (ft1s)
1.46
2.85
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
276
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold°
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold°
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.923
5.286
9 Total Segment Headloss (ft) = Friction + Elev.
-19.077
-22.714
Ott
Retum Force Main Friction Losses
5A-RM2 to J15
Segment Flow Rate (gpm)
Line Length (ft)
190
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
1.343
Line Velocity (ft/s)
2.40
J15 to J20
Segment Flow Rate (gpm)
Line Length (ft)
2860
Line Size ID (in.)
Minor Losses (ft)
s
Friction Headloss (ft)
13.215
Line Velocity (ft/s)
2.26
J20 to WWTF
Segment Flow Rate (gpm)
RMIMIM
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
11
Line Velocity (ft/s)
2.26
Retum Line Elevation Delta
Elevation (ft) from Retum Manifold to WWTF
m
Brooks Engineering Associates, PA p.2 of 3 10/2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE SA -23
oy 1
° I .Z
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
408.4
176.8
Low Pressure Check: P at Min. Flush Flow at Return Manifold
91.6
39.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
197.7
85.6
Flush Pressure at backwash tank for Min. Flush Rate
618.3
267.7
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
oy 1
° I .Z
Pressure at manifold before PRV
454.7
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.01
Low Pressure Check: P at Min. Flush Flow at Return Manifold
25.5
11.0
Flush Pressure at WWTF for Min. Flush Rate
277.8
120.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
127.6
55.2
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d487) (Q/C)185
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 5A-24
No. Laterals:
13
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
6418
Design Flow (gpm):
33.16
Ap lication Flow (gpm):
33.2
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID in
0.787
Residual Flow for Scour (gpm)6
2.30
Rea'd Flush Rate (gpm)':
63.1
Supply Manifold Elev.
5A-SM2
Return Manifold Elev.
5A-RM2
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Length
# Emitters
Flow g m 7
Length (ft)
Dose (gpm)
Flow (gpm)8
1 1
132
1.4
526
2.7
5.0
2
131
1.4
2 3
130
1.3
518
2.7
5.0
4
129
1.3
3 5
128
1.3
508
2.6
4.9
6
126
1.3
4 7
125
1.3
496
2.6
4.9
8
123
1.3
5 9
122
1.3
484
2.5
4.8
10
120
1.2
6 11
119
1.2
472
2.4
4.7
12
117
1.2
7 13
116
1.2
462
2.4
4.7
14
115
1.2
8 15
113
1.2
450
2.3
4.6
16
112
1.2
9 17
110
1.1
436
2.3
4.6
18
108
1.1
10 19
107
1.1
426
2.2
4.5
20
106
1.1
11 21
104
1.1
408
2.1
4.4
22
100
1.0
12 23
81
0.8
626
3.2
5.5
24
79
0.8
25
77
0.8
26
76
0.8
13 27
78
0.8
606
3.1
5.4
28
77
0.8
29
75
0.8
30
73
0.8
3209 33.2
63.1
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE SA -24
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
I Inputs Dose Flow Wj Flush Flow b)
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit'
Line length (ft) from P.T. to H.U'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.015
0.014
2 Total Segment Headloss (ft) = Friction + Elev.
12.015
12.014
Hydraulic Unit
H.U. Elev NEW
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
_
Line Length (ft)
Line Size ID (1n)s
4 Friction Headloss (ft)
10.507
9.784
Minor Losses (ft)
1.051
0.978
Line Velocity (ft/s)
2.25
2.16
J20 to J15
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
5 Friction Headloss (ft)
6.678
6.218
Minor Losses (ft)
0.668
0.622
Line Velocity (ft/s)
2.03
1.95
J15 to 5A-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
6 Friction Headloss (ft)
0.391
1.348
Minor Losses (ft)
0.039
0.135
Line Velocity (ft1s)
1.46
2.85
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
276
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.888
5.230
9 Total Segment Headloss (ft) = Friction + Elev.
-35.112
-38.770
Return Force Main Friction Losses
5A-RM2 to J15
Segment Flow Rate (gpm).
Line Length (ft)
190
Line Size ID(in.)'
_. ..
Minor Losses from Check Valve
Friction Headloss (ft)
1.343
Line Velocity (ft/s)
2.40
J15 to J20
Segment Flow Rate (gpm)
k'
Line Length (ft)
2860
Line Size ID (in.)
Minor Losses (ft)
- I
Friction Headloss (ft)
13.215
Line Velocity (ft/s)
2.26
J20 to WWTF
Segment Flow Rate (gpm)
ROW
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (ft/s)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
ra
Brooks Engineering Associates, PA p.2 of 3
c
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-24
Feet
75.2
PSI
51.2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
411.4
178.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
88.6
38.4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
213.8
92.5
Flush Pressure at backwash tank for Min. Flush Rate
615.3
266.4
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
75.2
PSI
51.2
Pressure at manifold before PRV
454.7
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.0 "
Low Pressure Check: P at Min. Flush Flow at Return Manifold
22.5
9.7
Flush Pressure at WWTF for Min. Flush Rate
274.8
116.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
143.6
62.2
Brooks Engineering Associates, PA
p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hr = (4.727 U d°'87) (Q/C)1.ae
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 5B-25
No. Laterals:
11
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
5986
Design Flow m):
30.93
Supply Manifold Elev.
30.9
58 -SMI
2.0
Return Manifold Elev.
0.787
5B-RM1
2.30
Req'd Flush Rate (gpm)8:
Run
Run
5.2
Lateral Run Elev.
Len th
# Emittt
1 1
iii
136
2
2.2
136
2 3
3.0
136
4
137
3 5
137
6
138
4 7
139
8
139
5 9
140
10
141
6 11
141
12
142
7 13
142
14
143
8 15
110
16
106
9
82
75
67
70
10 21
70
22
65
23
63
24 60
11 57
53
48
43
Mi In 41
5986
Application Flow (gpm):
30.9
Min. Design Scour Vel. (ftls)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm)8
2.30
Req'd Flush Rate (gpm)8:
56.2
Dose
1.4
1.4
1.4
1.4
1.4
1.4
1.4
1.4
1.5
1.5
1.5
1.5
1.5
1.1
1.1
0.8
0.8
0.7
0.7
0.7
0.7
0.7
0.6
0.6
0.5
0.5
0.4
0.4
Lateral Lateral Min. Flush
snath (ft) Dose (qpm) Flow (gpm)
546
2.8
5.1
550
2.8
5.1
556
2.9
5.2
562
2.9
5.2
566
2.9
5.2
570
2.9
5.2
432
2.2
4.5
588
3.0
5.3
516
2.7
5.0
556
2.9
5.2
30.9
56.2
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

r
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE SB -25
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 .5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev now
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
a� tl e�mai,d��r
rlau
Line Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft)
10.507
8.787
Minor Losses (ft)
1.051
0.879
Line Velocity (ft1s)
2.25
2.04
J20 to J16
Segment Flow Rate (gpm)
i
Line Length (ft)
Line Size ID (in)s
5 Friction Headloss (ft)
7.752
6.483
Minor Losses (ft)
0.775
0.648
Line Velocity (ft/s)
2.03
1.84
A 6 to 5B-SM1
Segment Flow Rate (gpm)$
�" &
Line Length (ft)
f`
Line Size ID (In)5
6 Friction Headloss (ft)
0.359
1.054
Minor Losses (ft)
0.036
0.105
Line Velocity (ft/s)
1.39
2.50
Supply Force Main Elevation Delta
H.U. to Manifold
268
7 Elevation (ft) from
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
__
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.610
4.779
9 Total Segment Headloss (ft) = Friction + Elev.
-31.390
-35.221
Return Force Main Friction Losses
5B-RM1 to A 6
Segment Flow Rate (gpm)
Line Length (ft)
190
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
2.511
Line Velocity (ft/s)
2.93
J16 to J20
Segment Flow Rate (gpm)
,,`.;/ see,":
`
Line Length (ft)
3320
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.262
Line Velocity (ft/s)
1.91
J20 to WWTF
Segment Flow Rate (gpm)
- -
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.883
Line Velocity (ft/s)
1.91
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
i§
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 513-25
Feet
78.3
PSI
51.2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
396.3
171.6
Low Pressure Check: P at Min. Flush Flow at Return Manifold
103.7
44.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
216.9
93.9
Flush Pressure at backwash tank for Min, Flush Rate
620.5
268.6
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
78.3
PSI
51.2
Pressure at manifold before PRV
453.5
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
28.5
12.3
Flush Pressure at W WTF for Min. Flush Rate
278.8
120.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
139.9
60.6
Brooks Engineering Associates, PA p.3 of 3 10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d4'$') (Q/C)' as
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 5B-26
No. Laterals:
8
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
4714
Design Flow g m :
24.36
Application Flow (gpm):
24.4
Min. Design Scour Vel. ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour (gpm s
2.30
Read Flush Rate ( m)':
42.8
Supply Manifold Elev.
5B-SM1
Return Manifold Elev.
5B-RM1
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Length
# Emitters
Flow gpm'
Length (ft)
Dose ( m)
Flow gpm
1 1
39
0.4
574
3.0
5.3
2
45
0.5
3
49
0.5
4
50
0.5
5
51
0.5
6
53
0.5
2
76
0.8
604
3.1
5.4
76
0.8
75
0.8
75
0.8
3 11
74
0.8
590
3.0
5.3
12
74
0.8
13
73
0.8
14
74
0.8
4
75
0.8
600
3.1
5.4
75
0.8
75
0.8
75
0.8
5 19
75
0.8
594
3.1
5.4
20
74
0.8
21
74
0.8
22
74
0.8
6
75
0.8
598
3.1
5.4
75
0.8
75
0.8
74
0.8
7 27
75
0.8
594
3.1
5.4
28
74
0.8
29
74
0.8
30
74
0.8
8
71
0.7
560
2.9
5.2
71
0.7
70
0.7
fi 68
0.7
4714
2357
24.4
24.4
42.8
Brooks Engineering Associates, PA p.1 of 3 10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
q
ZONE 5B-26
TOP LOAD MANIFOLD PRESSURE ANALYSIS
.1
INPUT
LINE
inputs Dose
Flow (a)
Flush Flow b
Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size 1D (in)
Friction Headloss (ft) from Pump to H.0 2
0.015
0.013
2 Total Segment Headloss (ft) = Friction + Elev.
12.015
12.013
Hydraulic Unit
H.U. Elev
i
3 Headloss from H.0 (ft.)3
ht
Supply Force Main Friction Losses
H.U. to J20
j
Segment Flow Rate (gpm)
Line Length (ft)
`..
Line Size ID (1n)s
L,u6
4 Friction Headloss (ft)
10.507
8.787
Minor Losses (ft)
1.051
0.879
r�
Line Velocity (ft/s)
2.25
2.04
J20 to J16
Segment Flow Rate (gpm)
Line Length (ft)
KNOMM
Line Size ID (in)6
_
5 Friction Headloss (ft)
7.752
6.483
Minor Losses (ft)
0.775
0.648
w
Line Velocity (ft/s)
2.03
1.84
J16 to 5B-SM1
Segment Flow Rate (gpm)
g�
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.359
1.054
Minor Losses (ft)
0.036
0.105
Line Velocity (ft/s)
1.39
2.50
Supply Force Main Elevation Delta
i
7 Elevation (ft) from H.U. to Manifold
268
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
_
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
r-§
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (1n)5
��
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.631
4.815
9 Total Segment Headloss (ft) = Friction + Elev.
-28.369
-32.185
Return Force Main Friction Losses
5B-RM1 to J16
Segment Flow Rate (gpm)
Line Length (ft)
190
Line Size ID (in.)
Minor Losses from Check Valve
rq%
Friction Headloss (ft)
2.511
Line Velocity (ft/s)
2.93
J16 to J20
Segment Flow Rate (gpm)
Line Length (ft)
3320
In"
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.262
Line Velocity (ft/s)
1.91
J20 to WWfF
Segment Flow Rate (gpm)
Line Length (ft)
3503
9
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.883
Line Velocity (ft/s)
1.91
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
r
Brooks Engineering Associates, PA p.2 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 5B-26
_Feet
75.3
PSI
51.2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
397.3
172.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
102.7
44.4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
213.9
92.6
Flush Pressure at backwash tank for Min. Flush Rate
619.5
268.2
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
_Feet
75.3
PSI
51.2
Pressure at manifold before PRV
453.5
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
' 50.0 -
Low Pressure Check: P at Min. Flush Flow at Return Manifold
27.5
11.9
Flush Pressure at WWTF for Min. Flush Rate
277.8
120.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
136.9
1 59.3
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U da.s�) (Q/C),.es
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 E uals the Required Flush Rate plus the Dose Flow Rate
Zone: 513-27
No. Laterals:
9
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
3986
Design Flow (gpm):
20.59
Application Flow (gpm):
20.6
Min. Design Scour Vel. ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour g m)6
2.30
Re 'd Flush Rate (gpm)':
41.3
Supply Manifold Elev.
5B-SM2
Return Manifold Elev.
5B-RM2
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Len th
# Emitters Flow gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)
1 1
144 1.5
574
3.0
5.3
2
143 1.5
2 3
137 1.4
542
2.8
5.1
4
134 1.4
3 5
131 1.4
516
2.7
5.0
6
127 1.3
4 7
123 1.3
484
2.5
4.8
8
119 1.2
5 9
114 1.2
446
2.3
4.6
10
109 1.1
6 11
106 1.1
416
2.1
4.4
12
102 1.1
7 13
90 0.9
338
1.7
4.0
14
79 0.8
8 15
71 0.7
272
1.4
3.7
16
65 0.7
9
56 0.6
398
2.1
4.4
52 0.5
48 0.5
43 0.4
_
3986
1993 20.6
20.6
41.3
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 58-27
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.0 5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev NEW
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm).',1tt
Line Length (ft)
Line Size ID (in)s�`
4 Friction Headloss (ft)
10.507
8.787
Minor Losses (ft)
1.051
0.879
Line Velocity (ft/s)
2.25
2.04
J20 to J16
Segment Flow Rate (gpm)`
%)
Line Length (ft)
Line Size ID (in)6
5 Friction Headloss (ft)
7.752
6.483
Minor Losses (ft)
0.775
0.648
Line Velocity (ft/s)
2.03
1.84
A 6 to 56-SM2
Segment Flow Rate (gpm)ffl�
Line Length (ft)
Line Size ID (in)6
6 Friction Headloss (ft)
2.563
8.678
Minor Losses (ft)
0.256
0.868
Line Velocity (ft/s)
1.50
2.90
Supply Force Main Elevation Delta
Manifold
268
7 Elevation (ft) from H.U. to
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.867
3.478
9 Total Segment Headloss (ft) = Friction + Elev.
-17.133
-21.522
Return Force Main Friction Losses
58-RM2 to J16
Segment Flow Rate (gpm)
�-
Line Length (ft)
865
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
6.497
Line Velocity (ft/s)
2.16
J16 to J20
Segment Flow Rate (gpm)
RMEEM
Line Length (ft)
3320
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.262
Line Velocity (ft/s)
1.91
J20 to WWTF
Segment Flow Rate (gpm)
_
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.883
Line Velocity (ft/s)
1.91
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 5B-27
PSI
51.2
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
399.0
172.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
101.0
43.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
200.2
86.7
Flush Pressure at backwash tank for Min. Flush Rate
606.9
262.7
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
Pressure loss required (high pressure - 60 psi) 61.6
PSI
51.2
Pressure at manifold before PRV
451.1
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
127.1
.55.0 ,
Low Pressure Check: P at Min. Flush Flow at Return Manifold
45.1
19.5
Flush Pressure at WWTF for Min. Flush Rate
284.4
123.1
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
137.2
59.4
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

r
6;
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hr = (4.727 U da.s7) ((�C)s.ss
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 5B-28
No. Laterals:
5
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
2684
Design Flow (gpm):
13.87
Application Flow (gpm):
13.9
Min. Design Scour Vel. fts)
2.0
TubingID (in)
0.787
Residual Flow for Scour (gpm)6
2.30
Req'd Flush Rate (gpm)':
25.4
Supply Manifold Elev.
Lateral
5B-SM2
Min. Flush
Return Manifold Elev.
Length (ft)
5B-RM2
Flow (gpm)
Run
Run
3.0
Lateral Run Elev.
Length
# Emitters
1 1
43
2
45
3
47
4
0.5
48
5
51
6
53
2
484
56
4.8
0.6
59
63
64
3 11
67
12
0.7
70
13
5.2
71
14
70
4
69
0.7
69
68
546
2.8
67
5 19
67
20
0.7
37
21
36
22
32
23
524
28
24
0.4
24
25
21
26
_
17
0.3
2684
1342
Brooks Engineering Associates, PA
Dose
Lateral
Lateral
Min. Flush
N (gpm)'
Length (ft)
Dose (gpm)
Flow (gpm)
0.4
574
3.0
5.3
0.5
0.5
0.5
0.5
0.5
0.6
484
2.5
4.8
0.6
0.7
0.7
0.7
556
2.9
5.2
0.7
0.7
0.7
0.7
546
2.8
5.1
0.7
0.7
0.7
0.7
524
2.7
5.0
0.4
0.4
0.3
0.3
0.2
0.2
p.1 of 3
10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5B-28
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev OEM
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft)
10.507
8.787
Minor Losses (ft)
1.051
0.879
Line Velocity (ft/s)
2.25
2.04
J20 to J16
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
7.752
6.483
Minor Losses (ft)
0.775
0.648
Line Velocity (ft/s)
2.03
1.84
J16 to 5B-SM2
Segment Flow Rate (gpm)5a
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
2.563
8.678
Minor Losses (ft)
0.256
0.868
Line Velocity (ft/s)
1.50
2.90
Supply Force Main Elevation Delta
H.U. to Manifold
268
7 Elevation (ft) from
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.443
4.501
9 Total Segment Headloss (ft) = Friction + Elev.
-26.557
-30.499
Return Force Main Friction Losses
5B-RM2 to J16
Segment Flow Rate (gpm)
Line Length (ft)
865
Line Size ID (in.))
Minor Losses from Check Valve
Friction Headloss (ft)
6.497
Line Velocity (ft/s)
2.16
J16 to J20
Segment Flow Rate (gpm)
=
Line Length (ft)
3320
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.262
Line Velocity (ft/s)
1.91
J20 to W WTF
Segment Flow Rate (gpm)
' z
Line Length (ft)
3503
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.883
Line Velocity (fUs)
1.91
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 613-28
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
399.0
172.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
101.0
43.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
209.6
90.8
Flush Pressure at backwash tank for Min. Flush Rate
606.9
262.7
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
71.0
51.2
Pressure at manifold before PRV
451.1
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
127.1
5 0 ;
Low Pressure Check: P at Min. Flush Flow at Return Manifold
45.1
19.5
Flush Pressure at WWTF for Min. Flush Rate
284.4
123.1
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
146.6 1
63.5
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curare.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U da.s�)
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 4B-29
No. Laterals:
7
Tubing: ID (in)
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
5018
Design Flow (gpm :
25.93
Application Flow (gpm):
25.9
Min. Design Scour Vel. ft/s
2.0
Tubing ID in
0.787
Residual Flow for Scour (gpm)'
2.30
Req'd Flush Rate (gpm)':
48.9
Supply Manifold Elev.
4B-SM1
Return Manifold Elev.
4B-RM2
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Length
# Emitters
Flow (gpm)7
Length (ft)
Dose m)
Flow g m)e
1 1
19
0.2
534
2.8
5.1
2
32
0.3
3
45
0.5
4
55
0.6
5
58
0.6
6
58
0.6
2
74
0.8
616
3.2
5.5
74
0.8
80
0.8
80
0.8
3 11
101
1.0
406
2.1
4.4
12
102
1.1
13
102
1.1
410
2.1
4.4
14
103
1.1
15
104
1.1
418
2.2
4.5
16
105
1.1
17
106
1.1
426
2.2
4.5
18
107
1.1
4
98
1.0
610
3.2
5.5
71
0.7
69
0,7
67
0.7
5 23
76
0.8
580
3.0
5.3
24
72
0.7
25
72
0.7
26
70
0.7
6
68
0.7
492
2.5
4.8
65
0.7
59
0.6
_
54
0.6
7 31
49
0.5
526
2.7
5.0
32
43
0.4
33
39
0.4
34
35
0.4
35
30
0.3
36
26
0.3
37
23
0.2
38
18
0.2
5018 2509 25.9 2b.y
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

F
10/20/2008
PRESSURE ANALYSIS
6111111
TOP FEED MANIFOLD SYSTEM
ZONE 4B-29
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE Inputs
Dose Flow (a)
Flush Flow (b)
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.007
0.001
2 Total Segment Headloss (ft) = Friction + Elev.
12.007
12.001
Hydraulic Unit
H.U. Elev mom
3 Headloss from H.0 (ft.)3
MEMEMEM
Supply Force Main Friction Losses
H.U. to J20
- Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
4 Friction Headloss (ft)
5.061
0.920
Minor Losses (ft)
0.506
0.092
Line Velocity (ft/s)
1.51
0.60
J20 to A 6
Segment Flow Rate (gpm)
_g ���
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
0.209
0.679
i
Minor Losses (ft)
0.021
0.068
Line Velocity (ft/s)
0.29
0.54
J16 to 4B-SM1
Segment Flow Rate (gpm)
- -
-
�,
Line Length (ft)
Line Size ID (in)5
B
6 Friction Headloss (ft)
2.144
6.949
Minor Losses (ft)
0.214
0.695
Line Velocity (ft/s)
1.12
2.12
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold 254
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold"
wi
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold°
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.453
4.518
9 Total Segment Headloss (ft) = Friction + Elev.
-30.547
-34.482
s�q
Return Force Main Friction Losses
4B-RM1 to J16
Segment Flow Rate (gpm)
- k
Line Length (ft)
1230
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
4.958
i :..
Line Velocity (ft/s)
1.54
J76 to J20
Segment Flow Rate (gpm)
Line Length (ft)
3320
Line Size ID (in.)
Minor Losses (ft)
1.237
Friction Headloss (ft)
Line Velocity (ft/s)
0.58
J20 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
3503
Line Size ID (in.)
—
Minor Losses (ft)
Friction Headloss (ft)
1.305
Line Velocity (ft/s)
0.58
Willi
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4B-29
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
379.5
164.3
Low Pressure Check: P at Min. Flush Flow at Return Manifold
125.5
54.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
243.4
105.4
Flush Pressure at backwash tank for Min. Flush Rate
631.8
273.5
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
104.8
51.2
Pressure at manifold before PRV
466.8
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
23.5
10.2
Flush Pressure at WWTF for Min. Flush Rate
276.0
119.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
139.0 1
60.2
Brooks Engineering Associates, PA p.3 of 3
w5.:.
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes .& Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: ht = (4.727 U d4.17) (Q/C)1.85
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 313-30
Application Flow (Ppm):
95.1
No. Laterals:
48
Min. Design Scour Vel. ft/s)
2.0
Tubing: ID (in)
0.79
3B-RM1
Run
Tubing ID (in)
0.787
Emitters h :
0.62
Residual Flow
Re 'd Flush
for Scour (gpm)a
2.30
Emitter Spacing ft2
Rate m e:
205.5
Total Footage: 18398
Length (ft)
Dose(gpm)
Design Flow pm): 95.06
Supply Manifold Elev.
3B-SM1
Supply Manifold
Elev.
3B-SM2
Return Manifold
Elev.
Run
3B-RM1
Run
Return Manifold
Dose
Elev.
Lateral
Lateral
3B-RM2
Min. Flush
Lateral
Run
Elev.
Len th
# Emitters
Flow (gpm)7
Length (ft)
Dose(gpm)
Flow (gpm)'
1
1
156
1.6
1 312
1.6
3.9
2
2
167
1.7
334
1.7
4.0
3
3
169
1.7
338
1.7
4.0
4
4
171
1.6
342
1.8
4.1
5
5
173
1.8
346
1.8
4.1
6
6
175
1.8
350
1.8
4.1
7
7
177
1.8
354
1.8
4.1
8
8
179
1.8
358
1.8
4.1
9
9
182
1.9
364
1.9
4.2
10
10
183
1.9
366
1.9
4.2
11
11
184
1.9
368
1.9
4.2
12
12
185
1.9
370
1.9
4.2
13
13
185
1.9
370
1.9
4.2
14
14
185
1.9
370
1.9
4.2
15
15
186
1.9
372
1.9
4.2
16
16
186
1.9
372
1.9
4.2
17
17
187
1.9
374
1.9
4.2
18
18
188
1.9
376
1.9
4.2
19
19
188
1.9
376
1.9
4.2
20
20
190
2.0
380
2.0
4.3
21
21
192
2.0
384
2.0
4.3
22
22
194
2.0
388
2.0
4.3
23
23
196
2.0
392
2.0
4.3
24
24
199
2.1
398
2.1
4.4
25
25
202
2.1
404
2.1
4.4
26
26
205
2.1
410
2.1
4.4
27
27
209
2.2
418
2.2
4.5
28
28
212
2.2
424
2.2
4.5
29
29
216
2.2
432
2.2
4.5
30
30
220
2.3
440
2.3
4.6
31
31
217
2.2
434
2.2
4.5
32
32
216
2.2
432
2.2
4.5
33
33
216
2.2
432
2.2
4.5
34
34
217
2.2
434
2.2
4.5
35
35
215
2.2
430
2.2
4.5
36
36
214
2.2
428
2.2
4.5
37
37
213
2.21
426
2.2
4.5
38
38
208
2.1
416
2.1
4.4
39
39
204
2.1
408
2.1
4.4
40
40
200
2.1
400
2.1
4.4
41
41
197
2.0
394
2.0
4.3
42
42
193
2.0
386
2.0
4.3
43
43
188
1.9
376
1.9
4.2
44
44
183
1.9
366
1.9
4.2
45
45
178
1.8
356
1.8
4.1
46
46
172
1.8
344
1.8
4.1
47
47
166
1.7
332
1.7
4.0
48
48
161
1.7
322
1.7
4.0
18398
9199
95.11
95.1
205.5
i,
Brooks Engineering Associates, PA p.1 of 3
Imi
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 36-30
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
I Inputs Dose Flow(a Flush Flow b)
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.Z
0.005
0.019
2 Total Segment Headloss (ft) = Friction + Elev.
12.005
12.019
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
4 Friction Headloss (ft)
2.324
9.667
Minor Losses (ft)
0.232
0.967
Line Velocity (ft/s)
1,17
2.53
Supply force Main Elevation Delta
5 Elevation (ft) from H.U. to Manifold
66
Drip System Headloss Results
6 Total Headloss (ft.) in drip system from supply manifold to return manifold "t..
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)'
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.587
2.378
7 Total Segment Headloss (ft) = Friction + Elev.
-50.413
-55.622
Return Force Main Friction Losses
3B-SM2 to WWTF
Segment Flow Rate (gpm)'
Line Length (ft)
2585
Line Size ID (in.)
Minor Losses (ft)
8 Friction Headloss (ft)
17.538
Line Velocity (ft/s)
2.78
Return Line Elevation Delta
9 Elevation (ft) from Return Manifold to WWTF
1 Brooks Engineering Associates, PA p.2 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3B-30 SUBMANIFOLD 3B-SM2
316.3
51.2
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min, Flush Rate at Return Manifold
160.7
69.6
Low Pressure Check: P at Min. Flush Flow at Return Manifold
331.3
143.4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
454.9
196.9
Flush Pressure at backwash tank for Min. Flush Rate
446.8
193.4
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
316.3
51.2
Pressure at manifold before PRV
470.4
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
45.0`
Low Pressure Check: P at Min. Flush Flow at Return Manifold
44.0
19.0
Flush Pressure at WWTF for Min. Flush Rate
94.4
40.9
Hi h Pressure Check: Emitter P on Bottom Lateral at Dose Flow
147.4
63.8
Note: Return Flush Tank needed. See Pressure Calcs for Zone 3B-30 Submanifold 1.
Brooks Engineering Associates, PA
p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3B-30 SUBMANIFOLD 3B-SM1
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
98.7
42.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
393.3
170.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
517.0
223.8
Flush Pressure at backwash tank for Min. Flush Rate
382.8
165.7
PRV NEEDED? YES
ZONE SUMMARY All PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
378.4
51.2
Pressure at manifold before PRV
470.4
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
104.0
45.0-
5.0 °Low
LowPressure Check: P at Min. Flush Flow at Return Manifold
44.0
19.0
Flush Pressure at WWTF for Min. Flush Rate
30.4
13.2
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
147.5
63.9
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush.
Brooks Engineering Associates, PA P.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit, .
a flushing flow velocity of 2 ft1s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: ht = (4.727 L/ d4b) (Q/C)1.86
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Re uired Flush Rate plus the Dose Flow Rate
Zone:F-6-AA-1-1 Application Flow m): 50.4
No. Laterals: 18 Min. Design Scour Vel. (foal 2.0
Tubing: ID in 0.79 Tubin ID in EEIF0.787
Emitters h : 0.62 Residual Flow for Scour ( m)s 2.30
Emitter S acin ft 2 Re 'd Flush Rate (pm)s: 91.8
Total Foota e: 9760
Daskin Flow m : 50.43
Supply Manifold Elev. 6A-SM5
Return Manifold Elev. 6A -RMS
Supply Manifold Elev. 6A-SM4
Return Manifold Elev. 6A-RM4
Supply Manifold Elev. 6A-SM3
Return Manifold Elev. 6A-RM3
Run Run Dose Lateral Lateral Min. Flush
teral Run
Elev. Lenrith # Emitters Flow m)'
Lenath (ft)
Dose m)
Flow (gpm'
1 1
158 1.6
630
3.3
5.6
2
157 1.6
2 3
157 1.6
628
3.2
5.5
4
157 1.6
3 5
156 1.6
622
3.2
5.5
6
155 1.6
4 7
154 1.6
616
3.2
5.5
8
154 1.6
5 9
153 1.6
612
3.2
5.5
10
153 1.6
6 11
124 1.3
496
2.6
4.9
12
124 1.3
7 13
126 1.3
506
2.6
4.9
14
127 1.3
8 15
129 1.3
518
2.7
5.0
16
130 1.3
9 17
131 1.4
526
2.7
5.0
18
132 1.4
10 19
134 1.4
538
2.8
5.1
20
135 1.4
11
67 0.7
622
3.2
5.5
54 0.6
51 0.5
48 0.5
46 0.5
45 0.5
12
44 0.5
514
2.7
5.0
45 0.5
45 0.5
45 0.6
46 0.5
32 0.3
13
49 0.5
392
2.0
4.3
49 0.5
49 0.5
49 0.5
14 37
49 0.5
598
3.1
5.4
38
50 0.5
39
50 0.5
40
50 0.5
41
50 0.5
42
50 D.5
15 43
51 0.5
612
3.2
5.5
44
50 0.5
45
510.5
46
51 0.5
47
51 0.5
48
52 0.5
16 49
52 0.5
624
3.2
5.5
50
52 0.5
51
52 0.5
52
52 0.5
53
52 0.5
54
52 0.5
17 55
49 0.5
488
2.5
4.8
56
45 0.5
57
42 0.4
58
39 0.4
59
36 0.4
60
33 0.3
18 61
31 0.3
218
1.1
3.4
62
28 0.3
63
26 0.3
Brooks Engineering Associates, PA p.1 of 3 11/18/2008

ftp
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE SA-31
TOP LOAD MANIFOLD PRESSURE ANALYSIS
�..
INPUT
LINE
I Inputs I Dose Flow fall Flush Flow Ib
1 Operating Head from Pump Curve'
1,
I
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U.'
WWI
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U'
0.010
0.011
2 Total Segment Headloss (ft) = Friction + Elev.
12.010
12.011
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.? .
Supply Force Main Friction Losses
H.U. to 38-SM2
Segment Flow Rate (gpm)
6
Line Length (ft)
Line Size ID (in?
4 Friction Headloss (ft)
5.052
5.635
Minor Losses (ft)
0.505
0.564
Line Velocity lift(s)
1.78
1.89
3BSM2 to 3BSM1
Segment Flow Rate (gpm)
Line Length (ft)
j
I
Line Size ID (ln0
�q
0.410
0.458
5 Friction Headloss (ft)
Minor Losses (ft)
0.041
0,046
Line Velocity (ft/s)
1.78
1.89
3BSM1 to 6A-SM3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
Room
6 Friction Headloss (ft)
0.731
2.174
Minor Losses (ft)
0.073
0.217
Line Velocity (itis)
1.30
2.35
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
-174
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return
manifold`
6A-31_SM-3 Feed Manifold to Bottom Lateral
Headloss (ft) in manifold'
I
Line Length (ft) from Supply Manifold to Bottom Feed Lateral s
Im
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateran
0.000
0.000
9 Total Segment Headloss (ft)= Friction +Elev.
.49.000
-56.000
Return Force Main Friction Losses
6A-RM3 to 3B -SMI
Segment Flow Rate (gpm)
Line Length (ft)
440
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
5.261
Line Velocity (itis)
2.78
3B -SMI to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft)
210
Line Size ID (in.)
Minor Losses (ft)
71
Friction Headloss (ft)
0.515
Line Velocity (ft/s)
1.61
38-SM2 to W WTF
Segment Flow Rate (gpm)
Line Length (k)
2585
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
6.341
Line Velocity (Itis)
1.61
Return Line Elevation Delta
Elevation (ft) from Return Manifold to W WTF
Brooks Engineering Associates, PA p.2 of 3 11/1812008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-31 SUBMANIFOLD 6ASM3
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
45.7
-19.8
Low Pressure Check: P at Min. Flush Flow at Return Manifold
546.7
236.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
696.2
301.4
Flush Pressure at backwash tank for Min. Flush Rate
200.0
86.6
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
557.6
51.2
Pressure at manifold before PRV
473.2
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
20.5
8.9
Flush Pressure at W WTF for Min. Flush Rate
-151.6
-65.6
Hi h Pressure Check: Emitter P on Bottom Lateral at Dose Flow
157.5
68.2
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure
to return the
flush.
Brooks Engineering Associates, PA p.3 of 3 11/182008

Brooks Engineering Associates, PA
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-31 Submanifold 6A-SM4
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
10.3
Low Pressure Check: P at Min. Flush Flow at Return Manifold
- 490.7
LO
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
624.2Flush
Pressure at backwash tank for Min. Flush Rate
254.0
PRV NEEDED? YES
ZONE SUMMARY WI PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
485.6
512
Pressure at manifold before PRV
4732
117.7
PRV setfing calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
20.5
8.9
Flush Pressure at W WTF for Min. Flush Rate
-97.6
.42.3
Mich Pressure Check: Emitter P on Bottom Lateral at Dose Flow
141.5
61.3
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush
p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A31 SUBMANIFOLD SA -SMS
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
72.3
31.3
Low Pressure Check: P at Min. Flush Flow at Return Manifold
428.7
185.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
570.2
246.8
Flush Pressure at backwash tank for Min. Flush Rate
306.0
132.5
PRV NEEDED? YES
ZONE SUMMARY WI PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
431.6
51.2
Pressure at manifold before PRV
473.2
117.7
PRV setting calculated (pressure at manifold - pressure lass required)
154.3
66.5
PRV setting utilized
115.5
•' 5'0.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
20.5
8.9
Flush Pressure at WWTF for Min. Flush Rate
-45.6
-19.7
Hiah Pressure Check: Emitter P on Bottom Lateral at Dose Flow
149.5
64.7
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush
Brooks Engineering Associates, PA p.3 of 3
10/20/2008

5
8
e
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U da.e7)
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 6A-32
No. Laterals:
12
Tubing: ID in
0.79
Emitters h :
0.62
Emitter Spacing ft
2
Total Footage:
6350
Design Flow m):
32.81
Supply Manifold Elev. 6A-SM2
Return Manifold Elev. 6A-RM2
Run Run
Lateral Run Elev. Length
1
2 7
8
9
10
11
12
3 IN,
4 17
18
5 19
20
6 21
22
7 23
24
8 25
26
9 27
28
10 29
30
11 31
32
12 33
34
35
36
37
38
Ap lication Flow (gpm):
32.8
Min. Design Scour Vel. ft/s)
2.0
Tubing ID in
0.787
Residual Flow for Scour (gpm)e
2.30
Req'd Flush Rate (gpm)5:
60.4
32M
TOR
Brooks Engineering Associates, PA p.1 of 3 10/20/2008
Supply Manifold Elev.
6A-SM1
Return Manifold Elev.
6A-RM1
Dose Lateral
Lateral
Min. Flush
# Emitters Flow (gpm)' Length (ft)
Dose (gpm)
Flow (gpm)°
42
0.4 530
2.7
5.0
43
0.4
44
0.5
44
0.5
45
0.5
47
0.5
48
0.5 646
3.3
5.6
50
0.5
53
0.5
56
0.6
57
0.6
59
0.6
60
0.6 540
2.8
5.1
66
0.7
70
0.7
74
0.8
78
0.8 322
1.7
4.0
83
0.9
94
1.0 400
2.1
4.4
106
1.1
112
1.2 520
2.7
5.0
148
1.5
157
1.6 622
3.2
5.5
154
1.6
152
1.6 604
3.1
5.4
150
1.6
146
1.5 578
3.0
5.3
143
1.5
140
1.4 552
2.9
5.2
136
1.4
i 128
1.3 502
2.6
4.9
123
1.3
67
0.7 534
2.8
5.1
57
0.6
50
0.5
44
0.5
37
0.4
12
0.1
32M
TOR
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

10/20/2008
PRESSURE ANALYSIS
1
TOP FEED MANIFOLD SYSTEM
ZONE 6A-32
j
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINEInputs
Dose
Flow a)
Flush Flow b
i
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P.T. to H.U'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 2
0.010
0.011
2 Total Segment Headloss (ft) = Friction + Elev.
12.010
12.011
Hydraulic Unit
?q
H.U. Elev MOM
3 Headloss from H.0 (ft.)3
MEMEMEM
Supply Force Main Friction Losses
H.U. to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft))
Line Size ID (in)5
�l
4 Friction Headloss (ft)
5.052
5.635
Minor Losses (ft)
0.505
0.564
I
Line Velocity (ft/s)
1.78
1.89
3B-SM2 to 3B-SM1
Segment Flow Rate (gpm)+:
Line Length (ft)
Line Size ID (in)s
5 Friction Headloss (ft)
0.410
0.458
Minor Losses (ft)
0.041
0.046
Line Velocity (ft/s)
1.78
1.89
3B-SM1 to 6A-SM3
Segment Flow Rate (gpm)
t
Line Length (ft)
Line Size ID (1n)5
6 Friction Headloss (ft)
0.731
2.174
Minor Losses (ft)
0.073
0.217
Line Velocity (ft/s)
1.30
2.35
f
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
18
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold°MONEINEERM
���
6A -32 -SM -1 Feed Manifold to Bottom Lateral
Headloss (ft) in manifold°
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
r
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID,(in)s
y
Friction Headloss (ft) from Manifold to Bottom Feed Latera13
1.333
4.313
9 Total Segment Headloss (ft) = Friction + Elev.
-41.667
-45.687
Return Force Main Friction Losses
.!
6A-RM3 to 3B-SM1
J
Segment Flow Rate (gpm)
Line Length (ft)
440
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
5.261
Line Velocity (ft/s)
2.78
I ,!
3B-SM1 to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft)
210
�
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
0.515
Line Velocity (ft/s)
1.61
3B-SM2 to WWTF
Segment Flow Rate (gpm)
(-
Line Length (ft)
2585
I
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
6.341
Line Velocity (ft/s)
1.61
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3
(i
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-32 Submanifoid 6A-SM1
Feet
358.2
PSI
51.2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
143.3
62.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
357.7
154.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
496.8
215.1
Flush Pressure at backwash tank for Min. Flush Rate
383.0
165.8
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
358.2
PSI
51.2
Pressure at manifold before PRV
473.2
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
23.5
10.2
Flush Pressure at WWTF for Min. Flush Rate
31.4
13.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
150.2
65.0
Note: Return Flush Tank needed. Flush Pressure at WWTF is too low. May not have sufficient pressure to return the flush,
Brooks Engineering Associates, PA p.3 of 3 10/2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-32 Submanifold 6A-SM2
304.2
51.1
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
187.3
81.1
Low Pressure Check: P at Min. Flush Flow at Return Manifold
313.7
135.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
442.8
191.7
Flush Pressure at backwash tank for Min. Flush Rate
427.0
184.8
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
304.2
51.1
Pressure at manifold before PRV
473.2
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.0'
Low Pressure Check: P at Min. Flush Flow at Return Manifold
23.5
10.2
Flush Pressure at WWTF for Min. Flush Rate
75.4
32.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
140.2
60.7
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush.
Brooks Engineering Associates, PA p.3 of 3
Itai
10/20/2008

IN
Brooks Engineering Associates, PA p.1 of 3 10/20/2008
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Encineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 fVs is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in
Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hr = (4.727
U d4.11) (DjC)t.es
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
8 Equals the Required Flush Rate Plus
the Dose Flow Rate
Zone: 8833
AD loation Flow (ppm):
59.6
No. Laterals: 30
Min. DeskinScour Vel. fy.)
2.0
Tubin : ID in 0.79
Tubin ID in
0.787
Emitters h: 0.62
Residual Flow for Scour( pm)s
2.30
Emitter 6 acin it2
Req'd Flush Rate ( pm)'
128.6
Total Footage: 11528
Design Flow (qpml, 59.56
supply Manifold Elev. 68SM3
Return Manifold Elev. 6B-RM3
Supply Manifold Elev. 68-SM2
Return Manifold Elev. 6B-RM2
Supply Manifold Elev. 6BSM1
Return Manifold Elev. 6B-RM1
Run Run Dose Lateral Lateral
Min. Flush
Lateral Run Elev. Length # Emitters Flow f. pnn� Length (ft) Dose qpm)
Flow rn?
1 1 74 0.8 628
3.2
5.5
2 77 0.8
3 80 0.8
4 83 0.9
2 5 87 0.9 354
1.8
4.1
6 90 0.9
3 7 92 1.0 376
1.9
4.2
8 96 1.0
4 9 98 1.0 398
2.1
4.4
10 101 1.0
5 11 104 1.1 414
2.1
4.4
12 103 1.1
6 13 101 1.0 400
2.1
4R
14 99 1.0
7 15 98 1.0 388
2.0
4.3
16 96 1.0
8 17 96 1.0 380
2.0
4.3
18 94 1.0
9 19 93 1.0 372
1.9
4.2
20 93 1.0
10 21 92 1.0 368
1.9
4.2
22 92 1.0
11 23 910.9 364
1.9
4.2
24 91 0.9
12 25 91 0.9 364
1.9
4.2
26 91 0.9
13 27 90 0.9 360
1.9
4.2
_
28 90 0.9
14 29 89 0.9 356
1.8
4.1
30 89 0.9
15 31 88 0.9 352
1.8
4.1
32 88 0.9
16 33 88 0.9 350
1.8
4.1
34 87 0.9
17 35 87 0.9 348
1.8
4.1
36 87 0.9
18 37 86 0.9 346
1.8
4.1
38 87 0.9
19 39 87 0.9 348
1.8
4.1
40 87 0.9
20 41 87 0.9 348
1.8
4.1
42 87 0.9
21 43 87 0.9 348
1.8
4.1
44 87 0.9
22 45 87 0.9 346
1.8
4.1
46 86 0.9
23 47 85 0.9 340
1.8
4.1
48 85 0.9
24 49 86 0.9 344
1.8
4.1
50 86 0.9
25 51 86 0.9 342
1.8
4.1
52 85 0.9
26 53 83 0.9 328
1.7
4.0
_
54 81 0.8
27 55 80 0.8 316
1.6
3.9
56 78 0.8
28 57 75 0.8 592
3.1
5.4
58 74 0.8
59 74 0.6
60 73 0.8
29 61 70 0.7 518
2.7
5.0
62 66 0.7
63 63 0.7
64 60 0.6
30 65 58 0.6 440
2.3
4.6
IN
6s 56 0.6
67 54 0.6
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4B-34 Submanifold 4B-SM3
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
11.3
4.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
493.7
213.7
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
611.6
284.8
Flush Pressure at backwash tank for Min. Flush Rate
259.0
112.1
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
473.0
51.2
Pressure at manifold before PRV
468.2
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
50.0 ..
Low Pressure Check: P at Min. Flush Flow at Return Manifold
25.5
11.0
Flush Pressure at W WTF for Min. Flush Rate
-96.6
-41.8
Hiah Pressure Check: Emitter P on Bottom Lateral at Dose Flow
139.9
60.8
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush.
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

1.7 Irrigation Schedule Spreadsheet

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2.0 Bulletins
Bulletin A Aqueonics Plant Cut -Sheets for: concrete mix design, railing,
chemical feed pumps, Parkson sand filter and air compressor, DuraPac
trickling filter media, Trojan UV, level controller and tranduscers,
chemical feed pumps and pressure relief valves.
Bulletin B — Cut -Sheets and Pump Curves for WWTP Pumps: forward
flow/recycle pumps, sand filter flow pumps, equalization tank grinder
pumps, sludge tank decanting pump.
Bulletin C — Cut -Sheets for WWTP Blowers
Bulletin D — Cut -Sheets and Pump Curve for Irrigation Dosing/Flushing Pump
Bulletin E — Cut -Sheets for Flushing Return Pumps and Tanks
Bulletin F — Cut -Sheets for Alternate Pond Liner
Bulletin G — WSI PC Controller Electrical Schematics
Bulletin H — Cut -Sheets for Drip System Valving
Bulletin I Cut -Sheets for Flow Meter
Bulletin J - Cut -Sheets for Disc Filtration System
Bulletin K - Cut -Sheet for Rainbird Rain Gauge
Bulletin L - Drip Line Cut Sheets
Bulletin M - Pole Blower Curve and Cut -Sheet
Bulletin N - Back -Up Generator Cut -Sheets
Bulletin O — Turbidity Meter
E

BULLETIN A
Aqueonics Plant Cut -Sheets for: concrete mix design, railing, chemical feed
pumps, Parkson sand filter and air compressor, DuraPac trickling filter media,
Trojan UC, level controller and transducers, chemical feed pumps and pressure
relief valves.

MARION CENTER. SUPPLY, INC.
READY MTX- C.ONCRE 1 E
P.O. BOX 173
MARION CENTER, PA 15759
[phone] Fax [phone]
WEBSITE: WWW.MARIONCENTERSUPPLY,COM
DATE: 14 -Aug -08 N -st `z !'' 1 t x � 6, IJ
Z7 --Al P L'� � E)
PROJECT, Treatment Plant
Slump (inches): 4" Maximum
Calcul2ted Unit Weight (pC�' 145,60
Water l Ratio: 0.35
Marion Center Supply will not be held responsible for any type of cracking_ Cracking
Is a natural thing which we have absolutely no control over-
*** ADMIXTURE NOTES **'
1. At ambient temperatures below 75 degrees, 3 az/cwt of 20ON
2. At ambient temperatures from 75 - 85 degrees, 3 oz/cwt of 100XR
B. At ambient temperatures above 85 degrees, 4 ozlcwt of 1 DOXR
MATERIALS SOVIRCE
ASTM
TYPE
DOSAGE
Cement; Cemex, Fttsburgh/ Wampum, PA
C-150
Illi
n/a
1:XL Select- RM Excell Minerals, Sarver, PA
0114&1157
nia
Coarse Aggregate: Hansen Aggregates, Torrance, PA
C-33
957
n/a
Fine Aggregate. Glacial Sand & Gravel, Tarrtown, PA
C-33
A
nfa
Wafer: Onsite Well
n/a
potable
n/a
1 Mai
Air Entraining. Master Builders Inc„ MBAE 90
C-260
n/a
As Required
Water Reducer. Master Builders Inc., Pozzolith 20ON
C-494
A -B -D
See Below
Retarder: Master Builders Inc,, Pozzolith 100XR
C-494
B -D
See Below
Super Plastickder Master Builders Inc., Gienium 3030 NS
C-494
A F
As Required
I.:I
Non Chloride Aco, Master Builders Inc,, Pozzolity NC Sad
C-494
C -E
As Required
MIX [DESIGN 4000 psi Air Entrained
Material Weight Gallons S.G. Volume
(Ibs,) (ru, ft.)
Cement 420 3.15 2.14
EXL Select - RM 140 2.90 0.77
Coarse Aggregate 1800 2.68 10,76
Fine Aggregate 1376 2.57 8,58
fob
Water 195 23.41 1.00 3.13
Air 6.Ow1,5°/a 6.00°!0 1.62
®
TOTAL 3931 27.00
Slump (inches): 4" Maximum
Calcul2ted Unit Weight (pC�' 145,60
Water l Ratio: 0.35
Marion Center Supply will not be held responsible for any type of cracking_ Cracking
Is a natural thing which we have absolutely no control over-
*** ADMIXTURE NOTES **'
1. At ambient temperatures below 75 degrees, 3 az/cwt of 20ON
2. At ambient temperatures from 75 - 85 degrees, 3 oz/cwt of 100XR
B. At ambient temperatures above 85 degrees, 4 ozlcwt of 1 DOXR

SCC6SPL ,'s- L, t'>' m)e—fz
r
Valley City:
Cement
488 lb
3.15 Sp Gr
62.4
2.48 ft3
Fly Ash
102 Ib
2.35 Sp Gr
62.4
0.70 ft3
Slag Cement
0 Ib
2.35 Sp Gr
62.4
0.00 ft3
Gravel 57
840 Ib
2.64 Sp Gr
62.4
5.10 ft3
Gravel 8
560 Ib
2.64 Sp Gr
62.4
3.40 ft3
Concrete sand
1568 Ib
2.64 Sp Gr
62A
9.52 ft3
Water gl
30.50 254.065 Ib
1 Sp Gr
62.4
4.07 ft3
Air
7% 1.89
1
1
1.89 ft3
6100
48 oz
APA14
6 oz
NC
50 oz If Needed
Plastiment
15 oz If Needed
27,16 ft3
Comments:
water/cem coarse/fine cem/f/a total agg
agg cu.ft.
2968
590 1400.00
0.43 0.53
22% 40%
8.50

- 07�
r
Valley City:
Cement
530 Ib
3.15 Sp Gr
62.4
2.70 ft3
Fly Ash
110 Ib
2.35 Sp Gr
62.4
0.75 ft3
Slag Cement
0 Ib
2.35 Sp Gr
62.4
0.00 ft3
Gravel 57
840 Ib
2.64 Sp Gr
62.4
5.10 M
Grave! 8
560 Ib
2.64 Sp Gr
62.4
3.40 ft3
Concrete sand
1428 ib
2.64 Sp Gr
62.4
8.67 ft3
Water gl 34.00
283.22 Ib
1 Sp Gr
62.4
4.54 ft3
Air 7%
1.89
1
1
1.89 ft3
6100
48 oz
AEA14
4 oz
NC
50 oz if Needed
Plastiment
15 oz if Needed
27.04 ft3
Comments:
water/cem coarse/fine cemlfla total agg
agg cu.ft.
2828
640 1400.00
0.40 0.50
22% 40%
8.50

N
1 Cat 1A S1 p OnFittings 2/15/04 12:39 PM Page 1
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R14 Wb 0Z_
tw4ellsender.
Your Handrail Source.
Structural Slip -Do fittings used with aluminum, galvanized steel, stainless steel and
black iron pipe an installations around the world top over fifty years.
Hollaender Products are produced from only the highest
quality materials and feature proprietary fasteners
and design features.
Aluminum Allay 535
• ivlost corrosive resistant aluminum casting alloy
available today
• High strength as cast
• Bright, attractive burnished mill finish
• Conforms to ASTM B26 & BI 79
Proprietary Internal/External Reverse Knurl Cup
Point Set Screw
• Knurl cup point design provides tremendous resist-
ance to loosening due to heavy vibration
• Full contact of point greatly resists pullout and
rotational slip
• Conforms to FF -S-200, ANSIIASNiEBIS.3
Type CIG
The Hollander Advantage
• Speed of Installation —Studies have shown
significant cost savings when compared to the
cost of welded handrail and other structures
• Ease of Installation —Only tools required are a
saw, hex key and tape measure
• Flexibility — Cast fittings can be used with galva-
nized steel, aluminum, stainless steel and black
iron pipe
• Reusability — Structures fabricated with
Hollaender fittings can easily be disassembled
and reconfioured
The Rib® Design
Hollaender®
Speed -Railer
Nu -Rada
Speed -Railer II
Rackmastera
Mend-A-RailO
Interna -Rail'•
Bumble Bee'
AH are registered trademarks of the
Hollaender Manufacturing Company.
Call Tali Free; 800.772-8800 • www bollaeader.com
rmt� T
t;�V!
• Strength — Railing systems can be designed using
standard Hallaender products to meet any building
code. Please refer to Technical Section of Catalog,
www.hoilaendercom or call our engineers.
• Time Tested — Products are backed by over 50
years of experience
Hogaendep features the Worids hest known brands
Speed -Rail"
Inline design has become the benchmark for quality
throughout the industry.
Nu -Rail•
Offset design of heavier duty structural fittings allows
multiple pieces of pipe to cross, minimizing number
of cuts.
Rackmaster•
Heaviest duty line developed for the construction of
rack systems.
Mend-A-RailO
Ideal for repairing broken welds on existing pipe
structures.
Speed -Rail" Il
Patented modular fitting system which easily allows
for additions and changes to existing structures
without having to entirely disassemble.
Applications are limited only by the imagination
Handrails & guardrails, playgrounds and carts,
store fixtures, offshore petro/chemical, industrial
plants, racking systems, warehouses, health &
medical buildings, portable structures, recreational
areas, amusement parks, film industry, government
facilities & public works, displays, and much,
much more.
Instant Structures

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Cat 1A Slip-OnFittings 2/16/04 12:39 PM Page 2
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Outlet Tee —
#47 Rectangular Range
Call Toil Free; 800-772.2300 • www,hollaendeccom
Notes:
• Handrail post must be installed as one piece.
Never splice post at mid -rail.
• Top -rail should be spliced using an internal
or external splice.. Never splice inside a
single set screw tee (5E).
"The Fitting nth the Rib"'

FF
05060
I'
06060
1-1/4"
01060
1.112"
08060
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US. Size Iiem Number
3/4° 15000
1.1/4° 11000
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Your Handrail Source.
I.P.S. Size Item Number
3/4'
05060
I'
06060
1-1/4"
01060
1.112"
08060
I.P.S. Size Item Number
2° 09010
I.P.S. Size Item Number
1-1/4' 01000
1-1/2" 08080
I.P,S. Size Item Number
3/4'
05090
t"
06090
01090
08090
2
09000

011mander.
Your Handrail Source.
Call Tall Free: 800-772-8000+ www.hollaender,com
Cat 3A Flames 2(16101 12:49 PM Page
1
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Hollaender offers an extensive line of flanges for
mounting handrail, guardrail, and other pipe structures.
These flanges are available in all the optional
finishes. Selecting the right flange becomes extremely
MRM
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important in all handrail applications. To aid in the
selection process, please refer to the chart on the
following page, and dimensional drawings on the
subsequent pages.
�a
Our engineering staff is available m answer questions
regarding the appropriate hardware. Concrete
a
anchors and machined bolts maybe ordered to
complete the handrail system. Many applications
require toeplate. (Refer to Tech Information section,
building codes and OSHA standard pipe railing for
requirements.)
Refer to our accessories section for our toeplate and
toeplate brackets. Please refer to our web page at
www.hollaender.com for additional technical support
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011mander.
Your Handrail Source.
Call Tall Free: 800-772-8000+ www.hollaender,com

0
" , Sulzer CompaXTm
The space -saving solution
Sulzer Chemtech
3
Sq
ate:
dA6 aY. vt
� 9tt

M
M
01"
CampaX`117%chno�ogy
Sulzer CompaXTm
for turbulent flow
Sulzer CompaX is the name for the new, space -saving
and efficient solution to your mixing problems in the
turbulent flow regime. In comparsion to conventional
static mixer configurations, the Sulzer CompaX has
an amazingly reduced overall length. This greatly im-
proves your operational flexibility and reduces installa-
tion costs. Further more the additive can be admixed in
an easy and reliable way.
Functional description
The patented Sulzer CompaX design consists of a
highly efficient mixing device with integrated dosing in-
let point. The additive is fed into the zone where strong
turbulent flow prevails.
This design secures homogeneous mixing over a very
short distance with the use of only one mixing element
and with only one additive dosing point.
The Sulzer CompaX is patented technology.
Field of application
The Sulzer CompaX is widely used for the inline mixing
of liquids, gases and suspensions in the turbulent flow
regime.
Outstanding features
The following features make the Sulzer.CompaX an
advantageous and efficient solution to.your mixing
needs:
• very short mixing distance independent -of
mixing ratio, a homogeneous mixture is achieved
only.3 pipe diameters .downstream. of the mixer
• low pressure drop (typically 10 —100 mbar)
• extremely short overall installation length
(approx. 0.3 pipe -0)
• easy to fit, low installation costs
• simple dosing of additive: no multipoint dosing
system necessary
• no clogging (both in the main flow and in additive
stream)
• robust construction, no moving parts
• easy to clean
• excellent price/performance ratio

Main fio
—0.
Homogeneity data
1
0.01
1000
9 100
0
a
1
0,1 0,5 1
Velocity (In s)
iSulzer CompaX
O 11 :2000
• t: too
8 1:20
UD [-1
Homogeneity curve measured at different mixing ratios
calculation of the homogeneity with CFD (Computational Fluid Dynamics)
Pressure drop (lip)
The pressure drop can be calculated as follows:
Ap=0.015pv2
©p = pressure drop (mbar)
p = density (kg/m3)
v velocity (m/s)
In the case of water, the relevant pressure drop value
can be seen in the diagram below.
_ _ Sulzer CompaX
5
Sulzer CornpaX�M
Applications
There are many potential application areas for the Sulzer
CompaX:
• concentration and temperature equalisation of low -
viscosity liquids and gases
• mixing of additives
• dilution of concentrates
• water and wastewater treatment (adjustment of pH
value, mixing of flocculation agents, neutralisation
processes using acids or caustic solutions)
• concentration- and flow equalisation for an accurate
representative sampling from a single point down-
stream the mixer
• etc.
Design features
The Sulzer CompaX consists of a mixer with an inte-
grated dosing point. The dosing point is designed for
the mixing of an additive into a primary stream at ratios
ranging from 1 to 3.
The mixer is installed in the pipe, mounted between two
flanges (DIN 2633 or ANSI B16.5). The overall installa-
tion length is equivalent to less than half of the actual
pipe diameter.
Sulzer CompaX is available in the following materials:
• Stainless steel (1.4571)
• Polypropylene (PP)
• FRP for diameters > DN 500
• following other materials on request
PVC, PTFE, SS-ETFE coated
For mixing ratios > 1 to 3 and nominal diameters
DN > 100 mm flanged versions are available.
Pressure rating: Stainless steel = 16 bar @ 120 °C
PP = 10 bar @ 20'C

Headquarters
Sulzer Chemtech Ltd
P.O. Box 65
8404 Winterthur, Switzerland
Phone [phone]
Fax [phone]
chemtech@sulzeccom
www.sulzerchemtech.com
North and South America
Sulzer Chemtech USA, Inc.
4019 South Jackson Avenue
Tulsa, OK 74107, USA
Phone [phone]
Fax [phone]
Asia Pacific
Sulzer Chemtech Pte. Ltd.
10 Benoi Sector
Singapore 629845
Phone [phone]
Fax [phone]
Sulzer Chemtech Ltd, a member of the Sulzer Corporation, with head- The activity program comprises:
quarters In Winterthur, Switzerland, is active in the field of process engi- . Process components such as trays, structured and random
neering and employs some 2500 persons worldwide. packings, internals for separation columns and reaction technology
Sulzer Chemtech is represented in all important industrial countries and , Engineering services for separation and reaction technology such
sets standards in the field of mass transfer and static mixing with its as optimizing energy consumption, plant optimization studies,
advanced and economical solutions. pre -engineering for governmental approval, basic engineering
• Separation and purification of organic chemicals by means of
crystallization and membranes
• Mixing and reaction technology with static mixers
• Mixing and Cartridges Technology
• Tower field services
Distributed by:
1A
23.13.06,40 - 11.08 - 50 - Printed in Switzerland
diaki

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,KIPARKSON CORPORATION
DynaSancr Filter
DSF 19FT2 DBTF SS
SALES DRAWING
PROJECT NUMBER DRAWING FILE NUMBER: REVISION:
NAME 003758-01
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DRAWN: F. J. CAMARGO
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DATE 3-22-99 BY: F. J. CAMARGO CHECKED: P.
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NEMA Premium" BaUdor5.0 horsepower
totally enclosed, [e-mail]
6W
DlOto[8. Specifications: EM3615T
Catalog Number:
EK43615T
Specification Number:
36G271T081
Horsepower:
5
| �
Voltage:
230/468
Hertz:
SD
Phase:
3
Full Load Amps:
13/6.5
Usable at2O8Volts:
13.6
RPM:
1750
Frame Size:
184T
Service Factor:
1.16
Rating:
40C AMB -CONT
Locked Rotor Code:
N
NEMA Design Coda:
B
Insulation Class:
F
Full Load Efficiency:
90.2
Power Factor:
OO
� !
Enu\ooupa� �
TEFC
—
Bo|dorType:
3643M
DE Bearing:
8206
[�
ODE Bearing: �
6205 `
Electrical Specification Number:
36VVGTO31
Mechanical Specification Number:
36G271
Base:
R8
Mounting:
F1

F
N
I
RASCHIG GmbH
Mundenheirner Strasse'100
67061 Ludwigshafen - Germany
Phone: [phone]
Fax: +49.621 �5611 8.604
email: [e-mail]
www.raschig.de
Locations/Production Sites
Ludwigshafen and
Espenhain, Germany
Houston, Texas
El Dorado, Kansas
Monterrey, Mexico
DURA -PAC
flow PVC sheet
submerged fixed beds
wastewater treatment
crossflow
media for
DU RA -PAC is a self-
supporting PVC sheet
media, capable of
withstanding loads
in excess of industry
standards. DURA -PAC
modules are available
in various sizes and
specific surface areas
of 30, 31, 48 or 68 ft2lfV.
and vertical
tricklinct filters,
and other
applications
DURA -PAC is a plastic sheet media
available in two basic designs. DURA -PAC
XF is a cross flow media recommended
for low to medium BOD loading
applications. DURA -PAC VF is a vertical
flow media recommended for high BOD
loading applications. DURA -PAC's
volumetric void ratios of at least 95% allow
for uniform redistribution of wastewater
and air while maximizing contact between
the biomass and the wastewater.
DURA -PAC is available in specific surface
areas of 30, 31, 48 and 68 ftl/ft. 31 ftl/ft'
media is typically used for BOD removal
and 48 ftl/ft' media can be used for
nitrification to reduce the size of new
nitrifying trickling filters.
The DURA -PAC media is non-toxic to
microorganisms and immune to rot. It
is resistant to degradation by ultraviolet
light, fungi, bases and acids, and other
compounds normally found in wastewater.
DURA -PAC consists of thermoformed flat
PVC sheets. Sheets are sized in varied
thicknesses indexed to applications. For
cross flow applications (DURA -PAC XF)
these sheets are corrugated horizontally
and bonded to one another in a
honeycomb pattern module. Vertical flow
media modules (DURA -PAC VF) are
formed by alternating flat and corrugated
sheets. DURA -PAC modules typically
measure 2'x 4'x 2'. Custom module
sizes are available. DURA -PAC sheets
can also be shipped to the job site for
assembly, if the application requires.
DURA -PAC is one of five trickling filter
media designs from Jaeger
Environmental. Jaeger Environmental has
manufactured trickling filter media since
1979, with system installations worldwide.
We offer random and structured media for
municipal and industrial applications.
Product specifications for DURA -PAC
are detailed on the reverse side of this
presentation. For further information,
or to discuss your application, contact
Jaeger Environmental via phone, fax or
e-mail.

4
DURA -PAC
TRICKLING FILTER MEDIA
A. Standard Product Specifications
B.
Installation
C. Module Testing
1 , The media shall be fabricated from rigid PVC
I .
The media shall be placed inside the filter by
1 � Structural testing of fabricated modules shall
sheets completely corrugated forming a
crane or mechanical conveyor. The media
be performed by an Independent testing
cross -corrugated pattern with adjacent sheets
modules shall be transported by cranes or
laboratory approved by the engineer.
to permit continuous horizontal redistribution
placed on wooden slides or conveyors to the
of both the air and wastewater throughout the
working level. The media modules shall be
2. All tests shall simulate service conditions and
depth f the media. The PVC roll stork sheets
placed by hand In their final location.
conform to the following criteria,
shall b'e' of uniform thickness with no sections
less than :k 0.002 inch manufacturing
2.
Use 112 inch thick plywood, pegboard or other
a. The test samples shall consist of a stack
tolerance The media shall be specifically
suitable temporary planking to protect the
of modules at least two modules high. The
designed for use in the biological oxidation
media from foot traffic. Do not allow workers
arrangement of the stack shall simulate
of municipal and industrial wastewater.
to directly walk or stand on the media.
the geometry as placed in the filter towers.
2� The polyvinyl chloride used in the media shall
3.
Place each module as close as possible to
b� Modules intended for the base layer shall
be tested on a simulation of the support
be resistant to degradation from ultraviolet
radiation, rot, fungi, bacteria and other forms
each other while avoiding damage to the
modules. The sheets of all modules in a layer
system. Modules intended for all other
of microorganisms. The media shall be
shall be placed parallel to each other in order
to maximize horizontal
layers shall be tested on a flat base.
chemically resistant to concentrations of
uniform and continuous
c. Test loads shall be the design loads of the
common inorganic mineral acids or alkalies
movement of air and water,
media specified.
and organic solvents or compounds normally
experienced in sewage.
4.
Modules in each layer shall be rotated 90'
d. The test load shall be uniformly applied at
to the layer immediately below to enhance
a temperature of 75* F, (± 21 F) and the
3. Each module shall consist of several
water redistribution and to maximize
design load shall be applied as follows;
PVC sheets, bonded together to form a
self-supporting of the media.
structurally self-supporting block measuring
5.
The media modules shall be carefully
I . A pre -load, equal to 10 percent of the
design load, shall be applied for I hour
2Vwide x 24" high x 48" or 72" long. The
trimmed or cut to fit within 2 inches (50.8 mm)
to seat modules and to establish a
modules shall be designed with a minimum
or less of the center column, Cut or trim
baseline flexural condition.
specific surface area of 30 (or 31, 48 or 68)
modules to fit within 2 inches (50.8 mm) or
square feet per cubic foot with a minimum
less of the filter perimeter wall.
2. The loading shall be increased in 100-
95% void volume ratio. Each module shall
pound -per -square -foot intervals. Each
be capable of withstanding a minimum load
6.
Shaping, trimming and cutting of the media
loading shall be held for a minimum of
of 35 pounds per square foot per foot of
may be done in the filter provided appropriate
5 minutes and the deflection recorded
media depth. Maximum allowable deflection
measures are taken to prevent any chips,
at the end of the 5 -minute period.
shall be limited to 2%.
broken pieces or similar debris from falling
into the media. Canvas or similar working
3, Incremental loading shall continue until
4� The manufacturer shall submit test reports
materials shall be used to cover the media
recorded deflections are I percent and,
for the mil thicknesses to be supplied.Test
modules, Before a new layer of modules is
subsequently, 2 percent.
reports shall comply with the requirements
added, the existing layer shall be cleared of
of paragraph C. If there are no test reports
all construction material or objects that may
a- Maximum allowable compressive deflection
or if there are any alterations to the media
have fallen on it. The top layer of media shall
of the individual modules shall be 2
in respect to materials or design, the
also be protected from damage caused by
percent.
manufacturer shall test the modules in
failing material due to any subsequent work
f. If more than 10 percent of the modules
accordance with paragraph C.
until start-up of the system.
tested in any strength gradation exhibit
5. Individual sheets used in the manufacture
7.
The media modules in the bottom layer shall
a compressive deflection of greater than
of the media shall conform to commercial
be placed on the supports provided. Support
2.0 percent, or if any one module exhibits
standards ANSI/ASTMD1784-78:12454C with
ledge (a minimum of 4 inches wide) should
a deflection greater then 4,0 percent,
the following physical properties when tested
be provided around the center column and
additional testing may be required as
in accordance with the method indicated:
the tank perimeter wall, The top of the support
considered necessary to determine the
beams and ledges should be at the same
structural suitability of the media, If the
elevation and within a maximum tolerance
tests indicate the media is structurally
of :k 1/8 inch (3.18 mm) in their elevation.
unsuitable for its intended use, the media
may be replaced with new media meeting
the specifications and passing the
structural testing.
D. Product Handling And Storage
I . If storage is required, assembled media
Properties Test Method
Results
modules shall be stored on a flat, clean
surface to prevent damage to the module
A. Tensile Strength (psi)
ASTIVI D-638/882 4,000-8,000
edges.
B. Tensile Modulus
ASTM D-6381882
300,000-550,000
C. Modulus of Elasticity (psi)
ASTM D-746
Min 325,000
2. Modules should be checked at least once per
D. Impact Strength (ft-lb/In of notch)
ASTM D-256
1.0-5.0
week- Modules that rnay have fallen shall be
inspected for any damage and undamaged
E. Gardner Impact
ASTM D-4226
Proc.A 0.8in. lb./mil
modules should be restacked and secured.
F. Heat Distortion Temp (*F@264 psi)
ASTM D-648
155 — 170* F
Damaged modules should be either repaired
G. Izod Impact (ft-lbAn)
ASTM D-256
0-6-2.2
or discarded.
H, Maximum Service Temp
135' F
1. UL Flammability
94
V-0
3. During shipment and storage, modules shall
always be stacked on their long face with the
J. Specific Gravity
ASTM D-792
1.3- 1.5
plastic sheets in a vertical position. Modules
K. Resistance to Grease, Fats & Oils
ASTM D-722
Excellent
shall not be stacked more than four high,
L. Resistance to Acids & Alkalies
ASTM 0-534
Excellent
and modules in each layer shall be set at
M. Flammability
AsTm D-635
<5 secs, <5mm burn
right angles to those below, Weathered or
otherwise damaged media are not acceptable
and will be replaced as deemed necessary or
DURA -PAC Is Represented By:
appropriate,
E. Cleaning
As Installation of each module layer is completed
modules surfaces should be inspected for the
presence of debris or other construction materials.
Any foreign material detected should be removed
and all surfaces cleaned. Upon completion of the
media installation, a final check of the media
surface should be conducted for the presence of
foreign material and any material detected
removed prior to the application of water. Following
completion of the inspection and the removal of all
foreign material, the media should be thoroughly
flushed with clean water -
(b 2366 Durapac Flyer 08/07

N
@ Siemens AG 2008
Poll
ij,
�, ��, - -­ � , , _� t �
Continuous level measurement - Ultrasonic controllers
6esign
ciiF
Weight
Made of Operation - Wall mount 1-37 kg (3.02 lbs)
Measuring principle Ultrasonic level measurement
Measuring range 0.3 to 15 m (1 to 50 ft), transducer - Panel mount 1.50 kg (3.31 lbs)
dependent Material (enclosure) Polycarbonate
Measuring points 1 or 2 Degree of protection (enclosure)
fdow Input - Wall mount I P65[Type 4X/NEMA 4X
Analog 0 to 20 mA or 4 to 20 mA, from - Panel mount I P54/Type 3/NEMA 3
alternate device, scaleable (6 Cable
relay model)
Discrete 10 to 50 V DC switching level Transducer and mA output signal 2 -core copper conductor, twisted,
Logical 0 = < 0.5 V DC shielded, 300 Vrims, 0.82 mm2
Logical 1 = 10 to 50 V DC (18 AWG), Beldeno 8760 or
Max. 3 mA equivalent is acceptable
Max. separation between trans- 365 m (1200 ft)
Output ducer and transceiver
EchomaxO transducer 44kHz
Displays and controls 100 x 40 mm (4 x 1.5') multi -block
Ultrasonic transducer Compatible transducers: ST -H LCD with backlighting
and Echomax series XPS-10/1 OF,
XPS 15/15F, XCT-8, XCT-1 2 and
Programming Programming using handheld
programmer or via PC with
XRS-5 SIMATIC PDM software
KffiL Relays') Rating 5 A at 250 V AC, non-
. . . . . . . . Power supply4)
inductive
44 1 1 Model with 1 relay2) AC version 100 to 230 V AC 15%, 50160 Hz,
2) 1 SPST Form A 36 VA (17 W)
Model with 3 relays 2 SPST Form All SPDT Form C DC version 12 to 30 V DC (20 W)
Model with 6 relays 4 SPST Form A/2 SPIDT Form C Certiffeates and approvals - CE, C-TICKI
mA output 0 to 20 mA or 4 to 20 mA - Lloyd's Register of Shipping
- Max. load 750 n, isolated - ABS Type Approval
- Resolution 01 % of range - FM, CSANRTL/C, UL listed
Accuracy - CSA Class 1, Div. 2, Groups A, 8,
C and D, Class 11, Div. 2, Groups
Error in measurement 0.25% of range or 6 mm (0.24"), F and G, Class III (wall mount
whichever is greater only)
Resolution 0.1 % of measuring range or 2 mm - MCERTS Class 1 approved for
(0.08"), whichever is greater3) Open Channel Flow
Temperature compensation - -50 to +150 'C (-58 to +302 'F) Communication - RS -232 with Modbus RTU or
- Integral temperature sensor in ASCII via RJ -1 1 connector
transducer - RS -485 with Modbus RTU or
- External TS -3 temperature sen- ASCII via terminal blocks
sor (optional) - Optional: SmarILinx8 cards for
- Programmable fixed tempera- PROFIBUS DP
ture values DeviceNejm
Rated operating conditions Allen-Bradleye Remote 1/0
Installation conditions 1) All relays certified for use with equipment that fails in a state at or under the
rated maximums of the relays
Location indoor / outdoor
2) This model is level control only; no open channel flow, differential level or
Installation category 11 volurne conversion functions
4 ducer plus any range extension
Pollution degree 3) Program range is defined as the empty distance to the face of the trans -
Ambient conditions 4) Maximum power consumption is listed
5) EMC performance available upon request
Ambient temperature (enclosure) -20 to +50 *C (-4 to +122 *F)
Siemens FI 01 , 2009

(D Siemens AG 2008
g
Continuous level measurement - Ultrasonic controllers
i�,-(;alon and Ordering data Order No. Selection and Ordering data
Order No.
Siemens HydroRanger 200
G) 7MLS034-
Siemens HydroRanger 200
C)7MLS034-
Ultrasonic level controller for up to six pumps that
Ultrasonic level controller for up to six pumps that
b VS, M V
provides control, differential control and open
provides control, differential control and open
Order code
liannef flow monitoring. The HydroRanger 200 is
channel flow monitoring. The HydroRanger 200 is
a so available as a level measurement controller
Y15
also available as a level measurement controller
only. Select option from model code below.
only. Select option from model code below.
Order No.
Mounting
C) 7ML1998-5FC03
c ce S 5 o' nw
C) 7ML1998-5FC11
Wall mount, standard enclosure
C) 7ML1998-5FC32
Handheld programmer
7ML1830-2AK
Wall mount, 4 entries, 4 M20 cable glands included
2
Tag, stainless steel, 12 x 45 mm (0.47 x 1.77'), one
7ML1930-IAC
Panel mountl)
3
text line, suitable for enclosure
Power supply
TS -3 Temperature Sensor - see TS -3 on page 5/147
100 to 230 V AC
A
SITRANS RD100 Remote display - see RDIOO on
12 to 30 V DC
B
page 51263
SITRANS RD200 Remote display - see RD200 on
Number of measurement points
page 5/265
Single point model, 6 relays
A
Dual point model, 6 relays
a
6 r t F,
Single point model, level only, 1 relay2)
C
Power Supply Board (100 to 230 V AC)
C) 7ML1830-lMD
Single point model, level only, 3 relays2)
D
Power Supply Board (12 to 30 V DC)
C) 7ML1830-IME
Display Board
C) 7ML1830-1MF
Communication (SmartL!nx)
See SmartLinx product page 5/260 for more infor-
Without module
0:
mation.
SmartLinxO Allen-Bradleye Remote 1/0 module
1
SmartLinx PROFIBUS DP module
2
Available with approval option 1 only
SmarlLinx DeviceNetTm module
3.
2) This model is level control only; no open channel flow, differential level, or
See SmartLinx product page 5/260 for more infor-
volume conversion functions
C) Subject to export regulations AL N, ECCN: EAR99
mation.
Approvals
General Purpose CE, FM, CSAus/c, UL listed,
C -TICK
CSA Class 1, Div. 2, Groups A, B, C and D; Class 11,
Div 2, Groups F and G: Class ]H (for wall mount
applications only)
F�v' "F, -A dosign.s.
Order code
Please add "-Z" to Order No. and specify Order
code(s).
Stainless steel tag [69 mm x 50 mm (2,71 x 1.97")]:
Y15
MeasurIng-point numberlidentification (max. 16
characters) specify in plain text
lf;sir'ut�:i'fon m��n"ua!
Order No.
English
C) 7ML1998-5FC03
French
C) 7ML1998-5FC11
German
C) 7ML1998-5FC32
Note: The instruction manual should be ordered as
a separate line on the order,
This device is shipped with the Siemens Milltronics
manual CD containing the complete ATEX Quick
Start and instruction manual library.
SmartLInx Allen-Bradley Remote 1/0, English C) 7ML1998-IAP03
SmartLinx PROFIBUS DP, English C) 7ML1998-lAQ03
SmartLinx PROFIBUS DP, German C) 7ML1998-IA033
SmartLinx PROFIBUS DP, French C) 7ML1998-IA012
SmartLinx DeviceNet, English C) 7ML1998-lBHO2
Note: The appropriate SmartLinx instruction manual
should be ordered as a separate line on the order.
Siemens Fl 01 - 2009

N
@ Siemens AG 2008
RN '_ 1111111 Number of measurement points
Single point model, 6 relays
Dual point model, 6 relays
Single point model, level only 1 relay2)
Single point model, level only, 3 relays2)
eModbus is a registered trademark of Schneider Electric.
@Belden is a registered trademark of Belden Wire and Cable Company,
eAllen-Bradley is a registered tradernark of Rockwell Automation.
.2 TMDeviceNet is a trademark of Open DeviceNet Vendor Association (ODVA)
:3
Furthwr dr,.z;iKy-,q Order code
Please add "-Z" to Order No. and specify Order
code(s).
Stainless steel tag [69 mm x 50 mm (2.71 x 1.97")]: Y15
Measuring -point numberfidentification
(max. 16 characters) specify in plain text
fos"I'LIC-Hop n7anuo"
Order No.
English
C) 7ML1998-lFC06
French
C) 7ML1998-lFC14
German
4
Note: The instruction manual should be ordered as
a separate line on the order.
Continuous level measurement - Ultrasonic
controllers
manual CID containing the complete ATEX Quick
Start and instruction manual library.
Evauff
SmartLinx Allen-Bradley Remote 110, English
C) 7ML1998-lAP03
SmartLinx PROFIBUS DP, English
C) 7ML1998-1A003
SmartLinx PROFIBUS DP, German
C) 7ML1998-IA033
SmartLinx PROFIBUS DID, French
�
SmartLinx DeviceNet, English
C) 7ML1998-IBHO2
I ta Ii�' -
0.
Milltronics HydroRanger 200 C) 7M L 10 3 4 -
Milltronics HydroRanger 200
C) 7ML1034-
Ultrasonic level controller for up to six pumps that
Ultrasonic level controller for up to six pumps that
w v, a P,
provides control, differential control and open
provides control, differential control and open
channel flow monitoring. The HydroRanger 200 is
channel flow monitoring. The HydroRanger 200 is
also available as a level measurement controller
also available as a level measurement controller
only. Select option from model code below.
only. Select option from model code below.
Mounting
ories
Wall mount, standard enclosure
Handheld programmer
7ML1830-2AK
Wall mount. 4 entries, 4 M20 cable glands included 2
Tag, stainless steel, 12 x 45 mm (0.47 x 1.77"), one
7ML1930-1AC
Panel mount')
text line, suitable for enclosure
Power supply
TS -3 Temperature Sensor - see TS -3 on page 5/147
100 to 230 V AC A
SITRANS RD100 Remote display - see RD100 on
12 to 30 V DC B
page 51263
Communication (SmartLlInx)
SITRANS RD200 Remote display - see RD200 on
Without module.
page 5/265
SmartLinxO' Allen-BradleyO Remote 1/0 module B
Spore pa�
SmartLinx PROFIBUS DID module
Power Supply Board (100 to 230 V AC)
C) 7ML1830-lMD
SmartLinx DeviceNetT" module
Power Supply Board (12 to 30 V DC)
C) 7ML1830-lME
See SmartLinx product page 5/260 for more infor-
Display Board
C) 7ML1830-lMF
mation.
See SmartLinx product page 5/260 for more infor-
Approvals
mation.
General Purpose CE, FM, CSAustc, UL listed, 1
C -TICK
1) Available with approval option 1 only
CSA Class 1, Div. 2, Groups A, B, C and D; Class fl, 21
2) This model is level control only; no open channel flow,
volume conversion functions
differential level, or
Div 2, Groups F and G; Class III (for wall mount
C) Subject to export regulations AL: N, ECCN: EAR99
applications only)
RN '_ 1111111 Number of measurement points
Single point model, 6 relays
Dual point model, 6 relays
Single point model, level only 1 relay2)
Single point model, level only, 3 relays2)
eModbus is a registered trademark of Schneider Electric.
@Belden is a registered trademark of Belden Wire and Cable Company,
eAllen-Bradley is a registered tradernark of Rockwell Automation.
.2 TMDeviceNet is a trademark of Open DeviceNet Vendor Association (ODVA)
:3
Furthwr dr,.z;iKy-,q Order code
Please add "-Z" to Order No. and specify Order
code(s).
Stainless steel tag [69 mm x 50 mm (2.71 x 1.97")]: Y15
Measuring -point numberfidentification
(max. 16 characters) specify in plain text
fos"I'LIC-Hop n7anuo"
Order No.
English
C) 7ML1998-lFC06
French
C) 7ML1998-lFC14
German
C) 7ML1998-lFC34
Note: The instruction manual should be ordered as
a separate line on the order.
This device is shipped with the Siemens Milltronics
manual CID containing the complete ATEX Quick
Start and instruction manual library.
SmartLinx Allen-Bradley Remote 110, English
C) 7ML1998-lAP03
SmartLinx PROFIBUS DP, English
C) 7ML1998-1A003
SmartLinx PROFIBUS DP, German
C) 7ML1998-IA033
SmartLinx PROFIBUS DID, French
C) 7ML1998-lAQ12
SmartLinx DeviceNet, English
C) 7ML1998-IBHO2
Note: The appropriate SrnartLinx instruction manual
should be ordered as a separate line on the order,
g
Siemens A 01 .2009

P
@ Siemens AG 2008
0
Continuous level measurement - Ultrasonic controllers
1 6j 1
t Schematics
IN Dimensional drawings
TB2
Wall Mount Version
6W
14.9 mm 160.3 mm
mounting 91 Mon
6.6 mm
15.2 nun
+-T
holes
(0.26")
(0.6")
0 43 finnn
(0.17") (A)
Iva
IAINP�
P lveqs on
cover
240 rnm
LAY I
txc6rrs
(9.45")
227
—�A
V
:,3FIFLAY2
OUTPOIS
+
+
sulta6ie EafR fu,
WW
conclull t efitninces. us O�mer
'Slarnens Milltronics mountin :h I
a hole. (66cess6cl under lid)
-h
E) I
f d'Ilihg the holes. �4.3 .17")
-TRE�AY4
Panel Vair
F
MM
rnnn�,
07:rfirn
82)
ffIRELAY5
F
z 1
Notes'
with.phlelo, for ekipansion up.16 366P (1200%)..
278 tran
ants are installed in accbr:fance.:�ih instr uktions.
. 3; Cori 6 nectl on 6 A6iddiffere
r) gal
(10.. 1r)
4� K060 exposed cbnou . . ct . o . rs or) .,..shield c ]a : s, as 06 a as� Oossibleto reduce noise
n
o 6 i4i 6 apse.d.by
so
stray transmis i ns and noise pickup.
6MI
HydroRanger 200 dimensions
1 6j 1
t Schematics
HydroRanger 200 connections
Siemens Fl 01 .2009
&06
TB2
T.,
L21N L
G
+-T
See note
TB3
12- �OY�.- —7
IAINP�
P lveqs on
E)
LAY I
—�A
V
:,3FIFLAY2
OUTPOIS
+
+
E) I
-TRE�AY4
F
G i
ffIRELAY5
F
z 1
Notes'
with.phlelo, for ekipansion up.16 366P (1200%)..
6461 d f
Qin, grgun. ed,�,netal, conrlpit; separate: rom othercables,
ants are installed in accbr:fance.:�ih instr uktions.
. 3; Cori 6 nectl on 6 A6iddiffere
r) gal
4� K060 exposed cbnou . . ct . o . rs or) .,..shield c ]a : s, as 06 a as� Oossibleto reduce noise
n
o 6 i4i 6 apse.d.by
so
stray transmis i ns and noise pickup.
HydroRanger 200 connections
Siemens Fl 01 .2009

I
I
for i'll't ushlial application of tilt nolson if's
1 W� t nI
j ti, 1 4 1�
it
n I
j iL.
F.t t.-vw our %. !i ,te 0 r
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IVAONJI�t
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I
SPECIFICATIONS- ECHOMAX@ NON -CONTACTING ULTRASONIC TRANSDUCERS
Model Min.Range Max Range Beam He metically Dam Foam Built In Temp.Range Chemical Thread FlangeA Freq. Weight
Angle Sealed Housing acing Temp. Temp. Celsius Immunity Size Mount. kHz Kg
M Ft. =M[ =Ft -3dB XPS & XCT opt Rating Rating (Fahrenheit) Rating Opt, (nom.) (lbs.)
THE SURE SIIOT XPS SERIES
XPS-10
0.3
1
10
33
12*
Kvnar@
Kyna r@
.(White)
95.
Yes
-40' to 95'
1 Excellent 1
1 NPT
1 NPT
1 BSP
43
.75
.75
(1.65)
:XCT�l 2
pq�
0.46
1.5
12.
40
(6lue)
�ynuS
:(white)
(203')
W'. 41. 1,4M49, ffia,..'� .,.any
(40- to 203-)
-40' to 145*
(-40' to 293')
1 BSP
1 NPT
1 BSP
(1.65)
XPS-15
03
1
15
50
6'
Kynar@
Tal -31016 W 15-12 '.� —Mlr' W. ll '02
95,
Yes
-40' to 95'
Excellent
1 NPT
Yes
43
1.28
1, N.pT,:.:,
7_::::�
13
(blue)
(203-)
(40- to 203-)
1" BSP
(2.81)
XPS-30
0.6
2
30
100
6*
Kynar@)
(14;0):l
95"
Yes
-40' to 95'
Excellent
1 '12 "
56.
30
4.14
Yes
Ad' to
Fill
N PT
(blue)
(203')
.4.4
(40- to 203-)
BSP/NPT
Compa-
(9.12)
ed
—
019
3
40
130
6'
Kynar@)
4
65'
Yes
-40' to 95'
Excellent
Xj 50
22
7,9
I—T-1XPS-40
:i6d:
m-,
(blue)
-40' to 150'
(1149')
(40- to 203-)
tible
-13
63
(17.4)
THE HOT SHOT XCT SERIES
XCT-8*
0,45
t5
8
26
12'
Kyna r@
.(White)
Yes
Yes
-40' to 145'
(-40- to 293
Excellent
1 NPT
1 BSP
43
.75
(1.65)
:XCT�l 2
pq�
0.46
1.5
12.
40
'..6*:,:
�ynuS
:(white)
Gr .
W'. 41. 1,4M49, ffia,..'� .,.any
:Yes
-40' to 145*
(-40' to 293')
Excellent
1 NPT
1 BSP
43
1.28
THE LONG SHOT XLT 1XLS SERIES
O�'
A
R�-Jlnciklgy Customer diwen.
j:00.
�M4 �1�11ola.o D', P 0 3. Qz4
Yes
-401 to 90'
Fair
V. NOT
It, - 32(QI3326 45 54 F.— �3Z(0)3UI .5 21
:22,:�
1 4�4 :1
131W Fl ---
6.1, 69 m F,�. 31 � �2 59 63 .1
Gr .
W'. 41. 1,4M49, ffia,..'� .,.any
�9 2 1 �r2 1.21 F7 -4� 111 16� 61M
40* td:1.94')
W.-, S— 602, Q-ry 8,y. Nang Klag
T.l -ol 1"135228bG 31�16 IF— �ol 1 — �811,2oli�
F
(9.7)
---1 1., .1-1823 Aft B-1., — N.1an I.no,l
Tal -31016 W 15-12 '.� —Mlr' W. ll '02
200
log —,— D— I -, I.— U,S.A. '—
�7
Yes
:-40* to 90.*
Fair
1, N.pT,:.:,
7_::::�
13
(40'to 19V .
(14;0):l
36:�::! i
:160
56.
A luminum:
Yes
Ad' to
Fill
N PT
2Z:]
.4.4
ed
j-401 116.3.001).
(9.7 F
Xj 50
:i6d:
m-,
Yes...
-40' to 150'
Fair
N p]
-13
63
T:
40, to 300
Note: Effective maximum range capability may vary aepenaing on application. . t-000 sale. rulA dcueptuu
Our continuous program to improve products may result in changes in design and specifications withOLIt notice.
For XRS-5, XKS-6, XPS-10F, see Technical Specification Sheets.
ECHOMAX' SERIES APPROVALS
CENELEC EEx m 11 T5: XLS Series. EEx m 11 T4: XPS Series.
EEx m 11 T3: XLT & XCT Series, TS -3.
CSA Class 1, 11, Div. 1, Group A, B, C, D/E, F, G. Class Ill.
FM Class 1, 11, Div. 2, Group A, B, C, D/F, G. Class Ill.
FM XPS 10115: Class 1, 11, Div. 1, Group A, B, C, D/E, F, G.
Class 111,
CSA. FM. TS -3 Temperature sensor: Class 1, Div. 1, Group C & D
Class 11, Div. 1, Group E, F & G.
NOTE XCT-8, unfaced only, CSA approved.
CONDENSED APPROVALS LISTING. CONSULT AGENCY APPROVAL GUIDE FOR DETAILS.
Representative
35751080 NA
� hit I. 1-- 1.1, — ..". . .....
N Polyester covering is standard.
Milltronics versatile line of sophisticated Ranger- transceivers provide reliable level con-
trol in a single vessel or a multiple tank farm.
35751082 A4 69-1
,N!"ib.—
A
R�-Jlnciklgy Customer diwen.
�M4 �1�11ola.o D', P 0 3. Qz4
14, 2`l3l
N—" .. it- 3,l% — u.,
—11139691-M. 1- —1613�—Wo
wqw.
It, - 32(QI3326 45 54 F.— �3Z(0)3UI .5 21
131W Fl ---
6.1, 69 m F,�. 31 � �2 59 63 .1
W'. 41. 1,4M49, ffia,..'� .,.any
�9 2 1 �r2 1.21 F7 -4� 111 16� 61M
W.-, S— 602, Q-ry 8,y. Nang Klag
T.l -ol 1"135228bG 31�16 IF— �ol 1 — �811,2oli�
A—.1 N", 11-55, - - V-� G31OG M -11a D F —il-
To, -521,bI62128 F;�� -12-112686
---1 1., .1-1823 Aft B-1., — N.1an I.no,l
Tal -31016 W 15-12 '.� —Mlr' W. ll '02
log —,— D— I -, I.— U,S.A. '—
"'- '1 111.2 11 �543 r— � 1 811 389"
A aint ­ana, in Si.q.p.­ a —1- ni- in 8111il and
in �a

6W
Mm
I -A
Lm)
WALLACE: &TIERNAN
,k)
ENCORE" 700
DIAPHRAGM
METERING PUMP
SB.440.400.GE

ENCORE"' 700 DIAPHRAGM METERING PUMP
MORE APPUCATIONS, MORE 2ZNEF$TS,
MORE FEATURES ... MORE PLIMP
flydrauflc diaphragri) pamin am renownedfoj- their dur,8billty, burstart-up iml
maintemvice can be Jabot-Jous, pat-ticubidy when ser -vice mquirar purffing arld PePlacing
Intermediate flums. Additionally, 117,.?ny designs av? vei- n n
.y sensitive to rhang! 9 .1 actfu
t-unditions. If andjagnased, hlockpd m- stinvvd Suction can lead to h.,;,draulic omrfill and
szjAvpquFnt rRaygmagm 1�dlufv.
jWEdminical diaplmvgni pumpf are lar Aess SUP11-isdemcd. slarr-tq.? and sez-vice afe
�ypically niuch smoorhei- sInce thprp. al v 120 n2emy 112termedi'me flulds, internal I-ellef valvp,�
oz, hTdr-m.dic Tefill cin-Wis to timp.1- with. But, urmil nmv, rnediarVeal diaphl-agril Pulnivs
haven't Shaled the hydivulir dhaphl'agm pump , s.mpatedon.fol- robustn(,�Ss.
WPIC017)e W the &]WIlt"11' 700
A whole new class of motering
combines thp rolmisinem of hydraulle
dRiphragn) drives with the unpiralletcd
economy, simptichy ancl serviceability of
rnechanical diaphmgm liquir.1 ends.
Handles capaciti�.!s to 2,400 1/h,
back pressums to 1.2 bar.
Non -loss rnotion (amplitude modulation)
stroke. adjust mechanism renders unrNaled
efficiency, longevty arld rehabili(.Y�
Choice of' two lield convertible drives.
direct coupled or pulley coupled, for an
additional 4:1 turntlown onstroke frequency
wilh a sian(hirrl induction rnot.or,
Pmc.Nion engineered licivid e.nds mater 11111d
soluliom, a&qressive chernicaK bigh viscosity
polymens and slurries witli far greater
effidency ihim conventional liquid (:!n(3%.
Clear f.`vT' cartridge. �,alves f6r Fast, fbOlproof
szvvjce� with I lo pifAn.g disturbanccS Mid
built -in yi�,,ual indication of operation.
11remium diaphragm design ensure.q high
inetej ing acc.urwy everi at vaoyng dtscharf�je
pressurt'v,

TYPICAL APPLICATIONS,
METERING AND PUMPING
FULL MECHANICAL MOVEMENT
AMPLITUDE MODULATION ADVANTAGE
Typical Industries
Typical AI:iPlications, Metering &- pturiping
Watel and Wastewater
Cnagulants, oxidising agents, disinfectants, corrosion
Treat.went
inlifbitors, chenilcals, for taste, odour and pli control
IPME
Svvinifning Pools
ACIdS, caustics, disinfectants and oxidising agents
IN
Food Proce-ising
Ba(Aericides, algaccicics, acids, caustics, detergents',
nil
corrosion inhibitorsand lubricants
chealical PrOcessink
Additives for petrochemical, pharmaccutical,
Pulp and paper, plastics and textile rninul'arture,
Brewing & Distillation
Filtration and Fermentation pids� Nictiricides, aci(is,
caustics and detergents
Agriculture
Fertilisers, herbicides, pesticides and
food supplerrients
NI�wring purnp manufacturers gcnerally use
one, of three diaphragni actuation methods.
Solenoid Pumps,
The rriust. simple and eWnOlfftal type 01'
purnp, these provide a pulsed Now with huge
pressure spikes, considerable noise and wear.
Lost -Motion Purrips.
These motor driven pumps are higher In
capacily Nan solenoid puaips, but also give
rapid accelerntion to the liquid at rest. in the
punip head due lo
diaphragm rnotion,
Non -Loss Motion Pumps.
'PhL dlaphragin is driven by aroLating
crankshaf't, where the. eccentricity can be
smoothly -d 'here
, adjuste during operation. I
are no return and the diaphragm
moves with simple harinunic inot-ion� The
rluid velocity profile is sinusoicial at all stroke
lengths, ad.iu,5flng stroke length simply alters
the amplitude or Ihe sine. wave. This design
provides reliability and Iongevwv and purrip
valves operate vvilh Far greater efficiency.
I - 'his graph shovvs the ve.locity proffles for eich purnp -type. For any given output. the areas
circumscribed by each curie are identical. Note the difference in non loss -motion (jesigns.
Encore' 700 non4oss
motion mechanical
diaphragm pump
&
[ost motion
PUMP

Aa
�M
�J
ENCORE@ 700 DIAPHRAGM METERING PUMP
Look kt: the
d
a V'�7�7
Available with standard induction and variable speeAl motors
(optional) for wider operating ranges and autornatic process control.
Short suction and discharge
porting minimises friction losses
and cavitation, improving
hydraulic characteristics and
providing bir more efficient fluld
metering than conventional
liquid end designs.
0LIf fferniUrn COMPOSItC
diaphragin is mai
stringent specifications to ensure
long life even under the most
demanding applications,
T'he design incorporates teflon -
facing, for the highest clegre.e. of
churnical resistance and nylon
reinforcements, all boraded to a
pre -formed elastomeric supporL
We've added convolutions for
un(nnstralned rolling action,
a steel backing plate to assurn,
volurnetric accuracy even at varying
discharge preSSUres and an o -ring
groove in the. head's d1aphragni
cavity for complete seating.
High precWon guirled ball -and -seat clear
PVC cartridge valves (except 165rnm head)
provide buill -it) sight flow indication and fast,
foolproof service, The. design includes wide
flow paths and four -point guides to control
ball rise and assure propei seating. The. valve
housing is compression sealed to the. purnp
A secondary diaphragni seal
completelyseparaies the pumphead From
the drive (init, This double diaphragm
isolating design climinates the risk of
cro.55-ronjarninating gearbox lubricant and
process fluid.

I
Avaftble in two field convertible
drive arrangentents: dlrecL (Irive or
pulley drive. for an additional 4: 1.
r,jrig(-�abjiity on stroke frequency with
a standard Induction motor. When
the putlPy drive arrangerrient is
combined with -a DC variable
spep,d motor, total operating
turridown can be as high as 800:1!
With double siniplex:
capability, two drive units,
each with independent
capacity control, can be
multiplexed for blending
applications or future
process expansion,
This robust mecharrical assembly Fuature- liberal use of.'heavy duty
------ � parts including at-, epoxy painted cast iron gearbox for superior
corrosion resistance, 316 SS fastcners, load absorbing tapered roller
bearings, robust Sears and steel and rjodular iron drive components,
Obtain precise and highly repeatable Feed rate satings with a
10 turn inicrunietuir-type stroke length adjjt1ster.
A percent scale and vernier indicate stroke length III
iricretykent.s
Feed rate. is infinite.1y I(Ijus �j F
. ta le roni G to 100%.
Autornadc capadtv control vlastroke length is alsio available.
An optional cliaphragin leak detection systein styrses d -le early
stages of (11aphrigin Caflum The �Yslern consists ofa solki-state,
electro optic sen,5or that mounts to the liquid uric] and it IP 65
contrul box. This box, which can be motinted at ilia pump, or
up to 30 metrez, c2n monitor two liquid Prids, LED's and a rclay
provide both local jkrict reinote indicadon of'NJure..
6A
Elorlm-optir Sensor

MANUAL AND AUTOMATIC
STROKE LENGTH CONTROL
'Flip Exworp.T) 700 metering purnp can be
controlled by varying the stroke length or
stroke frequency. The rollowing control
-c
-hernes -are avallabie:
Manual or Remote malluat Control
Start Stop Control where the motor is
wired Into the circuit of a transferpurrip,
switch, tinier or con(roller
- Flow Proportiomil Control froin a single
process variable
Residual, Compound Loop or Setpoinl.
Control USirlg One or two process
variables
Manual Stroke Length Control
A 10 turn micrometer gives continuous
feed rate a4justinent overa 10: 1. range. A
percent scalp, and vernier indicate stroke
length setting to I part in 400. Each
revoltition of the knob changes feed late by
10%� Stroke lungth is infinitely adjustable
from 0 to 100%6.
ENCORE@ 700 DIAPHRAGM METERING PUMP
Automatic Stroke Length Control
For autornatic capacity contral vi -a stroke
length, our TIM IP 65 actuator is used in
con.junction vvith either of two new process
variable controllers'. The compact, field-
retrofittable actuator easily installs on the.
purnp and features local inanual override
and a window for clear indicat !oil of stroke
length. Two new micropracessor-based
controllers are available:
SCU, Signal Conditioning Unit
The econornical SCU gives autnniatic.
iocess control in
r
response to one
process variable.,
typicalky now
rate Homed in a
TP 6� enclosure,
the SCU features
all 8-0111-acter
alphanUrneric LCD display with 6-buttori
ke.y1jad arid menti -driven operator' prornpts
for simple operation, setup and calibration,
Input flow scaling kind output dosage
adu ustment allow independent scaling from
10 to 400%. See publication T1 40. 1 00GE
for oiore details.
Variable Speed Control
For precise and accurate leed rate controt
via stroking speccl, an SCR Drive Unit
varies thc. speed of a DC pump tnotor�
Stroke frequency can he, regulated manually
by potentiometer sLtlingr or aut,onlatically
via a 4-20 rnA process variable Input signal
(optional). Closed-loop speed regulation
provides I'Led rate. control accurate to 1% of
full sc rn
.ale. With continuous adjust - ent over
a 20:1 range, total operating tumdown
with water -like solutions is 200: 1. oil direct
drive units, 800:1 on pulley drives,
Dosing or scaling ol'a process variable carl
be acromplished by rneans of ail SCU,
Signal Conditioning Unit used in
conjunction with an SCR' drive.. For More
complex control, a PCU. Process Control
Unit can be used to provide setpoint
control in response to two PrO(,C-,S WIFiables,
such as plant flow and chlorine residual.
PCU, Process Control Unit
The PCU is a full feature setpolrA
controller. It provides autcrnatic process
control in response to Lwo process inputs,
ty ically flow rate and chlorine residual.
, p
The. PC U C-811 operate in ally Of r0rUr
different control inodes Including residual
Feedback, compound loop, dual signal feed
forward (for dechlorinitinn) and now
proportiona . n
additkin, the.
PC, U caTi be
configured for
mnter-zero
operatlon in
compound loop
z t,
rnoc e w en a
DEOX/2000�' Dechlorination Analyzer is
used. Housed in a IP 65 enclosure, the
fICU reatkires a large alphanumeric display,
an LED bargraph to indir.a(e now input or
WtUat0V Position ill 5% increments, a 13 -
button Rcypad and menu driven operator
pron).pts for silliple operation, st..tup and
calibration.
For inore information reclu(�st. publication
'11 40.200CE,

I
I
TECHNICAL INFORMATION
CAPACITIES AND DISCHARGE PRESSURES
501-l'. 1450 RPM Pro- (1,or)
Dl.phr�qnl
SlhAe
C�P.'q'
P"liq
oo ASO RFM
MY
n, T1 IN,
.31 W?) 737 1.551 .55 WIN
31)
]A)
I
12
611)
2.1
7.9
1
1?
R k"
I,/, 1T),
120
4. ?.
15.8
1
1
44
5.0
18.9
1
12
30
�Al
22.1
1
12
50
60
10J)
44.2
1
12
P, 1�1
12D
ZOD
80.0
1
I�
144
24
1136.0
1
12
N
9.4
3.9.5
1
ill
7 f,
F, 11
" �F.'
71
1
10
120
3 7 �;-,
141.9
1
144
45.0
370.3
1
3.0
19.0
6G.7
1
9
ill()
fit)
3 2 1
12 1 A
I
- 9
wil
64.2
242.9
1
144
77.0
1 291.4
1
30
3T5
A1.9
1
5
12,
`0
7511
283.9
1
R 1
120
]."O.o
IiIMA
1
5
144
Me
681.3
1
30
66.0
NO.()
1
3
16,
at)
132.0
520.0
1
- 3
120
164.0
1041.0
1
3
1-1.1
3 17.0
12511.0
1
.1
'Rdl,m �inipl�.x !�padZy, double,i,nplx arfanil�.)n,.Ats iiw.,t N� ... d Mth -�. stn,k�-ftpqu-��, - b(,th liquid unis,
pulle� 'I'M m i"'geme, Its, wp'itj�' ll�t,l n� fm pulhty wti. 1. Capadl i�,, ror slep,,Z. 3. afid 4 an 7 5%. 50% mid 25%
r,�5pL�Uwly.
Accuracy
Repeatable metering accuracy is + 2% of
Full scale, at constant hyclraullc conditions,
over a 10:1 operating range.
Stroke Length
L.iejaid End Si7e .3.5 and 50mm: 4. Sinn?
(01881�
Liquid Fnc.&Silp 7.5. 101.9, 125 and
165inrn: 9,6rnin (0.375 ") �
Feed Rate Adjustment
Feed rate is Infinitely adjustable from
0 through 100%. A percent scale and
vernier Indicate struke length scidn�� in
0.?5% increments. F.,ach revolution of the
knob changes strokL tength by 10LYo.
Operating Range
Dlrrcr Drivr Arranffrinant:
Stroke Ieng
_,th is adjustable over a
10: 1 range; stroke rrerjupTicy is adjustable
over a 20:1 range (using art optional
variable speed drive). 'Total corribined
maximum operating turndown CATI i)c its
high as 200:1. Above 100:1 conflnuous
turticlown, total available operating range
should be evaluated apiinsf specific
cheinicals being nietemd,
pulley DzyVe
Stri)ke length is adjustable, ever a
10: 1. range; stroke frequency is aqjustablL
over an 80:1 rangL (using arl Optional
variable speed drive). Total combined
maximurn operating turridown can be as
high -is 800: 1. Above. 100: 1. contimions
turndown, totalavailable ol.w.rating range
should be evaluated against specific
c.heinloals being metered.
Speed of Response
Autornatic stroke length control response.
time is LOO seconds front 0 to 100%.
Variable Speed COntr0l response tirno is
Under 3 seconds from 0 to 1,00%,
Suction Lift
The punip will self pritne with 3 nictres of
water Suction lift (wetted valves, ze.ro back
pressurc� full stroke and speed, waterlike
sohjtion%)� Once Primed, tile puirip will
operate with 3 metres of wite.irsuction lift.,
FIC30CICCI suction Ls recortirnended.
Weight and Shipping Weight
Singil,simplay. 50 kg-. 60 kg; doublesh77131ex
73 kg; 88 kg. Fur arningernents Willi
autornatic stroke length contral add
5,5 kg; 7.3kg.
Temperature Limits
With
frotin 2-52'C, process fiLlid tt.Toperatures
LIP to 52'C.
With 7�ynarljfjvld cnd: process ffiiid
remperatures tip to 62-C.
(fechnical Information continued un next
Fine.)
Dfl,m, Hy
�
El DuNnt

N
I
Electrical Requirments
Standard induction inotor arranginent Is
1450 rpm, 115/230 Volts, 5OHz, single
phase, TEFC. k4otors with other electrical
characteristics are available as art option.
Diaphragm leak detector requires 115/230
Volts, Rela�y rating 5 Amps @ 250 Volts. 30
VDC. IP 65 enclosure. Vat -table speed drive
control unit requires 11.5/230 Volts, 50/60
Hz, single phase, 200 mA 0 I,sv, 100 mA
(230V). Automatic sLi-oke length actuator -
3 alarm contacts (hig)i, low, actuator
disengaged) N.O., rated 5 Anips @ 250
Volts.
Materials of Construction
box and liquid end adopter.'epoxy
painted, cast iron
Sti-oke positioner 6ridosum., epoxy painted,
cast alurninutia
Pump bead: PVC or PVDF
Suction and efi.scharge va/vr housings -,'clear
I'VC, gxey PVC or PVDF
Vah-ebalft,,316 stainless.TFE, curanlic,
glass and potyurethane (for slurry service)
Valve seals.- Hypalon and Viton
Dmpjijz�gm. TFE-faced, fabric reltiffirced,
elastorner backed, Witt) a s (eel or cast. Iron
baddrig, pkite
Alloanang box (optional).- A13S
The pump is UV u-sistalyl:
Due to cGritinval produrt developrr&nt nd
ilrqlY0vLMl Lill L � C.Mla�ll STATificatiolls 11MY
chaqe livithout prior �tntiomiceinent.
ENCORE 700 DIAPHRAGM METERING PUMP
Polymer and Slurry Handling
Capabilities
Polymer solutions at viscosities up to �,000
cps at 144 spi'm Viscosities measured with a
B17001diOld Viscometer with No. 9— spindle
at 3 rpm.
I Iiydratecl lime slurries up to 0,38 kg per
litre ofxater� activated carbon slurries up
to 0. 11 kg per litre of water:
diatomaceous earth sJurries up to 0. 17 kg
per litre of water.
Chemical Metering Systems
Low cost packaged sysLerns can be CLIStOln
configurLd from standard stock
components including tanks, ri-Axers,
instrurnent,ation and a wide range. of
controls. All systeras are shipped assembled,
prewired and reody to install. Our
comprehensive range ofco-ordinated
, -icce,
ssortes provide the abtlity to produce
the best. possible installation,
Accessories
Choose ('rorri Bad- Pressure Valves, 1'ressultl
Relief Valves, Antisyphon \IaNeS, KIM'
runction Valves, Main Connections,
Strainers, Pulsation Darnpeners,
Calibration Chanibers, Solution Thril�s,
Mixers, Liquid I -eve] Switches, slurr.y
Flushing Systems and nurnerous MOUnttrig
Accessories,just to natne a Pnv.
PM Kits'"
Preveynive Maiwenance kits contain
original Wallace & Tiernan replacernerils
Cor those parts most susceptible to weat.
They facilitate scheduled maintenatic.e and
help maintain tiquipmerit In good working
order, eliminating equipment brPakdowns
and costly downtimp.
For further technical Information see
P1,1blicitions:
'1140.400,13E &
Tj.440,400,2.GF,
WALL.A.CTIE& TIERNAN
07/02
Che,nAfeed Dmitcd
Priory Works
T6ni--teidge, Ke i it TN I I 0QL
Telephone: [phone]
Fax: Alt (0) 1,732 771800
Srl�jlf;
hap.111-viviv,

r
7
7
f7
LAO
,7
L. -I
02/09/2000 113�21 7658273669
.TEC,'Inc.
1!L*1@qq11 �'Bl. �
TEC INC
PAGE 02
SPECIFICATIONS
PRESSURE RELIEF VALVES
WEIGHT LOAD -ED
The TEC weight loaded pressure relief valve offers non- ----- —
vibrating, reliable capacity relief for positive displacement
blowers.
The pressure relief valve Is instilled in the discharge air
'Eve displacement blowers
-stream to prevent damage- to post
when operating pressures exceed the maximum pressure
rating -of the blower.
As the system pressure approaches the valve s,et point, the
weight loaded cylinder is forced up from the valve seat and
exposes the vent ports for fast and efficient blow -down.
When acceptable system pressures are re-stcred, the valve
automatically returns to the original set position.
The valve cylinder and seat are constructed of cast Iron and
accurately machined to very tight tolerances for smooth
C
operation, OPEN
Removable weights have been carefully designed to permit
accurate pressure settings in Y2 PSI increments.
Adjustments In the relief setting can be made by adding or
removing weights.
DIMENSIQNS
SIZE A
8
C
. D
E
WL (08.)
771 7– 1.0"FPT
, !';;.t
4.19
4.75
' 2.00
6.00
a
- -.—
1.5" FPT
5.81
6.44-
2.63
8.13
--- I
110 -
2-1127 2.5" FPT
7.63
8.88
3.63
9.88
Es—
.mx oirmnernsiconss in iricnes
PERF
� A �
PIPETAP
TEC, Inc.
3594 S. CR. 350 E.
Connersville, -IN 47331
PH: [phone] FX_ [phone] SWL1199
FLOW RATING - CFM (68 F & 14.7 PSIA).
VALVE
SET PRESSURE - PSIG
SIZE
1
2
3
4 5 6
7
9
10
is
40
60
80 100 120
140 160
185
205
39
80
120
160 1 205 2.5
285 330
370
410
2-11T
119
240
366
490 1 620 740 -
866 1000
1125
1260
TEC, Inc.
3594 S. CR. 350 E.
Connersville, -IN 47331
PH: [phone] FX_ [phone] SWL1199

Lo
a
-1 1 . �U.r­mrl CrUnIz
GENERAL DIMENSIONS FOR STYLE 5002
MATERIAL
-TEMPERATURE RANGE
5002 -AL
1 3-1/2
1.315
1-5/8
4
6 1 41/2
4-7/8
El
1.660
MAL
5
7 5-9/16
6-1/8
1-1/2 4
1.900
2-1/4
6
.8 6-5/8
7-1/8
4
2-3/8
2-'3/4
8
10 8-6/8
9-1/2
5
2-7/8 1
3-1/4
10
12 10-3/4
11-1/2
5-1/2
Lo
a
-1 1 . �U.r­mrl CrUnIz
GENERAL DIMENSIONS FOR STYLE 5002
ALL DIMENSIONS IN INCHES STANDARD MODELS & MATERIALS
6_j
MATERIAL
-TEMPERATURE RANGE
5002 -AL
1 3-1/2
1.315
1-5/8
4
6 1 41/2
4-7/8
1-1/4 3-1/2
1.660
2
5
7 5-9/16
6-1/8
1-1/2 4
1.900
2-1/4
6
.8 6-5/8
7-1/8
4
2-3/8
2-'3/4
8
10 8-6/8
9-1/2
5
2-7/8 1
3-1/4
10
12 10-3/4
11-1/2
5-1/2
3-1/2
3-7/8
12
14 12-3/4
13-3/4
ALL DIMENSIONS IN INCHES STANDARD MODELS & MATERIALS
6_j
0 OPTIONAL MATERIAL SELECTION
* Aluminum
* Bronze
* 304 Stainless.Steel
316 Stainless Steel
Cadmium Plated Steel
Electroless Nickel Plated Steel or Aluminum
Monel*
Titanium*
a Hastalloy*
*Nan stock item — Available upon request.
MATERIAL
-TEMPERATURE RANGE
5002 -AL
Aluminum
Aluminum
50
6002 -B R
Srass
Brass
150
6002-304
304 Stainless Steel
304 Stainless Steel
150
5002-316
316 Stainless Steel
316 Stainless Steel
150
5002 -Class A
Steel
Aluminum
160
5002 -Class D
Steel
I Cadmium Plated Steel
150
Standard Elastomer: Buna-N
0 OPTIONAL MATERIAL SELECTION
* Aluminum
* Bronze
* 304 Stainless.Steel
316 Stainless Steel
Cadmium Plated Steel
Electroless Nickel Plated Steel or Aluminum
Monel*
Titanium*
a Hastalloy*
*Nan stock item — Available upon request.
11._� . a.. i *This temperature range is for general guidance. The
* 304 Stainless Steel figures may vary with application.
. 316 Stainless Steil CONSULT FA
Monel and Inconel springs available upon rsquest CTORY FOR MATERIALS, SIZES AND
PRESSURE RATINGS NOT SHOWN.
COMBINATION END CONFIGURATIONS ALSO AVAILAtLE.
MATERIAL
-TEMPERATURE RANGE
• Buna-N
—60 to 225, F
• Neoprene
—40 to 225* F
• Butyl
—65 to 3M- F
• Hypalon
—20 to 300- F
EPDM
—40 to 350* F
Viton
—20 to 400, F
Teflon
—20 to 450, F
Silicone
—100 to WO* F
FDA Approved
—40 to 2251 F
White Neoprene
11._� . a.. i *This temperature range is for general guidance. The
* 304 Stainless Steel figures may vary with application.
. 316 Stainless Steil CONSULT FA
Monel and Inconel springs available upon rsquest CTORY FOR MATERIALS, SIZES AND
PRESSURE RATINGS NOT SHOWN.
COMBINATION END CONFIGURATIONS ALSO AVAILAtLE.

BULLETIN B
Cut -Sheets and Pump Curves for \NWTP Pumps: forward flow/recycle pumps,
sand filter flow pumps, equalization tank grinder pumps, sludge tank decanting
pump.

Data Point ---
Flow: 147 US gpm
Head: 30 ft
Eff: 44%
Power: 2.5 hp
NPSHr: 6.54 ft
Design Curve ---
Shutoff head: 39.9 ft
Shutoff dP: 17.2 psi
Min flow: -- US gpm
BEP: 47%@18OUSgpm
NOL power.
2.66 hp @ 180 US gpm
4
10
Performance Evaluation:
Flow Speed
Company: Aqueonics
Name:
Recirculation Pump Selection
IrU,?O
" i
4,00ate: 1015/2008
1
US gpm rpm
HYDROMAT110-
%
hp
ft
4W
111,
27.9
46
2.63
Pump:
Search Criteria:
30.2
61�
Size: 30MMP
2.49
Flow: ---US gpm
Head: --- ft
Type: Self-Primer3
Speed: 1200 rpm
Fluid:
Synch speed: Adjustable
Dia: 8.4062 in
115 1200
31.9
41
2.26
Water
Temperature: 60 *F
Curve: 30MM2000
Impeller:
Density: 62.25 lb/ft'
Vapor pressure: 0.2563 psi a
Specific Speeds:
Ns: ---
Viscosity: 1. 105 cP
Atm pressure: 14.7 psi a
27
Nss: ---
NPSHa: --- ft
Dimensions:
Suction: --- in
Discharge: 3 in
Motor
Standard: NEMA
--- hp
Pump Urnits:
Enclosure: TEFC
Speed: ---
Temperature: 140 'F
Power: --- hp
Frame: ---
Pressure: 125 psi g
Eye area: --- in'
Sizing criteria: Max Power on
Design Curve
Sphere size: 2.5 in
Data Point ---
Flow: 147 US gpm
Head: 30 ft
Eff: 44%
Power: 2.5 hp
NPSHr: 6.54 ft
Design Curve ---
Shutoff head: 39.9 ft
Shutoff dP: 17.2 psi
Min flow: -- US gpm
BEP: 47%@18OUSgpm
NOL power.
2.66 hp @ 180 US gpm
4
10
0� H20ptimize Hydromatic 8
90
80
70
60
UJI
40
20
Selected from catalog: Self -Primer Pumps 60Hz Vers: Feb 2006
Performance Evaluation:
Flow Speed
Head
Efficiency
Power
NPSHr
1
US gpm rpm
it
%
hp
ft
4W
173 1200
27.9
46
2.63
8.31
144 1200
30.2
44
2.49
6.39
115 1200
31.9
41
2.26
4.55
86.4 1200
33.4
35
2.07
3.07
57.6 1200
35.4
27
1.94
1.69
0� H20ptimize Hydromatic 8
90
80
70
60
UJI
40
20
Selected from catalog: Self -Primer Pumps 60Hz Vers: Feb 2006

Operation is recommended in the bounded area with operational point within the curve limit.
Performance curves are based on actual tests with clear water at 70' F. and 1280 feet site elevation.
loom
28-
1
0 so
101 MIS
0 MINES
Is Is
Nil
MWEEN
24.
0
so mmismormal
SON
Is
Is
EMENE
so
Hill MAN
IN
MIS
20"
MIJOW1 IN
11 1
HE
0
1 101011201
1
'00"M
011011100111111111
No k , I
MEE
i Is
ism
IMMINUMIN
MEMO=
IMMENSE!
=04 omr
HLik"INIMIAMIS
1101191IRWEEK1
Il. Raq SH I
I
Is
Otis
-ROME 0110012
Billion
No
NOISOME FAIMMU
No -M
FINE
ISM
11011
u on
I
1
own
No 1
11 1-
0 50 100
150 200 250
300 .350
400
-T-�
io
�0
6 1 0 io
1001!
Operation is recommended in the bounded area with operational point within the curve limit.
Performance curves are based on actual tests with clear water at 70' F. and 1280 feet site elevation.

MP/MPH
Self Priming Sewage and Trash Pumps
CM
NOTE! To the installer: Please make sure you provide
this manual to the owner of the pumping equipment orto
the responsible party who maintains the system.
US)
rjr- HYDROMATIC'
Pentair Pump Group

I
The MP I MPH self -priming
centrifugal pump has a semi -open
impeller and suction flap valve.
Pump is designed to handle raw
un -screened sewage, mild indus-
trial waste and slurries containing
entrained solids. The material of
construction is a cast iron volute
case and bearing frame, ductile
iron impeller and wear plate.
Thank you for purchasing your
Hydromatic self -priming pump.
If there are any additional
questions not covered in this manual
please contact the HYDROMATIC
representative or HYDROMATIC
Pump Co.
Before Operation:
Read the following instructions
carefully. Reasonable care and
safe methods should be practiced
for installation and operation of
pump. Check all local codes and
requirements before installation.
Attention:
This manual contains important
information for the safe use of
this product. Read this manual
completely before using this
product and refer to it often for
continued safe product use. DO
NOT THROW AWAY OR LOSE
THIS MANUAL. Keep it in a
safe place so that you may refer to
it often.
Unpacking Pump:
Remove pump from pallet. When
unpacking unit, check for
concealed damage. Claims for
damage must be made at the
receiving end through the delivery
2
carrier. Damage claims cannot be
processed from the factory. Check
for and tighten all loose attaching
hardware. Check oil levels and
lubricate as necessary.
Warning: Before handling these
pumps and controls, always
disconnect the power first. Do
not smoke or use sparkable
electrical devices or flames in a
septic (gaseous) or possible
septic area.
Pump Not Operating Or
In Storage:
If pump is not put into service
immediately, it must be properly
stored to prevent damage. Store
unit in a dry warm location. Never
store unit in the open even if it is
protected with plastic or other
covering. The bearing housing
and motor will draw moisture,
which may result in pump failure
after being put in operation.
C,
While in storage pumps with
carbon ceramic seals must
have impellers manually rotated
(6 to 12 revolutions) after
setting non -operational for 3
months or longer and prior to
electrical startup.
Pumps with tungsten carbide seals
must have impellers manually
rotated (6 to 12 revolutions) after
setting non -operational for 3
weeks or longer and prior to
electrical startup.
Motors:
Pump unit may be shipped less
the motor for customer to supply
and mount.
Motor Types:
Pumps can be driven by Standard
drip -proof, totally enclosed fan
cooled, totally enclosed explosion
proof or drip proof with encapsulated
windings for moisture protection.
If motor is to operate in the open
or in a dusty location a totally
enclosed fan cooled motor must
be used. If pump is to operate in a
damp location a motor with
encapsulated winding should be
used. Motors are to be sized so
that no overload will exist in the
operating range of the pump.
Note: When pump units are
mounted at the factory, the
driver and pump are aligned
before shipment. During transit
and handling of pump and
components misalignment may
occur. Before operation the drive
alignment should be checked.
Shaft Couplings:
We recommend using Wood's
flexible coupling to prevent
misalignment and noise that can
be caused by other couplings. The
extra cost of the coupling is easily
saved in installation and field
service that can result from
coupling problems.
V -belt drive:
Where V -belts are used, keep belts
tight by adjusting motor base
screws. Belts should run cool. If
belts heat up it will indicate
slipping. The V -belts should be
fiddle string tight
CAUTION: Belt guards and
coupling guards must be
properly installed before
operating pump unit.
Electrical Starting Equipment:
If electrical starting equipment is
not furnished with pump, certain
precautions must be observed in
selecting motor starter.

I
I
Type Of Starter:
For three phase power a magnetic
starter with 3 leg overload
protection is recommended to
prevent motor burn out that can
occur from single phasing or
transformer faults on three phase
systems. For single-phase motors
a standard starter with 2 -leg overload
protection is recommended.
Electrical:
For motor overload protection
the magnetic starter trip amp
rating should not be more than
1.25 times the full load amps
of the motor. HYDROMATIC
recommends a rating of 1.15
times the full load amps of
the motor.
2. Always use fused disconnect
switch or circuit breaker
ahead of magnetic starter for
short circuit protection. When
duplex pumps are used and are
operated from single disconnect
switch be sure disconnect
switch is large enough to
withstand the starting current
of both pumps coming on at
once. This can occur after a
power failure, This is impor-
tant as a blown fuse or tripped
circuit breaker can make both
pumps and an alarm system
inoperative resulting in flooding
or other damage.
Ground:
Connect a ground wire to motors,
control box and other related con-
trols. Ground wired to be sized to
the National Electric Code article
250-95. Ground wire must be con-
nected to a driven ground stake or
to a ground wire from the supply
service. If a ground stake is used it
must be driven at least 8 feet into
the ground.
M
Codes:
All local wiring codes must be
observed and any exceptions to
data given must be followed in
accordance with the local code.
Consult the local inspector before
installation to avoid costly delays
that can occur due to rejection
afterjob is finished.
Pump Installation Foundation:
Pump frame or base should be
installed on a concrete floor with
proper shims and grout. Use
hardwood tapered shims to drive
under base to level. Base should
be about I to 1 1/2" off the floor.
Build form around the base and
fill base inside cavity with grout.
Foundation bolts can be set in the
grout or set in the concrete floor
with expansion bolts.
Grout should be made with I part
cement and 2 parts sand. Mixture
should be fluid enough to run
under base. Wood shim blocks can
be removed after grout has set and
holes filled with quick set cement.
Piping:
All piping to suction and discharge
openings of pump must be
supported to remove stress from
the pump case and bearing frame.
Suction Pipe:
1 . Suction pipe should be same
size as pump opening. DO
NOT use larger suction pipe as
priming time will be increased
and velocity may not be
high enough to properly
carry solids.
2. Pump should be installed as
close to the liquid being
pumped as possible with a
minimum of elbows or fittings.
To avoid air pockets suction
pipe must be as short and
direct as possible. Suction pipe
must always slope upwards to
the pump from the source of
the liquid being pumped.
4. The suction pipe should be
installed at a distance equal to
I 1h times the diameter of the
suction pipe from the wall of
the wet well, minimum.
5. The suction pipe should be
installed at a distance equal to
one half the diameter of the
suction pipe or 3" from the
floor of the wet well, minimum.
6. If more than one suction pipe
is to be installed in the same
wet well, a distance equal to
at least 3 times the diameter
of the suction pipe should
separate them, minimum.
7. Submergence of the suction
pipe is critical to efficient pump
operations. See the following
chart for recommended minimum
submergence vs. velocity.
Submergence may be reduced
by installing a standard pipe
increaser fitting at the end
of the suction pipe. The larger
opening size will reduce the
inlet velocity and required
submergence. See Figure #1.
Vertical Suction Lift:
Vertical lift should not be more
than 15 feet. This is for starting
level only. After pump primes,
level can be pumped down to 18
to 20 feet if desired, but sump
level must rise up to the original
level for restart. All suction line
joints must be air tight as a
leak in the suction pipe can
cause pump to loose prime or
not prime at all. Always
check N.P.S.H. calculations for
available atmosphere pressure
before applying purnp.
R1

Hydromatic Pump
pentair
Water
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10/412008
ENGINEERED
V
PRODUCTS
Superior Features:
-s
Grinder.. Pumps
Grinder Pump
-Carbon/Ceramic type 21 mecharfical seal
Systems
-Oil-filled motor with automatic reset thermal
Non -Clog Dry Pit
overload for maximum: protection (one phase
Pumps
models)
Non -Clog Pumps
-Upper and lower single -row ball-bearing
Self-primIng Pumps
cons-troction
Sewage Ejector
-Piggyback plug available for easy maintenance
PUrIlDS
and switch replacement
ACCESSORIES
Download PDF Saies Sheet
Control Panel�:,
Download PDF Mianual
Float Switches
Download Specification Submittal Data
VALUE
SERVICES
Specifications:
Cont'act Us
Typical High-capacity surnp/effluent,
Directions to
Application: sewage.
Hydrornatic
Capacities: up to 120 GPM (T5 LPS)
Requests
Heads: up to 28 ft (8,5 m)
Softsuare;
115V, lo, 9,5: FLA, 60Hz-
23OV, lo, 41 FLA, 6OHz'
MADE FOR YOU
4/10 HP split phase with
Click here if you are a
Motor, thermal overload protection,
Hydromatic distributor
1750 RPM
or representatives.
Intermittent Liquid 140-F (60"C)
_e'jeet__rAp40,htmI
Page I of 2
10/412008

Hydromatic Pump
Copyright C Pentair
Pump Group Ali
Rights Reserved.
I
Privoq Policy
f'enrfs and Cmdi Lion -
Temp:
Minim urn
simplex -- 18" (45-7 mm)
Recommended
Duplex = 30" (762 mm)
Sump Diameter:
Automatic
Diaphragm pressure switch
Operation:
(manual available)
Materials of,
Class 30 cast iron
Construction:
Impeller:
Thermoplastic
Discharge, Size,
T' N PT (50. 8 mm)
Solids Handling,
1-1/4" (31.8 mm)
Power Cord.:
101, $JTW (20'optional)
Performance.
0 us Q -TIN", A) 40 (11) 80 100 1 V11
flydroni.alic re.,-;erves� flie. iight to make revisions to it�
productsand their specificati Oils, this cata.log and relaW
information without notice.
'Page 2 of 2
http://vv-w w.hydroma 0.1itml 1014/2008

Company: aqueonics
"MI
Name:
�mOate: 10/5/2008
Pump Limits:
Temperature: 140 *F
Pressure: --- psi g
Sphere size: --- in
Speed: 1750 rpm
Dia: 7.0625 in
Impeller:
Ns: ---
Nss: ---
Suction: --- in
Discharge: 2 in
Power: --- hp
Eye area: --- in'
Search Criteria:
Flow: 70 US gpm
Fluid:
Water
Density: 62.25 lb/ft'
Viscosity: 1,105cp
NPSHa: 46.4 ft
16,1?0 HYDROMATIC;
Head: 23 ft
Temperature: 60 *F
Vapor pressure: 0.2563 psi a
Atm pressure: 14.7 psi a
Motor
PU AsrNlWYORRENWR to select a motor for this pump.
Catalog does not contain data to verify that NPSHa is sufficient.
;Pump:
Size: HPGF/H/X-300
Type: GRINDER-SUBM
Synchspeed: 18OOrpm
curve:
Specific Speeds:
Dimensions:
Pump Limits:
Temperature: 140 *F
Pressure: --- psi g
Sphere size: --- in
Speed: 1750 rpm
Dia: 7.0625 in
Impeller:
Ns: ---
Nss: ---
Suction: --- in
Discharge: 2 in
Power: --- hp
Eye area: --- in'
Search Criteria:
Flow: 70 US gpm
Fluid:
Water
Density: 62.25 lb/ft'
Viscosity: 1,105cp
NPSHa: 46.4 ft
16,1?0 HYDROMATIC;
Head: 23 ft
Temperature: 60 *F
Vapor pressure: 0.2563 psi a
Atm pressure: 14.7 psi a
Motor
PU AsrNlWYORRENWR to select a motor for this pump.
Catalog does not contain data to verify that NPSHa is sufficient.
LA—dH20ptimize Hydromatic 8
Selected from catalog: Grinder Pumps 60Hz Vers: Feb 2006
Data Point
8 in
Flow: 70 US gpm
Head: 23 ft
50
Eff: --- %
Power: 3 hp
NPSHr: --- ft
40
Design Curve
Shutoff head: 34.5 ft
.0 25 in
Shutoff dP: 14.9 psi
V
Min flow: 5USgpm
30
BER %
NOL power:
3 hp @ 5 US gpm
20
Max Curve
Max power:
3 hp @ 5 US gpm
10
lb
M
W 40 6 . 0
60 70
80 06 100 110 120
0.5
Z
0
10
20
30 40 50
60 70
80 90 100 110 120
4
2
0
10
2 0
3 1 0 4b 50
60 70
80 9 0 100 1 10 120
US gpm
Performance Evaluation:
Flow
Speed
Head
Efficiency
Power
NPSHr
US gpm
rpm
ft
%
hp
ft
84
1750
19.9
---
3
---
70
1750
23
---
3
56
1750
25.9
---
3
42
1750
28.6
---
3
---
28
1750
30.9
3
LA—dH20ptimize Hydromatic 8
Selected from catalog: Grinder Pumps 60Hz Vers: Feb 2006

DECANTING PUMP --
HYDROMATIC Model SK50
Tical Application
ities to
to
12
ILW6
1 + 1 .10, 120.
Lla*S�AO 2 4
Performance Curve
Sewage, High capacity sump
120 GPM (7.5 1/s)
ft (7.3 m.)
1115V, lo, 12.OFLA, 60Hz; 230V, lo, 6.OFLA, 60Hz
11/2 HP split phase w/thermal overload protection,
11750 RPM
Recommended
118" (457mm)
'Sump Diameter Duplex
....... ... ---- --
iAutomatic Operation
30" (762mm)
---- ... . ....... ..... .. .... ......
Wide angle float switch (manual available)
Materials of Construction 'Class 30 cast iron
!Impeller
XClass 30 cast iron non -clog
I
tDischarge Size 12" (50.8mm); 3" (76.2mm) optional
lSolids handling 12" (50.8mrn)
IPower cord '10', SJTW, (20'optional)
Carbon/Ceramic type 21 mechanical seal
'Superior Features
I
Oil filled motor w/automatic reset thermal overload
!for maximum protection
Upper and lower single row ball bearing
,construction
I
Piggy -back plug available for easy maintenance
iand. replacement

BULLETIN C
Cut -Sheets for WWTP Blowers

/"'^j \ 4A) ff,1/f 7'
( Mk--)
(j)
MEN
MIMM�
-
MMA
1,760
111M
46 2.6 !!!
m
4 3.0
41 3A
HP I VII -S 0,045 2265
800 76
1
1 1.6 67
2.1 63 2.5
59 3.0
56
3.5
2LP
211-S
0.035 250 91
1.3
86 1.8 B2
2.4 79 2.9
75 3.4
72
4.0
2LVP
1,760
560 102
1.4
97 2.0 93
2.6 78 3.2
86 3,7
83
4.3
7 162
2.0
157 2.8 153
3,7 149 4.6
146 5.3
143
6.1
110
5.0
107
760
149
1.9
142
2,8
135
31
130
4,5
124
5.2
120
6.1
3LP
2W�S
0.104
265
202
2.4
194
3.5
188
4.7
182
5.6
177
6.7
172
7.8
3LVP
8.2
204
2,770
254
2.9
247
4.3
240
5.5
235
6.8
230
8.2
225
9.6
-154
-7.0
1-51
3.600
341
3.7
333
5,3
27
7.1
321
8.9 1
316
10.6
311
12.4
191
8.2
187
1,760
253
3.0
24
-�-.5
�34
5.7
227
7.1
220
2%"-S
213
9,9
4LP
9.8
235
2,190
326
3.7
31
5.3
307
7,1
Soo
8 , 8
293
il,5
0.6
286
12.4
4LVP
31�s
0.170
2,620
400
4.4
389
6.3
381
8.4
373
10.6
366
, 2.7
360
14,8
188
8.8
182
3.600
566
5.8
556
8.7
54�71
1.6
539
14.5
533
17.4
526
20.3
321
133
316
1,500
463
12
5.2
449
7.5
3 8
438
10.0
427
12.4
418
14.9
409
17.4
5LP
4"-S
0.350
1,760
554
5.8
a
540
8.8
529
'2 9
11.7
518
IC6
509
17.5
Soo
20.4
5LVP
17.7
450
2,100
P Alin
673
an r2
0
659
9"
1 M
14.2
648
13.9
18-9
637
900
17.4
P -q 6
628
RAn
20.9
PA4
619
681;
24.4
�3j
332
14.2
326
1,170
739
E7.
8.0
716
11.9
L4
697
15.9
680
19.9
664
23.9
650
27.9
6L p
1TS
434
20A
1,162
, 0
12.0
1,139
18.0
1,120
24.0
1,103
29,9
1,088
35.9
1,074
41.9
6LVP
6"-F
0,718
11:761
930
1,284
13.1
1,261
191
1,242
26.3
1,225
32.8
1,210
39.4
1,196
46 , 0
655
25.0
649
2.350
1586
32.1
1 s9q
94 n
1544
32,0-
1,527
40,0
1.512
48.0
1.4Q7
560
363
16.5
354
1,170
1,277
13
1::4'
20.0
1,224
16.6
1,203
33.3
1,184
39.9
170
7LP
8`-F
1.200
25.1
1,6;3 ,
1 a�'7
1 .2
25�O
1.578
33.3
1,557
0.7
1,538
50.0
0.566
1:375
7LVP
2
25.8
634
11:465
760
1,985
20.0
1,966
30.0
1,932
40.0
1,911
50, 1
1 892
60,
1,800
884
33.8
875
2.050
2.333
23.3
2.304
85.0
2,280
46.6
2.269
58.3
2:240
70..
6" 1 '6
14,5
1,329
21.8
1,298
29.0
1:27;51
3' 3
':"'
" 5
SLP
10`�F
740
1,171 1:'.71
19.3
1,834
28.9
1,803
38.6
1
1
48:2
1 750
57.9
SLVP
Ll .
1,375 2,228
22.7
2,191
34.0
2,159
45.4
2.
56.7
2,107
68.0
1,800 2,967
297
2,930
44.5
2,899
59.4
1 2.
74.2
2.847
, 89.1
uh, - "11�
M,
uNgeim
2,800 25
1.7
22
2.1
2MP
ill -S
0.017
3250 33
3:560 38
1 9
2'. 1
30
35
Z5
2.7
28
34
2.7
3.0
&
7
7 r
2MVP
5275 67
3.1
64
3,9
63
4.4
60
5.1
1,760
64
3.6
59
4.6
45
Imp
3mvp
2"-S
0.060 A
��265
. 7t
95
-1 2V
- 4.6
5.5
- 89
11-6-*'
7.1
87
117
6.4
7.9
112
9.5
3�600
176
7.2
1 169
9.2
167
10,2
162
12.3
1
1
1,760
144
6.8
136
8,8
132
4MP
-S
0.117
2,190
194
8.5
186
1 0.9
182
19.8
2.1
4MVP
2,620
245
1 0.2
236
13.1
233
14.5
3,600
359
1 4.0
351
18.0
347
20.0
-
-
1,500
237
10.5
227
13 , 4
222
14.9
213
17.9
209
19A
amp
4"-,9
0.210
1�760
292
12.3
2Bl
15.8
277
17.5
268
21.0
263
22,8
5mvp
2,100
363
14.6
353
18.8
348
20.9
339
25.1
335
27.2
2.850
521
19.9
510
25.5
506
28.4
497
34�O
493
36.9
1,170
332
14.9
316
191
309
21.2
296
25.5
269
27.6
283
29.7
Imp
5"-S
0.383
1
111
22.4
542
28.8
5 35
32.0
522
38.3
515
41.5
509
44.7
6mvp
1:761
930
622
24.5
607
31.5
600
35.0
587
42.0
580
45.5
574
49.1
2.350
784
29.9
768
38.4
761
42.7
748
51.2
741
55.5
735
59.7
1,170
693
28.5
671
36.6
661
40.7
7mp
6`-F
0,733
1 6 1
909
35.6
887
45.8
877
50.9
7MVP
760
,:4
1,125
42.8
1,103
55.0
1,093
61.1
2,050
1,338
49.9
1,316
64.1
11,306
1 71 2
ISO
9
30.4
681
39.0
669
43�
amp
T -F
1.040
1 170
1,011
40.4
983
51 �9
970
5 .7
1
8mvp
1:375
1,224
47.4
196
11:638
6 1.0
1,183
67.8
1
1
1 1,800
1 1,666
62.1
.
1 79.9
1,625
88.7
MEN
MIMM�
-
1,760
111M
46 2.6 !!!
m
4 3.0
41 3A
HP I VII -S 0,045 2265
69 3.4
66 3.9
64 4.3 60 5.3
VP P:770
91 4.1
7
89 4.7
7�4
87 5.3 83 6.5
3,600
129 5.4
126 6.1
124 6.9 120 8A
7-
117 10.0 113 11.5
'3 --
-
1,760
so
4.0
7
77
46
-
74
5.2
p
4 HP
H
I WI -S
0.069
2190
110
5.0
107
5.7
104
6.4
99
7.9
HVP
4 H V p
2:620
139
6.0
137
6.9
134
7.7
129
9.4
124
11.1
3,600
207
8.2
204
9.4
201
106
196
13.0
192
1 15.3
188
17
-T�5-00-
-154
-7.0
1-51
8.0
147
9.0
140
10.9
5HP
5 H p
1,760
191
8.2
187
9.3
183
10.5
177
12.8
171
15.2
111
1"
17 1
H V p
5HVP
I
2%"-S
OA40
2,100
238
9.8
235
11.1
231
12.5
224
15.3
2 is
18.1
213
20.9
2,850
3
13.2
34
15A
336
17.0
329
20.8
323
24.6
31872
8.. 4
"
1,170
188
8.8
182
10A
177
11.3
-
168
13.8
159
16.4
.'p
6HP
1 760
321
133
316
15.1
311
1TO
302
20.8
293
24.6
266
28.4
6HVP
6 Vp
3"-S
0.227
1:930
360
14.5
355
16A
350
18.7
340
22A
332
27.0
324
31.1
2,350
455
17.7
450
20.2
445
22.8
436
27.8
427
32.9
419
37.9
1,170
332
14.2
326
16.3
319
18.3
308
22.4
297
26.5
287
30.5
p
7HP
465
441
1TS
434
20A
428
22.9
416
28.0
405
33.1
396
38.2
Vp
7HVP
4"-S
0.367
1,760
549
21.4
542
24.5
536
27�6
524
33.7
514
39.8
504
45.9
21050
655
25.0
649
28.5
642
32.1
631
39.2
620
46.4
610
5 .5
Sao
363
16.5
354
18.9
345
21.2
329
26.0
315
0.7
301
35.4
8HP
170
528
528
22.0
22-0
518
25.1
509
28.3
493
34.5
479
40.6
465
47.1
8 Vp
BHVP
4",S
0.566
1:375
644
644
2
25.8
634
29.5
626
33.2
609
40.6
595
48.0
581
55.3
1,800
884
33.8
875
38.6
866
43.5
850
53.1
835
62.8
822
72A
5 RPAA

I
I
I
Proven Performance. Global Applications. Local Support.
Below are just a few examples of the industries that,
over the decades, have depended Upon the Sutorbilt'
Legend- to deliver clean, oil -free air to a wide range
of global applications.
Industry Application
Aquaculture
Aeration
Cement and Lime
Fluidization and Conveying
Chemical
Vacuum Processing and Conveying
Coal Bed/Landlill
Methane Gas Recovery
Dairy
Automated Milking
Dry Bulk Hauling
Trailer Unloading and Aeration
Environmental Services
Sewer Cleaning and
Portable Restroom Services
Industrial
Material Vacuuming
Milling and Baking
Blending and Conveying
Oil and Gas
Gas Collection and Sparging
Power Generation
Fly Ash Conveying and Aeration
Process Gas
Gas Boosting
Pulp and Paper
Chip Conveying and
Process Vacuum
Resin and Plastic
Processing and Conveying
Soil Remediation
Vacuum Extraction and Sparging
Vacuum Excavation
Potholing and Slurry Recovery
Wastewater
Aeration and Backwashing
The sound data shown compares
the Legend and a comparably sized
blower operating at 3,275 rpm and
12 psig. An improved blower design
significantly reduces the sound
pressure output of the Legend
blower. The typical reduction is
3 dBA which represents 50% less
noise than the competition.
Superior Local Sales and
Service
Our extensive network of authorized
Sutorbilt distributors offers the most
convenient local sales and service sup-
port of anyone in the industry today.
These factory trained professionals
are experts in btower/vacuum. pump
technology providing system instaRation guidance, troubleshooting and
optimization recommendations of your new or existing applications.
Even a Legendary Warranty
Every Sutorbilt Legend Series blower/ vacuum PUMP is covered by
an uncontested warranty for 24 months from the date of shipment
or 18 months from the date of installation on all blower materials
and workmanship. Replacement or repair costs will be at no charge
. 1 1. r . f � — � ­ ---I C'.____L:1_

14 =-.* Small Compact Filter Silencers
w/ Standard Filter Design
TS" Series 1/2" - 3" MPT
-APPLIGA-TIONIE��EQU�FP�ME-60��4
+ Industrial &Severe Duty Engines + Waste Water Aeration
# Piston Compressors Constructlon\Contractor Industry 4 Nailers and Staplers
+ Screw Compressors Workshop + Vacuum Vent Breathers
+ Blowers - Side Channel & P.D. # Medical0ental Industry
o Hydraulic Breathers — fine filtration o Pneumatic Conveying
+ Polyester: 99%+ removal efficiency standard to 5 micron + Interchangeable media: Polyester, Paper, HEPA
# Paper: 99%+ removal. efficiency standard to 2 micron + Several element sizes available per given connection
# Fully drawn weatherhood - no welds to rust or vibrate apart (safety factor)
# Tubular silencing design - tube is positioned to maximize + Temp (continuous): min -1 5oF (-26'C ) max 2207 (1 04*C
attenuation and air flow while minimizing pressure drop * Filter change out differential: 10"-15" H20 over initial delta P
* Durable carbon steel construction with baked enamel + Pressure drop graphs available upon request
finish and powder coated weatherhood
+ 1/8" tap holes # Available in Stainless Steel + Various media available
# Pressure Drop Indicator * Epoxy coated housings # Special connections, BSPT
CONFIGURATON DRAWNG
DOLE7
4LET
Dimension tolerance + 1/4"
Wi " W/Pe
11h ��L —Cm 15tV —7
TYPICAL NOISE ATTENUATION — FS SEFUES
20
Z
0 10 '000 !-Wih
L. li� �L. * '�; 71�; 4oloo aolw
OCTAVE SMID MTEI FREGUENCIES — HZ
Noise attenuation may very due to the wide range of
applications and machines
Note: Model offerfngs and design parameters may change without notice.
Solberg — Discover the Possibilities
FS25-406 pg. 3
1151 Ardmore Ave. 4 Itasca, IL 60143 USA
Sales/Service: 630,773.1363 � Fax: [phone]
E-mail: [e-mail] # Web Site: www.solbergmfg.com
with
Polyester
Element
v0th
Paper
Element
MPT
Outlet
DIMENSIONS - inches
A B C
(Rated Flow SCFM)
fc—rew
(2EE� Element
Piston Fan Rating
No. of
Silencing
Tubes
Approx.
Wt. lbs
I
FS -15-050
FS -14-050
1/2"
4
1 1/2
6
10
10
35
1
2
I
FS -15-075
FS -14-075
3/4"
4
1 1/2
6
20
25
35
2
2
1
FS -15-100
FS -14-100
V
4
1 1/2
6
25
35
35
3
2
I
FS -19P-150
FS -18P-150
1 1/2"
65/8
1 5/8
6
70
85
100
5
4
I
FS -31 P-200
FS -30P-200
2"
7 1/4
21/4
10
85
6135)
195
5
8
S
FS -231 P-20-0
1 FS -230P-200
2"
121/4
21/4
10
135
135
300
5
N
- '0� 1,
Note: Model offerfngs and design parameters may change without notice.
Solberg — Discover the Possibilities
FS25-406 pg. 3
1151 Ardmore Ave. 4 Itasca, IL 60143 USA
Sales/Service: 630,773.1363 � Fax: [phone]
E-mail: [e-mail] # Web Site: www.solbergmfg.com

BULLETIN D
Cut -Sheets and Pump Curve for Irrigation Dosing/Flushing Pump

!FF
4
Marr,"
11111M
BEIM]
111111ml
Mul
milli

�0/16/2008 12;21pm wwsi
7792766535 #439 Page 11/12
c On By: TGJ
LC - 20953 Configured Curve Date: lo/g/200S
",",Pumps Rev.#
rc)j - ect Waste Water Systems ag 9 P-1 P-2 IP -0.
Model: 209S3
__f_-
69
Qty: 2
SPE
.9DU 0UU JbU 400 450 Soo 550 600 650 700
capacky - usgpnl
1+U
20 -
0.
I" 4;vw _1W JuU J�)U 400 450 Soo 660 600 650 700
capacky - Usgpm
U �U 100 ISO �00 250 300 350 400 450 Soo $50 Soo 650 700
capacay - usgpm
N
r
IPSHr i
.... ... . ................ ...... . ......
. .. .. ......
U �U 100 ISO �00 250 300 350 400 450 Soo $50 Soo 650 700
capacay - usgpm
N
PU
200 USspm
�Fluid: Water
Uct Press: 0.00 PsLa
;H:
350 ft
Tamp: 68.00 dog F
DI
Dls. Press-
�fttoff Head;
363 ft
0.998
5iff. Press:
NPSHr
7.04 ft
Visc.; I �60 cp�-gg
0
SHP: 310.3 hp
Iffi-)- Dig-:
9.54 In
jPump Eff.- 58.16
N�� Of Stages:
I
REP' 426 USgprn
D
40
lVoltage: 208-2301460
7
tL inal RPM.,
3500
... I I Phase: Three phase
1
F.. 1.15
ctual RPM-
3500
—
-
[Encl,: ODP
-1
PU

SELECTIOW
CaNDITTOWS
Flow:
Total Dynamic Hend:
200.0 GPM
140.0 feat
Priming Type:
M-ot-or Loading.
Standard,
Sta n d"a rd,
PUMP DESCRIPTION
Pump Model:
92TPMS
Pr�rnfng Type:
Ston-dard
Impeller Diameter:
6. 18 a i.n.
lrr-p-al-ler Material;
Iron
Suction;
2Yz"NPT
Digcharge:
2)"WPT
Shaft Seal;
Mechonicas
PUMP PERFGRMANCE
Flow:
ToLal Dynamic Head;
200.0 GPM
140-6 feet
po.wer.
Efficiency:
q.-7 EtIl. P
Nominal Speed.,
3600 Rpm
NPSHR:
73;4 7
'14..2 feet
Shut—Off Head:
154.3 feet
Max Power:
T'T.(J ErHP.
Sest Eff; 73.7 @r 2 1- 4.9 OPM
MOTOR
Size:
70 HP
Enclosure:
TEFC
Voltage; CorisulL Catcflog/Facto,ry
PRICE/ORDER
INFORMATION
Ca t a I n 9 N
Factory
wcigh L:
200 lbs.

BULLETIN E
Cut -Sheets for Flushing Return Pumps and Tanks

�Kl& IrY lallURS . FINZ-F /9, 7,q
Product information presented
here reflects conditions at time
of publication. Consult fac-
tory regarding discrepancies or
inconsistencies.
SECTION: 3.20.022
FM2D91
0207
Supersedes
0506
visit our web site:
www.zoeller.com
ZOE1616ER ONmSITE WASTEWATER PRODUCTS
a
Effluent turbine pumps are used in on-site applications that
demand more head than a traditional single stage centrifugal
submersible pump. Zoeller Pump Company is able to meet this
need by offering a complete line of submersible effluent turbine
pumps. These pumps have been proven in field applications and
have many years of development behind them. Typical appli-
cations include mound systems, drip systems, and recirculating
media filters. All units include cool running submersible motors
that do not require external water flow to prevent overheating.
An outer pump sleeve is not required. Pumps can be installed
directly in a dose tank as long as an effluent filter is used on the
septiGtank outlet. These pumps can also be used in conjunction
with the Zoeller Effluent Turbine Filtered STEP system.
FEATURES:
* Corrosion resistant.
* Many models available - 10, 19, 27, 35, 55 and 85 GPM.
* 1/2 thru 3 HP units.
* 115 and 230 Volt.
* 1-1 /4" discharge (10, 19, 27 gpm) or 2" discharge (35, 55
and 85 GPM).
10, 19,27 GPM Models 35, 55, 85 GPM Models
* Heavy wall stainless steel pump shell.
* Franklin Electric submersible motors.
* Stainless steel hex drive pump shaft.
* High Efficiency floating stack.
-DISCONNECT
* Glass -filled Noryl discharge and mounting ring
(10, 19, and 27 GPM models).
TO
DRA N
* Stainless steel discharge and mounting ring
TO
CONTROL FIELD
PANEL
(35, 55 and 85 GPM models).
* No external capacitors or relays required for starting
PREWIRED -J
CONDUIT
(1/2-11/2 HP).
* Starting box provided for 2 & 3 HP units.
* External check valves available.
* Pressure effluent filter available.
* 10 feet of jacketed SO type power cord (1/2 - 11/2 HP units
only). Consult Factory for longer lengths.
* Timed dosing panels available.
* 5 year extended warranties available. (Consult Factory
for details.)
SK2226
@ Copyright 2007 Zoeller Co. All rights reserved.

i 1:
U�LA
rl,N
75
70
65
60
56
50
45
40
35
30
25
20
15
10
6
0
co
LU
PUMP PERFORMANCE CURVE
85 GPM
2" NPT DISCHARGE
60 — 200 — 1 1
3 HP -6 STAGE
55 — 175 _�_.l 1
50 —
45 — 150
40 — STAGE
2 HP -4
< 125
z
35 —
_5HP
30 — 100 — 3 STAGE
25 — 75
20 — 1 HP -2 STAGE
15 — 50 —
10 — 3/4 H P-1 STAGE
25 -
5-
0 1
20 40 60 80 100 120 140
GALLONS
LITERS '
�FTERS 0 410 810 1210 1610 2010 2410 2810 3210 3 (T) 0 8� 1�0 2� 3�O 40'0 4 8'0
FLOW PER HOU RIMINUTE 015649 FLOW PER HOURIMINUTE 015845
- -Part Number
PUMP PERFORMANCE CURVE
55 GPM
Voltage
2" NPT DISCHARGE
Amps
Stages
Height
6034-0005
112
115
1
3 HP -7 STAGE
1
18-5/16'
225 —
112
230
1
6.0
1
18-5/16'
5034-0007
—
230
1
8.0
200
21-9/16'
5034-0008
1
175 —
1
9.8
3
24-3/4'
2 H P-5 STAGE Ilk
1-1/2
230
150 —
13.1
6
30-3/16'
5034-00101 1
2 1
230
1 1
13.2
1.5 HP -4 STAGE
32-5116'
1 5034-10011* 1
125
230
1 1
14.5
1 7
40-71W
100 —
1 HP -3 STAGE
See FM2244 for more information.
See FM2090 for more information.
75 —
3/4 H P-2 -0-1 AG E
60 —
112 H P-1 STAGE
NNI
10 20 30 40 60 60 70 80 90 10
GALLONS
co
LU
PUMP PERFORMANCE CURVE
85 GPM
2" NPT DISCHARGE
60 — 200 — 1 1
3 HP -6 STAGE
55 — 175 _�_.l 1
50 —
45 — 150
40 — STAGE
2 HP -4
< 125
z
35 —
_5HP
30 — 100 — 3 STAGE
25 — 75
20 — 1 HP -2 STAGE
15 — 50 —
10 — 3/4 H P-1 STAGE
25 -
5-
0 1
20 40 60 80 100 120 140
GALLONS
LITERS '
�FTERS 0 410 810 1210 1610 2010 2410 2810 3210 3 (T) 0 8� 1�0 2� 3�O 40'0 4 8'0
FLOW PER HOU RIMINUTE 015649 FLOW PER HOURIMINUTE 015845
- -Part Number
H P
Voltage
Phase
Amps
Stages
Height
6034-0005
112
115
1
12.0
1
18-5/16'
6034-0006
112
230
1
6.0
1
18-5/16'
5034-0007
3/4
230
1
8.0
2
21-9/16'
5034-0008
1
230
1
9.8
3
24-3/4'
5034-0009
1-1/2
230
1—
13.1
6
30-3/16'
5034-00101 1
2 1
230
1 1
13.2
1 5
32-5116'
1 5034-10011* 1
3 1
230
1 1
14.5
1 7
40-71W
Part Number
H P
Voltage
Phase
Amps
Stages
Height
6035-0005
314
230
1
8.0
1
20-1/8'
5035-0006
1
230
1
9.F
2
24"
5035-0007
1-1/2
230
1
13.1---
3
30-1/8'
5035-OOOB*
2
230
1
13.2
4
32-7/8'
6035-0009*
3
230
1
14.5
6
42-3/8'
I*Includes starter box and 2& long flat wire cable assembly.
@ Copyright 2007 Zoeller Co. All rights reserved
*Includes starter box and 251ong flat Wre cable assemUy.
Accessories
Filtered STEP System
Zoeller Pressure Effluent Filter
This Zoeller Filtered STEP
The Zoeller Pressure Filter will help
System is designed as an
prolong the life of an on-site drainfield
economical and reliable
by filtering out solids which cause
solution to an On -Site
plugging. Used in both residential and
pumping requirement,
commercial applications, this unique
When the effluent must
design and mounting location allows
be pumped up hill, for
easy access to the filtering screen.
enhanced flow, pressure
sewer or where alternative
Use in low-pressure pipe, drip, or
systems require high head,
enhanced flow applications. Use asa
the Filtered STEP System
prefilter for dosed treatment devices
is the answer without the
such as recirculating media filters.
extra cost of a pumping
chamber.
For use with pumps up to
55 GPM. Contact Factory
for 85 GPM applications.
See FM2244 for more information.
See FM2090 for more information.
@ Copyright 2007 Zoeller Co. All rights reserved

1�7
ugs�
_J
= _,Trr_�
All brass spring loaded check valves are designed to
screw directly into the pump discharge. Check valves
are assembled with components suitable for a septic
environment. Check valves should be used at the pump
in a pressure sewer system. A redundant PVC check
valve and isolator (ball) valve should also be used at
the sewer connection in pressure sewers.
Part
Number
Piping
Size
Pressure
Rating
Weight
30-0187
1-1/4"
400 psi
2 lbs.
30-0189
2"
400 psi
3 lbs.
10N
PVC check valves can be used inline with the pump
discharge piping or at the street service connection in a
pressure sewer system. Check valves are a true -union
design so they can be removed and serviced without
cutting the pipe. Clear PVC for easy inspection and
connection via a glue joint.
Part
Number
Piping
Size
Pressure
Rating
Weight
30-0207
ill
125 psi
1 lb.
30-0209
1-1/2"
125 psi
1 1 lb
30-0210
2"
125 psi
I
Rail systems are used for easy pump removal from an efflu-
ent pit. Service personnel will not need to enter a hazardous
environment. Pump sits on floor and engages piping system
via a sliding disconnect fitting. All parts are stainless steel or
brass and suitable for a septic environment.
Part
Number
Piping Size
Weight
39-0098
1-1/4" Female pipe thread
10 lbs.
39-0099
1-1/2" Female pipe thread
11 lbs.
39-0100
2" Female pipe thread
12 lbs,
Disconnects Onlv
Part Pipe
Number Size
Weight
39-0053
1-1/4"
2 lbs.
39-0001
1-1/2"
2 lbs.
139-0002 1
2"
1 2.5 lbs
Stainless Steel Pull Rods
3/8"-16 UNC
Part Number
Length
39-0069
11
39-0006
2%'
39-0007
3% .
39-0008
4%'
39-0009
5%'
39-0018
39-0010
ALL ZOELLER ON-SITE WASTEWATER PRODUCTS MUST BE INSTALLED IN ACCORDANCE WITH LOCAL AND/OR STATE PLUMB-
ING AND/OR HEALTH DEPARTMENT CODES.
Q Copyright 2007 Zoeller Co. All rights reserved.

Part Number
H P
Voltage
P
9
9
5030-0005
1/2
115
1 12.0
6
22-3/8'
5030-0006
112
MOW=
1 6.0
6
22-3/8'
5030-0007
112
115
1 12.0
8
24-1/8'
10 GPM Models
1/2
19 GPM Models
1 6.0
8
24-1/8'
5030-0009 ,
314
230
1 8.0
12
28-7/8'
2" NPT DISCHARGE
BB
300- t1ki w
56-
!
20
Lj
PUMP PERFORMANCE CURVE
1
-T
48-
PUMP PERFORMANCE CURVE
72-
ami
140 - -1 HP- 4 STAGE
10GPM
IHP-7 GE
22
40-
A
19 GPM
2g] 3/4 HP
17011
120-
1 1 /4" NPT DISCHARGE
32-
L314 HP,- 3 STAGE "It,
1%" NPT DISCHARGE
'r
1�1
120-
400-
1 1
z
280 -
24-
so -
V2 HP - 2 STA�E
1
112 -
In HP- 4 MGE
114 HP, 12 3TAGE
—+,
120-
9 STAGE
so-
380
%._�
24�
80 -
40-
1 04-
T--
16-
40 -- — — — —
72-
240
314 HP —
20 -- — — — — —
0
2
10 20 30 40 50 60
7 GE
10 95 40
I
GALLONS
GALI
LITERS
------
64-
200
__ __ —
6 �O A 66 do 1`00 1T20 IE
0 40 80 120 160 200
80-
FLONPERMINUTE 015045
112 HP- a STAGE
FLOWPERMINUTE 016044
56-
72-
48-
160
so-
0
1/2 P-GSTAGE Is
< 40-
120 -
1/2 P
H
48-
ISO-
It.
32-
6 STAG
E
IP
40-
120-
&—.
24 -
32 _
16-
-
8 0
-
40-
24
40-
8-
0
5 10 15 20 25 30
2 4 8' lb 12 14 16 18
GALLONS I
GALLONS
LITERS
LITERS
I I
0 8 116 24' 32 40 '4856 64
0'
2'0 410 610 810 1010
FLOW PER MINUTE
FLOW PER MINUTE
L1W
015413
015414
Part Number
H P Voltaoe I Phase Am s I Sta es wl� ki
Part Number
H P
Voltage
P
9
9
5030-0005
1/2
115
1 12.0
6
22-3/8'
5030-0006
112
230
1 6.0
6
22-3/8'
5030-0007
112
115
1 12.0
8
24-1/8'
5030-0008
1/2
230
1 6.0
8
24-1/8'
5030-0009 ,
314
230
1 8.0
12
28-7/8'
Part Number
H P
Voltage
Phase Amps
Stages
Height
5031-0005
112
115
1 12.0
5
21-15/16'
5031-0006
1/2
'230
E230
1 6.0
5
21-15116"
5031-0007
3/4
'230
1 8.0
7
25-1116'
5031-0008
1
230
1 9.8
9
28-1/8'
Part Number
H P
Voltage
Phase Amps
Stages
27 GPM Models
5032-0005
35 GPM Models
115
-
1 12.0
4
21-1/8'
5032-0006
JHP
1/2
230
PUMP PERFORMANCE CURVE
4
21-1/8'
6032-0007
3/4
27 GPM
1 8.0
PUMP PERFORMANCE CURVE
24-5116'
6032-0008
1 114"NPT DISCHARGE
230
35 GPM
7
go
320
1-112.
230
r-1
10
11/2HP- IOSTAGE
2" NPT DISCHARGE
BB
300- t1ki w
56-
!
20
I-WHP-5STAGE
1
-T
48-
'so-
7 7: IN
72-
'_ x
140 - -1 HP- 4 STAGE
IHP-7 GE
22
40-
A
L-�J
2g] 3/4 HP
17011
120-
56-
32-
L314 HP,- 3 STAGE "It,
'r
100
4B
�43'
z
1 40-
24-
so -
V2 HP - 2 STA�E
In HP- 4 MGE
—+,
120-
so-
24�
80-
40-
16-
40 -- — — — —
20 -- — — — — —
0
10 20 30 40 50 60
10 95 40
I
GALLONS
GALI
LITERS
------
.TTERS
__ __ —
6 �O A 66 do 1`00 1T20 IE
0 40 80 120 160 200
FLONPERMINUTE 015045
FLOWPERMINUTE 016044
Part Number
H P
Voltage
Phase Amps
Stages
Height
5032-0005
112
115
-
1 12.0
4
21-1/8'
5032-0006
JHP
1/2
230
1 6.0
4
21-1/8'
6032-0007
3/4
230
1 8.0
6
24-5116'
6032-0008
1
230
1 9.8
7
26-7116'
5032-0009
1-112.
230
1 13.1
10
31-7/8'
Part Number
H P
Vdtage I
Phase Amps
Stages
Height
5033-0006
112
115
1 12.0
2
19-7/16'
5033-0006
1/2
230
1 6.0
2
19-7116-
5033-0007
3/4
230
-1-3
1 8.0
22-3/1--
T
503M008
1
230
1 9.8
_4
24-15/16-
6033-0009
1-1/2
230
1 13.1
6
29-15/16'
�n,' 11 11
Copyright 2007 Zoeller Co. All rights reserved.

�J
Part Number
H P
Voltage
Phase
Amps
Stages
Haight
5030-0005
1/2
115
1
12.0
6
22-318'
5030-0006
1/2
230
1
6.0
6
22-3/8'
5030-0007
112
115
1
12.0
8
24-1/8'
5030-0008
10 GPM Models
230
19 GPM Models
6.0
8
24-1/8'
1 5030-0009 1
314
1 230
1 1 1
8.0
1 12
1 28-718'
2 0-
1-1/2HP-58TAGE
80-
260-
48-
PUMP PERFORMANCE CURVE
72-
'-
PUMP PERFORMANCE CURVE
40- -1 HP -48 E
TAG
IHP-7$TAGE
20
10GPM
19 GPM
120
11/4" NPT DISCHARGE
32-
314HP 3 STAGE
1%` NPT DISCHARGE
10
120-
400-
1 1 1
280 -
1%
W 2H P-4ST AGE
24-
112-
3A HP- 12 STAGE
12 - 1 .
-7�
so -
rl-_]
I HP 9 STAGE
32-
10
is -
60
24-
SO-
40-
u,j
a-
104
16-
72-
240 -
k/4 H
314 HP
213-
0
10 20 30 40 50 60
7,T
7 STAGE
0 25 Is 40
GALLONS
10
64 -
a 40 80 120 16 2GO
FLCWPERMINUTE 015045
FLOW PER M INU TE 015044
200 -
`0 -
112 HP- 8 STAGE
56-
72-
240-
48 -
160 -
6�4 -
56-
112 H
< 40-
120 -
1/2 HP
32-
5 STAGE
413 -
NA
<
40-
24 -
8
120 -
32-
Is-
24-
80-
40
16 -
40-
0
6
10 1
� 20 26 30
0-
GALLONS
GAL�L �NS
24681012141618
LITERS
0
20 40 60 80 100
LIT12RS 0
8, 1'8 24 32 0 48 56 64
FLOW PER MINUTE
FLOW PER MINUTE
015413
015414
�J
Part Number
H P
Voltage
Phase
Amps
Stages
Haight
5030-0005
1/2
115
1
12.0
6
22-318'
5030-0006
1/2
230
1
6.0
6
22-3/8'
5030-0007
112
115
1
12.0
8
24-1/8'
5030-0008
1/2
230
1
6.0
8
24-1/8'
1 5030-0009 1
314
1 230
1 1 1
8.0
1 12
1 28-718'
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5031-0005
1/2
115
1
12.0
5
21-15/16"
5031-0006
112
230
1
6.0
5
21-15/16'
5031-0007
314
230
1
8.0
7
25-1116'
5031-0008
1
230
1
9.8
9
28-1/8'
Part Number
H P
e
Voltage
Phase Amps
Stages
Height
27GPMModels
112
35 GPM Models
1 12.0
4
21-1/8'
5032-0006
112
230
1 6.0
4
21-1/8"
PUMP PERFORMANCE CURVE
27 GPM
314
PUMP PERFORMANCE CURVE
1 8.0
6
24-5116'
I 114'NPT DISCHARGE 5
1
35 GPM
1 9.8
7
26-7/16'
1 11 HP- 10 STAGE
1-1/2
2" NPT DISCHARGE
1 13.1
10
1--718-
3 0
56-
180-
BB_
2 0-
1-1/2HP-58TAGE
80-
260-
48-
160
72-
'-
40- -1 HP -48 E
TAG
IHP-7$TAGE
20
40-
21- 3M HP
6MGE
120
32-
314HP 3 STAGE
10
46-
1%
W 2H P-4ST AGE
24-
so- 1/2HP-2STA E
12 - 1 .
-7�
60
32-
10
is -
24-
SO-
40-
u,j
a-
16-
20-
213-
0
10 20 30 40 50 60
0 25 Is 40
GALLONS
10
LITERS
a 40 80 120 16 2GO
FLCWPERMINUTE 015045
FLOW PER M INU TE 015044
Part Number
H P
e
Voltage
Phase Amps
Stages
Height
5032-0005
112
115
50
1 12.0
4
21-1/8'
5032-0006
112
230
1 6.0
4
21-1/8"
5032-0007
314
230
V23
1 8.0
6
24-5116'
5032-0008
1
230
1 9.8
7
26-7/16'
6032-0009
1-1/2
230
1 13.1
10
1--718-
Part Number
H P
Voltage
Phase Amps
Stages
Height
5033-0005
1/2
115
1 12.0
2
19-7/16'
5033-0006
112
230
1 6.0
2
19-7/16'
5033-0007
314
230
1 8.0
3
22-3/16'
5033-0008
1
230
1 9.8
4
24-1511 IF
5033-0009
1-112
230
1 13.1
6
29-15116"
Copyright 2007 Zoeller Co. All rights reserved.

Cable Guide: SJOW. Junior hard service, same construction as type SOW but only rated for 300V Oacket thickness different). 601C.
*Dry run capable for up to 24 hours Without damage.
**Minimum Liquid Level (measured from bottom of pump). 9) Copyright 2006 Zoeller Co. All rights reserved.

7
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Fit

BULLETIN G
WSI PC Controller Electrical Schematics
L,J

PUMP A & B 120 VAC
DISCONNECTS DISCONNECTS
CONTACTOR A
FM�
OVERLOAD A
CONTACTOR B
FIR
OVERLOAD B
120V POWER
DISTRIBUTION
BLOCKS
IFM
MIM -M
M-12MKu"11
IF" -0111=211w,
IMMIRMHr"],
IF--11111"KIM,
1"Emnf"11
1F"-1nMp0Fw1
NF"—]Z��rwvll
Ir"Ir"IMOM,
11"R�Kr"11
I M11 I 191FLITIF11
24 VAC CONTROL
TRANSFORMER
(o
24 VAC ISOLATION
TRANSFORMER
C- L '7 ..
o D� 2 1' -8 -
RACK I
0' E E -------
0 Fw m7m m7m a7a cp 0 MIM 010 MIT 010 010 V(D V(D 010 M
0 0 7-0
M6
DIL..",
. . . 14 1�
FF -e-1
+12 VDC POWER
SUPPLY
F 7;�
IN 1.
. . I
le 01
F -p -31
S 11 L
SCP30 J -DN
+5 VDC POWER
SUPPLY
IN IN
0.
G (DI
.... an
- - . aa.,
............ w.04 --al!".)
DISTRIBUTION
BLOCKS 11 - 30
0
0j
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1 of 1 Waste Water
REV -0
Rose Hill P.O. BOX 1023
"PercAR.ite" DATE: 09/22/07 Fl I IJAY (A -�O.F)4n
Systems, Inc.
[phone]
F,, (7r)r,)
MEMMMMM
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1 of 1 Waste Water
REV -0
Rose Hill P.O. BOX 1023
"PercAR.ite" DATE: 09/22/07 Fl I IJAY (A -�O.F)4n
Systems, Inc.
[phone]
F,, (7r)r,)

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1 of 1 Waste Water Systems, Inc,
REV -0
Rose Hill P.O. BOX 1023 [phone]
DAT I E: 09 / 1 22/07 ELLIJAY, GA. 30540 Fox [phone]

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1 of 1
Waste Water Systems, Inc.
REV -0
Rose Hill
DATE . 09/2 1 2/07
P.O. BOX 1023 [phone]
ELLIJAY, GA. 30540 Fcx [phone]

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1 of 1
Waste Water Systems, Inc.
REV -0
Rose
Hill
P.O. BOX 1023 [phone]
"PercdRite"
DATE:
09/22/06
ELLIJAY, GA. 30540 Fox [phone]

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REV -0
Rose Hill P.O. BOX 1023 [phone]
"P e rc,i RJ t e DATE: 09/2 1 2/07 FLILIJAY, (,A. .30.54n FnY (7nr))

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1 of 1 — Waste Water Systems, Inc,
REV -0
RDse Hill P.O. BOX 1023 [phone]
"Perc.gR.ite" DATE: 09/2 . 2/07 F111JAY (A -�n.'�40 Fw (70r,)
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REV -0
RDse Hill P.O. BOX 1023 [phone]
"Perc.gR.ite" DATE: 09/2 . 2/07 F111JAY (A -�n.'�40 Fw (70r,)

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REV -0
Rose Hill P.O. BOX 1023 [phone]
Perc,iRite" DATE: 09/ 1 22/07 Fl I MAY CA -in.54n Fny (70R)

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1 of 1 Waste Water Systems, Inc,
REV -0
Rose Hill P.O. BOX 1023 [phone]
"PerciRite" DATE: 09/22/07
F1 I MAY (,A. -in.)4n FnY (7np))

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1 of 1 Waste Water Systems, Inc.
REV -0
Rose Hill P,O. BOX 1023 [phone]
"Perc.dR.ite" DATE: 09/ . 22/07 Fl I IJAY (A "�n.1�4n F,, (7nr,)
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1 of 1 Waste Water Systems, Inc.
REV -0
Rose Hill P,O. BOX 1023 [phone]
"Perc.dR.ite" DATE: 09/ . 22/07 Fl I IJAY (A "�n.1�4n F,, (7nr,)

I
I
bedrock. The top surface of layer one was set to actual field survey elevations and given a
layer thickness of 5'. Layer two for each model was given a uniform thickness of 100' based
on the depth of the deepest boring measured from the bottom of Layer 1. Layer 3 was given
a uniform thickness of 100' measured from the bottom of layer 2.
5.5.2.2 Time Parameters
The groundwater model was analyzed as a steady-state model. A model run time of 365
days was used as the time period of simulation. Loading rates were calculated at a yearly
rate to successfully calculate the annual loading rate for the groundwater model.
5.5.2.3 Hkdrogeologic Parameters
Monthly precipitation data was averaged over a 30 year period to determine a precipitation
6W rate of 48.6 inches/year for the study site. An annual evapotranspiration rate value of 28.2
inches/year was subtracted from the averaged precipitation value for a net precipitation rate.
An industry held practice of utilizing 10 percent of the net precipitation rate was utilized as a
baseline groundwater recharge rate. 2.1 inches/year was applied to the surface layer 1 of the
model to simulate the groundwater recharge that occurs naturally. Additional recharge
values were utilized to calibrate the base model to field conditions. Hydraulic conductivity
values, well head observations, and stream elevation observations were utilized in the
groundwater model to simulate the actual field conditions.
5.5.3 Boundary Conditions
A River boundary condition was utilized to model the effect of the branch that exists along
the eastern side of area F. Each cell had a specified stage level, branch bottom level, and
bottom conductance value assigned to it, taken from field data from the site survey. The
bottom of layer 3 and the outer perimeter cells are considered no -flow boundaries.
5.6 Model Calibration
The base groundwater model was calibrated using actual field measurements of well levels
and hydraulic conductivity. Recharge values were varied to achieve a model that simulated
in-situ field conditions within 0% - 10% Root Mean Square Error. The base numerical
groundwater model of area F was calibrated to 3.815% Root Mean Square Error. The
calibration graph is included in Attachment D.
r -I Brooks Engineeting Associates, PA Hydrogeological Assessment Report
L-1 BEA Project No. 307808 23 The Cliffs at High Carolina

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FIELD VALVE CONNECTIONS
1 of 1
Waste
Water
Systems, Inc.
REV -0
"��rqsRite"
Rose Hill
DATE: 09/22/07
P.O. BOX
1023
[phone]
ELLIJAY,
GA. 30540
Fox (706)

----------
BULLETIN H
Cut -Sheets for Drip System Valving

, W
Diaphragm Actuated Valve
Piston Actuated Valve
1c odel 700/705 diaphragm -actuated and the 800/805
t ted valves are hydraulically -operated, globe valves in either
t e, star) oblique M or angle pattern design. Each valve comprises
two major components- the body -seat assembly and the actuator
314"J"
I he actuator assembly is unitized and is removable from the body as
an integral unit, It consists of both an upper and a lower control -chamber.
Each basic valve can easily be configured, on-site, either as a
single -chamber control valve (Model 705/805), or a double -chamber
control valve (Model 700/800). The shaft sub -assembly, in both single
and double -chambered versions is center -guided, providing an
unobstructed seat area.
The Model 700/800 Basic double -chambered valve operation is
independent of valve differential pressure since the line pressure actually
serves as the actuator differential pressure. This develops maximum
power, ensuring immediate valve response, fhe upper control -chamber
is pressurized to close, and vented to open the valve. The lower control -
chamber is usually vented to the atmosphere, but can also be pressurized
to power the valve open,
The Model 705/805 Basic Valve uses valve differential pressure to power
the actuator open or closed. The lower control -chamber, which serves
AM
T'
Piston Actuated Valve
1c odel 700/705 diaphragm -actuated and the 800/805
t ted valves are hydraulically -operated, globe valves in either
t e, star) oblique M or angle pattern design. Each valve comprises
two major components- the body -seat assembly and the actuator
314"J"
I he actuator assembly is unitized and is removable from the body as
an integral unit, It consists of both an upper and a lower control -chamber.
Each basic valve can easily be configured, on-site, either as a
single -chamber control valve (Model 705/805), or a double -chamber
control valve (Model 700/800). The shaft sub -assembly, in both single
and double -chambered versions is center -guided, providing an
unobstructed seat area.
The Model 700/800 Basic double -chambered valve operation is
independent of valve differential pressure since the line pressure actually
serves as the actuator differential pressure. This develops maximum
power, ensuring immediate valve response, fhe upper control -chamber
is pressurized to close, and vented to open the valve. The lower control -
chamber is usually vented to the atmosphere, but can also be pressurized
to power the valve open,
The Model 705/805 Basic Valve uses valve differential pressure to power
the actuator open or closed. The lower control -chamber, which serves
AM

BERMAD�Watc-pwopks
L 700 Seples
Availab,le Sizes & Patterns '
0 1',12" - 20" 00 - 500 mm)0Y nd Angle
a 24" - 32" (600 - 800 mm) - Globe
r�i�e�tion StandagA
-J�9� �Flarn6—e� ISO 7005-2 (ANSI B-16.42),
re6ded, NPT or BSP 40, 50, 65 & 80 mm
Water Temr-,"Quiturf"
a Up to 800C (11 800F)
�Vorkmg Pressure —
0 ISO PN 16: 16 bar Class 4#150: 250
'�Cl fl 50. �r
SS4
0 ISO PN 25: 25 bar im C;ass #�300:psi
Standard Kiterials
Main valve body and cover
Ductile iron EN 1563 (ASTM A-536)
Main valve internals
Stainless steel and bronze
Lm� Control Trim
Brass components/accessories
117 Forged brass fittings & copper tubing
1 Elastomers
NBR (Buna-N)
Coating
Fusion Bonded Epoxy, RAL 5005 (Blue)
NSF 61 and WRAS approved
or Electrostatic Polyester Powder, RAL 6017 (Green)
17 WRAS approved
I kzdl oplional Material's
Main valve body/internals
7 Carbon steel (ASTM A-216-WCB)
Stainless steel 316 CF8M (316)
Aluminum
Nickel Aluminum Bronze
Titanium
Alloy 20
Duplex
Hastalioy
Marine Bronze
254 SMO
Control Trim
Stainless steel 316
Hastailoy C-276
Elastomers
EPDM
i,.J Viton
7-1
Hydraulic,r..ontroll ValvEs r-
700 & Boo Se ies
Pies
Available Size5 Patterns
;5
0- (140 -115(�)�Omrnl - Y F
It 11/2��.;�20"(4 500mm) Pattern
11/2" -`11 18"(401- 450 mm) - Angle
'a Flangeitf: ISO 7005-1 (ANSI B`16-5)�
Water 1'0i iperahi
Upto�1�11C(1800F)
Working f ressuri
* ISOPN116:16bar a Class #150:250 psi
* ISO PN"25:25 ar a Class #300: 400 psi
* ISO PN!40: 40 'ar a Class #400: 600 psi
,Standard Oateria
* Main �valve b y
Carlion steel �STM A-216-WCB)
Duc ile iron Ef� 1563 (ASTM A-536)
* Valvei cover (piIston cylinder)
Brorize or staikess steel
Main 1�vallve iQrnals
Stai6less steelland bronze
Con�ol Trim
Bra compononts/accessones
Fi ;d brass fi�tings & copper tubing
-j Flq-thmpr.-z I
NBRI (Buna-N)
-, ( a I
Fus! In Bonded!Epoxy, RAL 5005 (Blue)
I
NSF 1 and WqAS approved
or El I ctrostatic Polyester Powder, RAL 6017 (Green)
i
WRA approved
Optiori,aJ aterials
Main Ive bodyfinternals
Staid ss steel 316 CF8M (316)
Aluminum
Nickel *uminum, Bronzee
Alloy 2(
Duplex
Marine Qrom
254 SM6
-j Control TA m
Stainless Ste
Hastalloy C-,
Elastomers�,
EPDM
Viton
: 6,6 1
BERMAD�Watc-pwopks
L 700 Seples
Availab,le Sizes & Patterns '
0 1',12" - 20" 00 - 500 mm)0Y nd Angle
a 24" - 32" (600 - 800 mm) - Globe
r�i�e�tion StandagA
-J�9� �Flarn6—e� ISO 7005-2 (ANSI B-16.42),
re6ded, NPT or BSP 40, 50, 65 & 80 mm
Water Temr-,"Quiturf"
a Up to 800C (11 800F)
�Vorkmg Pressure —
0 ISO PN 16: 16 bar Class 4#150: 250
'�Cl fl 50. �r
SS4
0 ISO PN 25: 25 bar im C;ass #�300:psi
Standard Kiterials
Main valve body and cover
Ductile iron EN 1563 (ASTM A-536)
Main valve internals
Stainless steel and bronze
Lm� Control Trim
Brass components/accessories
117 Forged brass fittings & copper tubing
1 Elastomers
NBR (Buna-N)
Coating
Fusion Bonded Epoxy, RAL 5005 (Blue)
NSF 61 and WRAS approved
or Electrostatic Polyester Powder, RAL 6017 (Green)
17 WRAS approved
I kzdl oplional Material's
Main valve body/internals
7 Carbon steel (ASTM A-216-WCB)
Stainless steel 316 CF8M (316)
Aluminum
Nickel Aluminum Bronze
Titanium
Alloy 20
Duplex
Hastalioy
Marine Bronze
254 SMO
Control Trim
Stainless steel 316
Hastailoy C-276
Elastomers
EPDM
i,.J Viton
7-1
Hydraulic,r..ontroll ValvEs r-
700 & Boo Se ies
Pies
Available Size5 Patterns
;5
0- (140 -115(�)�Omrnl - Y F
It 11/2��.;�20"(4 500mm) Pattern
11/2" -`11 18"(401- 450 mm) - Angle
'a Flangeitf: ISO 7005-1 (ANSI B`16-5)�
Water 1'0i iperahi
Upto�1�11C(1800F)
Working f ressuri
* ISOPN116:16bar a Class #150:250 psi
* ISO PN"25:25 ar a Class #300: 400 psi
* ISO PN!40: 40 'ar a Class #400: 600 psi
,Standard Oateria
* Main �valve b y
Carlion steel �STM A-216-WCB)
Duc ile iron Ef� 1563 (ASTM A-536)
* Valvei cover (piIston cylinder)
Brorize or staikess steel
Main 1�vallve iQrnals
Stai6less steelland bronze
Con�ol Trim
Bra compononts/accessones
Fi ;d brass fi�tings & copper tubing
-j Flq-thmpr.-z I
NBRI (Buna-N)
-, ( a I
Fus! In Bonded!Epoxy, RAL 5005 (Blue)
I
NSF 1 and WqAS approved
or El I ctrostatic Polyester Powder, RAL 6017 (Green)
i
WRA approved
Optiori,aJ aterials
Main Ive bodyfinternals
Staid ss steel 316 CF8M (316)
Aluminum
Nickel *uminum, Bronzee
Alloy 2(
Duplex
Marine Qrom
254 SM6
-j Control TA m
Stainless Ste
Hastalloy C-,
Elastomers�,
EPDM
Viton

BERMAD WatEpwopks Flo
FlIma Chart
fic Control ValvEs
Valvc- Flow CoefficiEnt
Y -Pattern
inr,h
Flat Disc
2"
2.51'
Y -Pattern
411
6'0
U_Plug
10" 1 TO
14*1 16"
18'
_T
Kv
Angle
Flat Disc
L
55
An,.Ile
200
460
815
1,250 1,850
1,990 3,310
Clo�
7669 800 SEMEs
PIN`
inr,h
1.5"
2"
2.51'
30Y
411
6'0
87'
10" 1 TO
14*1 16"
18'
'20"
Kv
42
50
55
115
200
460
815
1,250 1,850
1,990 3,310
3,430
.3,550
CV
49
58
64
133
230
530
940
1,440 2,140
2,300 3,820
3,960
4,100
Kv
36
43
47
98
170
391
693
1,063 1,573
1,692 2,814
2,916
3,018
CV
41
49
54
113
200
450
800
1,230 1,820
1,950 3,250
3,370
3,490;
Kv
46
55
61
127
220
506
897 .1,375
�2,035
2,189 3,641
3
Cv
53
64
70
146
250
580
1,040
1,590 2,350
2,530 4,210
4,360
N��
Kv
39
47
51
108
187
430
762
1,169 1,730
1,861 3,095
3 ' 207
NA
CV
45
54
59
124
220
500
880
1,350 2,000
2,150 3,580
3,710
_��
inch 24" 28" 30" 32"
G -Pattern Kv 7,350 7,500 7,500 7,500
Fla'Disc
Cv 8,490 8,670 8,670 18,670
F-Gf
Valve fiow coefficient, Kv or Cv Kv(Cv)=Q � �-p
Where:
Kv = Valve flow coefficient (flow in m3/h at 1 bar Diff � Press.)
Cv = Valve flow coefficient (flow in gpm at Diff . Press. 1 psi)
Q = Flow rate (m -'11h ; gpm)
AP Differential pressure (bar; psi)
Gf Liquid specific gravity (Water = 1.0)
Ail
11 01-1

610
300 Sales
MML:80DY HYDRAULIC I ELECTRI
CONTROL VALVES I
6
Dimensions and Weights
Model 300
Hydraulic Control Valve
Model 300 is a hydraulically operated
control valve, requiring a pressure
command to close.
Model 310
Electric Control Valve
Model 310 has a 3 -way solenoid pilot
valve with manual override.
Standard: N.C, (normally closed), requiring
electrical energy to open.
Option: N.O.
Model 320
Pressure Reducing Control Valve
Model 320 reduces high upstream
pressure to lower set downstream
pressure.
TECHNICAL DATA
Specifications
. Valve Configuration.,
Y -pattern and angle
. Sizes:
Y — Y -pattern: 11/2", 2" & 3"
A —Angle: 2"
. End Connections:
- 11/2" & 2": threaded NPT, BSP
— 3": female threaded NPT/BS or
flanged to ANSi/ISO/BS-D
FIRM
. Operating Pressure Range:
10-150 psi (0.7-10 bar)
U4
- Temperature Range:
Water up to 1 80'F (80'C)
Materials:
Body: (11/2" & 2") Brass,
(3") Polyester -coated Cast Iron
Actuator: Plastic, Brass and
Stainless Steel
Diaphragm: Nylon-tabric,
Reinforced Natural Rubber
Seals: BNR and NR
Flow Chart
6
Dimensions and Weights
Model 300
Hydraulic Control Valve
Model 300 is a hydraulically operated
control valve, requiring a pressure
command to close.
Model 310
Electric Control Valve
Model 310 has a 3 -way solenoid pilot
valve with manual override.
Standard: N.C, (normally closed), requiring
electrical energy to open.
Option: N.O.
Model 320
Pressure Reducing Control Valve
Model 320 reduces high upstream
pressure to lower set downstream
pressure.

I
4
LMMIL NMIIMEI�MEI
3/4" LOW41OW PRESSURE REGUUtOR
OUTLET PRESSURE VS. INLET PRESSURE AT 1.3 GPM
50
40
30
20
10
0
28 56 84 1,12 140
Inlet Pressui e (psi)
Product Advantages
• Instant response to variations in pressure assures that outlet pressure will remain constant
regardless of inlet pressure.
• Pressure Regulators are preset with flows from 3.5 to 175 GPM.
• Manufactured from non -corrosive, high quality plastic and brass, to withstand all fertilizers
and chemicals in common use.
• Regulating unit has a stainless steel spring and screw.
• The EDPM rubber diaphragm creates a fight seal eliminating leakage.
• The rise versus the decline in outlet pressure has significantly decreased ensuring better
hydraulic perfomance,
• Sealed regulating unit is field replaceable and easy to maintain.
• Built-in operating indicator visually shows when proper outlet pressure is achieved.
• New regulating units are compatible with existing Pressure Regulator bodies.
3/4" Low Fkvw
Pressure FteWlator
• Improved in-line unit,
• Female threaded 3/4" X 3/4" connections.
• One-piece seoled unit regulates oc(urately
at low flows.
• Silicon diaphragm and stainless steel
spring — no leakage.
3/40 � Low ROW 3/40
_6,
Applicatims ;
For use in drip and sprinkler irrigation
systems.
specmcaflon$
* Available in the following pre-set pressures:
9Y 12, 15, 20, 25, 30, 35, 43, 50, 57 and 65 psi
* 3/4" Low Flow available in: 15, 20, 25,
35 and 43 psi
* Maximum operating pressure: 145 psi

Pressure Reguli Technical Infonnation
. .... ..................... . .
REGULATED PRESSURE vs FLOW RATE
HEAD LOSS vs FLOW RATE
60 12
'4 10
"j,
Z
50
6
45
40 2
35 0 20 40 60 80 100
30 Flow Rve (CAX)
AMPLE: HE -AD I I OSS vs FLOW RATE (3xJ0) 12)
25 I.xGiven Flow Rate 63 GPM, Nominal
required pressure 20 psi� 10
20 Using Pressure Regulator Model 2" x 6
8
MAI
(6 regulafing units) will result in I O� 5 GPM
per iegulaling unit. 6
15 10, 5 GPM per iegulafing unit will result in an
output pressure of 18 psi. (See Regulated 4
10 Pressure vs. Flow Rate graph).
Head loss of Pressure Regulator 2" x 6 at 2
63 GPM is 5 psi. (See Head Loss vs, flow
rm�
5 Rate graph).
Design pressure of inlet of Pressure Regulator 90 105 120 135 150 16 5 175
should be 18 + 5 23 psL Flow Rate (GAVI)
3.5 8 12
16 175
Flow Rate (per regakting unit)
100
PARTNUMBERS,
40 0 W'101-1-� omw
"11,00 W-11 "I' W"W"
�r 10 W
"WWi
V., Ww"W","
91%1-w A,00 , WN, NIPM."
071 WTI W-1 SM! -!,I NO ON W",
INP -1,11, MAW"I'', W1,11, "O"'Nom
�
OVIF 90"WI 0�0: IS
I W
"t7
-I
ISM W.- "W"
_V171'"', W'' MO �WV'011 100-00"W"e"'! IS(- "Y"O , W'',

The Dorot Quick Reacting Relief (QR) Valve is a direct -sealing diaphragm valve activated by line pressure
and controlled by an adjustable pilot, When the network pressure exceeds the pressure setting of the pilot,
the valve fully opens instantly. When the network pressure decreases below the set point, the valve closes
slowly.
Standalrd Featupe$ (see diagram)
A, Self -Cleaning Filter
B, Needle Valve
C. Ball Valves
D. Quick Response Pilot (66-300)
E. Quick Response Relay 2" (for 6' and larger valves)
The 2' QR valve (bronze) is available in a globe or angle pattern. A
pilot (68-200) with a built-in needle valve ensures slow closure.
The QR valve is installed on a tee -junction in a pipeline and releases
excess pressure to protect the pipe network from dangerous surges.
The slow closing of the valve, adjustable with a needle valve,
prevents secondary surges,
n i P irl tanne
U" U"a UPFU
The QR valve is not a modulating valve and should not be used to maintain a certain pressure in
the network, A pressure sustaining/relief valve should be used.
0 A quick reacting pressure relief valve cannot prevent water -hammer caused by power failure, A
surge anticipating valve should be used.
0 The use of an isolation valve is recommended at the upstream side of the QR valve.
0 A discharge pipe attached to the downstream side of the valve
must be sized for the maximum flow and not restrict the flow,
0 QR valves operate in case of emergency, usually for a short
time, The valve should be sized to accommodate 50%-80%
of the system's nominal flow rate.
Recommended Maximum Flow Rates (GPM)
Flow 450 1,100 1,700 4,000 7,000 10,000 15,000 28,000
pilots
*The green spring is standard
for the 68-200 and the red
-300
spring is standard for the 66
pilot,
68-200 66-300
For detailed information, material specifications and
dimensions, see the Dorot Basic Valve brochure.
C
_,,NETAF1M.___.,
(_!A,Quahty Works
(" 11
NETAFIM IRRIGATION, INC.
WEST COAST: 3025 E. Hani,,top- - Fro M_ CA 93721
(209) 49"680 - FAX t2O9) 442-3119
EAST COAST: 548 N. Dougln AVC. - Allamonte Spfings, FL 32714
[phone] - FAX [phone]
Pilot Specs
68-200
66-300
Staring
Yellow
B-30 PSI
8-30 PSI
Green
14-140 PSI
14-100 PSI
Red *
115-360 PSI
30-190 PSI
Black
N/A
100-360
Dimensions
Pori Size
Height
6 V�­
9"
Width
1 2"
3 112"
Max. Press.
350 PSI
350 PSI
Materiols
Body/b t
Bross
Br.a.,,,
, ,,,onne
PI,
St � Steel
SJ.S
Diaphragm
Not. Rubber
Not, Rubber
0 -rings
Nitrile
Nitrile
_,,NETAF1M.___.,
(_!A,Quahty Works
(" 11
NETAFIM IRRIGATION, INC.
WEST COAST: 3025 E. Hani,,top- - Fro M_ CA 93721
(209) 49"680 - FAX t2O9) 442-3119
EAST COAST: 548 N. Dougln AVC. - Allamonte Spfings, FL 32714
[phone] - FAX [phone]

BULLETIN I
Cut -Sheets for Flow Meter

f,* i A
T()TAIJ,-fFR
(VISIC"RIF I ON
MOVEL MIAO FIAW,EP TlJef MEYFP�,S iriaiftll'�AiALIFtM tO 'lle tli�MES!
IP w4odty
I ol, f 0
M-"Ioi AVM,'Ar3h,0",fJ Thp ikm�pd end W4r' d��siP
rrf��foll�' lisf, in wid�� 0 veAfi jjp �rj 3',Y) psi working
'md'� ""rp "Kil" it;, AowWA zhls� 'P fah3od fact� steol
W" tut*� hav�� straviterwqg, vane5, end aot
�swrf C-Poxy resin.
INSTALLATQN i,,, mVj'!-� V� c ' hurt 101,Ctfi'l Y iiRrIgoo vid, pipt; k,", tha
�"r indmed F'o su�ficll or
Fufl�' C'- OF"A "a Irml—
t�i o1wi! Plat 1wid tc, &Ot tip
ol' tp—pl
rx� Oa�'H�Aens qslmam and
'in"e c'�Jp� fmw� thq lma'er
PROPELLEP, wilh ljw vive,inod alw�'m 1hrough tile
om M '��'Jl qsafbox 1!0,,� walir ontering thfe�
a, wpl! a,, PKi, ne',A hv any paAwtq glaod The, propaller
voqk"'al ��Hapf.w'l 1"',
mok"u", ot
Nch, fkxv
SEAWNG 41 �FtQf �pii-4e sy�,Ap_rn
lhousl Oaalings,
� d rec jo is
"�n "la f 'o� a, I S f',af, oi- �hn�i �z in totb an o r e��, o r ;� , t t r., .
-�fvnaiwm-""l -,"i) rfr"E Proo-Illei
N� vJuiu J-� uwwi mm�';hpntsm a* she' d
! mji�
Aol q lh�� !lf47 'm lhe
ie"7 h
mt�l a S�'� fitt
I lit, Straigm
-lig
x �4�jlar.;�jT
",-41 ho a! all W
S f�:'
'—i 6va Units f�:
j 01 pi d1k)"J, �Wiij"
O�PING ",EAI -S ?'4 wlm�"�
u 15�)y (A RIG
tv 11, 1 quid" Inemw-atl b", the
V W A, vo - P� t� t'
MODEL fAL-08
- :zA�
R� f
300 psi FLA f,,J' E Cl F -JI -3E MIE'HE
SEALED M�ETER MECHANIISJA (AIA N F, I C U V2,'V F
I r j_' F�
NDICA-1 OR - i R
�l 11 j" Ij 'W'�' -
'A,
A,'
T
OPTIONAL ECAMMIENT
A
"�Jl.�1�6':4y'W' 'k

MODEL ML -08
300 psi FLANGED TUBE METER
SEALED METER MECHANISM -- MAGNETIC DRIVE
INDICATOR -TOTALIZER
SIZES 3" thru 48
E - Bolt Circle
F - Number of Bolts
G - Size of Bolts
METER
& PIPE
SIZE
FLOW RANGES,GPM
*LOWVELOCITY STANDARD HIGHVIELOCITY
CONSTRUCTION CONSTRUCTION CONSTRUCTION
MIN. - MAX. MIN. - MAX. - INT. MIN. - MAX.
DIMENSIONS
SHIPPING
WEIGHT
POUNDS
A
B1
B2
C
D
I E
F
G
H
K
�3
40-250
45-250-350
N/A
18
81/4
5
11/8
7
65/8
8
3/4
53116
9
85
4
50-500
55-500-700
200-700
18
10
63/16
11/8
7
77/8
8
314
53/16
9
122
6
90-1200
120-1200-1500
300-1500
22
121/21
81/2
13/8
1 9
105/8
12
3/4
61/4
9
167
8
100-1500
150-1500-2000
400-2500
24
15
10518
19/16
9
13
12
7/8
71/4
9
237
10
125-2000
180-2000-3000
500-3500
26
171/2
123/4
15/8
10
15v4
16
1
81/2
11
310
12
150-2800
200-3000-3500
800-5000
28
1 201/2
15
1 113/16
10
1 17314
1 16
11/8
91/2
1 11
400
14
250-3750
300-4000-4500
1000-6000
42
23
161/4
115/16
12
201/4
20
11/8
1101/2
131/2
600
16
350-4750
400-5000-6000
1200-7500
48
251/2
181/2
21/16
12
221/2
20
11/4
111/2
131/2
800
18
450-5625
700-6000-7500
1500-9000
54
28
21
23!16
15
243/4
24
1114
12112
13112
1080
20
550-6875
850-8000-9000
2000-12000
60
30112
23
27/16
15
27
24
11/4
131,,2
1131/2
1260
24
800-10000
1000-10000-13500
3000-15000
72
36
27114
211/16
18
32
24
1 v2
173/4
23
2040
30
1200-15000
1800-15000-21000
4000-25000
84
43
35
215/16
18
1391/4128
13/4
203f4
23
3220
36
1500-20000
2000-20000-30000
5000-35000
96
50
42
33/16
201
46
132
2
233/4
23
4550
42
2000-28000
3000-30000-40000
6000-50000
108
57
507/ir
q711 9
28
36
5900
48
2500-35000
5500-35000-5000n
7onn-snc
Standard construction will be supplied for all main line meters unless special flow range, materials, or construction are
required.
Low velocity (LV) construction has the same low and maximum flow rates as AWWA C704. For lower f lows refer to Model
TM -01 turbine meters.
Y
rD­ P ""'I V (L
i 4, 04, 3
A 1-1,
HU)Nr
14 n fl- 1"t �q f
FA'x' YQ
" 1� ... .. ...
N TEE,

LaLj
BULLETIN J
Cut -Sheets for Disc Filtration System
Q,,-

La�
'k MEMMM mmmm-
Fully Automatic Disc Filters
For 50-800 GPM Flow Ranges
2
I. o
o.4
0.2
2ff & 3" DISC-KLEEN FILTERS
Headloss
4o 100 200 400 1000 2000
Flow PAte (GPM)
Procluct Advantnes
• Quick Installation — factory assembled and tested, arriving on a pallet ready for hook-up
and immediate operation.
• Less Maintenance — molded spine, chemically resistant and performs reliable backflush.
Monual cleaning is practically eliminated.
• Filtration Grade Versatility — filtration discs can he changed quickly and easily from
40 mesh up to 200 mesh.
• Optimizes Irrigation — less backflush time means more uniform application of water in the
field.
• System Flexibility — each Disc-Kleen Battery is capable of handling a wide operational flow
range.
• Lasts Longer — manufactured from engineered synthetics to resist rust and corrosion from
chemicals and weather.
• Standard with installed polypropylene drain manifold.
Filtration Process
As dirty water travels through a
Disc-Kleen Filter, debriis is captured
along the walls and in the grooves of
the channels in the filter element
During the backflush cycle, the valve
changes position, the pressure in the
outlet manifold loosens the discs
automatically. A specially designed
nozzle system inside the filter stack
then sprays pressurized water against
the loosened discs, spinning them
clean quickly and efficiently. After
backflushing, the stack of discs
automatically compress to resume
filtrdon.
3" Disc-l(leen
Filter Battery
I . . =
For surface water containing algae and
other organic materials such as reservoirs,
canals, rivers and waste water applications.
For well water containing light sand
(,3 ppm) and other contaminants.
Specifications
Includes installed drain manifold
Inlet and outlet connections: Grooved
Backflush valve flush port: 2" NIPT
Maximum operating pressure: 140 psi
Minimum backflush pressure required:
40 psi downstream of filter during backflush
Minimum backflush flow per spine: 35 GPM
Minimum PH: 5
Mesh sizes and color: 40 - Blue
80 - Yellow
120 - Red
140 - Black
200 - Green
Materials
Manifold: Polypropylene
Filter Body: Glass Reinforced
Polyamide
Spine: Polypropylene
O-Riings and Seals: EPDM
itNEYARM"',
S'
NETARM USA
5470 E. Home Ave. a Fresno, CA 93727
888.638.2346 * 559.453.6800
FAX[phone]
www.netafimusa,com
MONA
ii�
ii�am
Subsfitute XXX for proper mesh siae. GR
= Grooved.
3" Disc-l(leen
Filter Battery
I . . =
For surface water containing algae and
other organic materials such as reservoirs,
canals, rivers and waste water applications.
For well water containing light sand
(,3 ppm) and other contaminants.
Specifications
Includes installed drain manifold
Inlet and outlet connections: Grooved
Backflush valve flush port: 2" NIPT
Maximum operating pressure: 140 psi
Minimum backflush pressure required:
40 psi downstream of filter during backflush
Minimum backflush flow per spine: 35 GPM
Minimum PH: 5
Mesh sizes and color: 40 - Blue
80 - Yellow
120 - Red
140 - Black
200 - Green
Materials
Manifold: Polypropylene
Filter Body: Glass Reinforced
Polyamide
Spine: Polypropylene
O-Riings and Seals: EPDM
itNEYARM"',
S'
NETARM USA
5470 E. Home Ave. a Fresno, CA 93727
888.638.2346 * 559.453.6800
FAX[phone]
www.netafimusa,com

I
211 & 311 Disc-lGeen Filter Batteries Technical Infonination
ftaii� AL M 41,04 AL
IMPORTANT NOTE: We have categoflzed water quality as a guideline for filtration requirements. Be aware all water quality categories shown above are general. Your water quality may vary. If your water
contains more thon two parts per million of sand, a sand separator is recommended. If in doubt, consult an authorized Netaft USA dealer.

BULLETIN K
Cut -Sheet for Rainbird Rain Gauge

Amok
Ammk
AN-=
PAIA V -, RIRDc,
@ TECH SPECS
Rainfall and Wind Speed Sensors
Rain Bird Rainfall Gauge
The Rain Bird Rainfall Gauge customizes the
weather data gathering features of
Maxicom2 by providing site-specific rainfall
measurements. The central controller
retrieves this information daily, adjusting
station rundmes using the site-specific
weather data. The Rainfall Gauge may be
used to automatically interrupt MaxiCOM2
during an irrigation cycle if it starts to rain,
If enough rainfall occurs, further irrigation
will be cancelled. If only a small amount of
rainfall occurs, irrigation will resume,
adjusting runtimes for the amount of
rainfall that occurred.
Features
Identifies localized rainfall and adjusts
system operation accordingly
Watering cycle can be interrupted or
cancelled when rainfall commences
Provides site specific rainfall
measurements in increments of 0.0 1,,
(.025 cm)
Heavy-duty construction, with a gold
anodized aluminum collector funnel and
white baked enamel coated aluminum
sensor housing
Filter screen for capturing debris
Integrates into the Maxicom2 system
using the Rain Bird pulse decoder for
two-vdre CCU systems, or directly to the
sensor input on ESP -Site and MAMLink
satellite controllers
Specifications
• Resolution: 0.01" (.025 cm)
• Accuracy 1.0% at 1" (2.5 cm) /hour or less
• Average switch closure time: 135 ins
Maximum bounce settling time: .75 ms
Maximum switch rating: 30 VDC @ 2 A,
115 VAC @ IA
Temperature limits: +32'F to +125'F
(0' C to +521 Q
Humidity limits: o — I 00%
Height: 4.5 " (11,4 cm)
Weight: 1.5 pounds (0,68 Kg)
Receiving orifice diameter: 3.80" (9,7 cm)
Cable: 60 feet (18 meters)
Model
, RAINGAUGE
Rain Bird Anemometer
(Wind Speed Meter)
The Rain Bird Anemometer provides
additional custornization to the MaxicoM2
Central Control system by providing site-
specific windfall measurements. Local wind
speed is captured by the Wind Speed Meter
and input to the Cluster Control Unit (CCU).
The CCU can interrupt irrigation when wind
velocity reaches a programmed set point.
Interrupting a watering cycle during windy
conditions saves water, avoids property
damage, and improves sprinkler distribution
uniformity.
Features
• Precision three -cup anemometer for
measuring wind velocity
• Balanced rotor and low friction bearings
detect wind speeds from 4 MPH to
8OMPH (6,5 to 128 km/h)
• Electronics supplied with a weather tight
enclosure exceeding NEMA 4 and 6
specifications
• Mounting bracket and 20 feet (6 meters)
of cable
• Identifies localized wind speed and
adjusts system operation accordingly
• Watering cycle can be interrupted during
windy conditions
• Integrates into the MaxiCOM2 SySteM
using the Rain Bird pulse decoder for
two -wire CCU systems, or directly to the
sensor input on ESP -Site and MAXILink
satellite controllers
Specifications
Power supply. 5 to 24 VDC
Current draw. 3 to 7 mA
Output signal: K = 1.6965, offset of +0.059
Cable: 20 feet (6 meters)
Weight: 1.3 Lbs (0,6 Kg)
Dimensions: 22"L x 8"Wx 8"H (56 cmL x
20cmW x 20cmH)
Model
0 ANEMOMETER (Wind Speed Meter)
Rainfall Gauge
Anemometer
RAINGAUG
AMEMOME

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

BULLETIN L
Drip Line Cut Sheets

NEWIMUSA
Product Advantages
• Wide pressure range U to 60 psi) produce uniform dripper flow rates - longer runs and steep
topographies are irrigated with high uniformity.
• Mechanical barrier pieven�s root infirusion - ideal for sub -surface irrigation (SDI).
• lowest coefficient of manufacturing variability (Cv) in the industry.
• Seamless, one-piece construction prevents damage to drippers during installation and retrieval.
• Design flexibility and performuncewith various dripper flows and spacings allow for specific
application rates and coritiolling of wetting pattern in differentsoil types.
• Pressure compensating feature delivers precise water applications anywhere in the field.
/5
Applications
• For sub -surface or surface applications.
• For tree, vine, row crops, geenhouse and
nursery.
• Multi-scasonal use.
• For undulating fields.
Specifications
Nominal flow rates (GPH): .32, .42, .53,
.62_92
Common spacings: 24", 30", 36", 42.25", 48"
Recommended filtration: 120 mesh
Inside diameter: .540 - 16mm (45 rnil)
.570 � 1.7mm (45 mil)
.620 - 18mm, (45 mil)
,690 - 20rrm-i (48 mil)
.820 - (35, 45 mil)
VineLlne
Vineyard Solutions
Pire-Installed Adjustable Nipperline Ring
See back for detak
The Most Successful Pressure Compensating
Dripper in the History of Irrigation
C-4
Industry's Widest Flow Path Self -Adjusting
Wider cross-section allows large Diaphragm
particles through short flow path. diusts
Continuously a
A to varing water
-M
pressures - crushing,
minimizin g and
�,_,Ial`,,�� N flushing debris.
Large Filter Inlets,
Secondary Filtration
Reduces clogging and Pressure
maimains the essential (ompensatin
lilt
80 th and Out
supply of water to the Delivers precise water
dripper for constant
delivery of water f1mv. appkations anywhere
in the fiek
Increased Flow Path Velocity
Commonly used turbulent chippers have overlapping tooth patterns,
easily ocitc4iing debris.
Turbonet Technology improves dripper performance by widening
the tooth pattern, maximizing flow path velocity, allowing
contaminants to pass easily through the dripper, virtually eliminating
plugging.
Product Advantages
• Wide pressure range U to 60 psi) produce uniform dripper flow rates - longer runs and steep
topographies are irrigated with high uniformity.
• Mechanical barrier pieven�s root infirusion - ideal for sub -surface irrigation (SDI).
• lowest coefficient of manufacturing variability (Cv) in the industry.
• Seamless, one-piece construction prevents damage to drippers during installation and retrieval.
• Design flexibility and performuncewith various dripper flows and spacings allow for specific
application rates and coritiolling of wetting pattern in differentsoil types.
• Pressure compensating feature delivers precise water applications anywhere in the field.
/5
Applications
• For sub -surface or surface applications.
• For tree, vine, row crops, geenhouse and
nursery.
• Multi-scasonal use.
• For undulating fields.
Specifications
Nominal flow rates (GPH): .32, .42, .53,
.62_92
Common spacings: 24", 30", 36", 42.25", 48"
Recommended filtration: 120 mesh
Inside diameter: .540 - 16mm (45 rnil)
.570 � 1.7mm (45 mil)
.620 - 18mm, (45 mil)
,690 - 20rrm-i (48 mil)
.820 - (35, 45 mil)
VineLlne
Vineyard Solutions
Pire-Installed Adjustable Nipperline Ring
See back for detak

Lateral Length
I I I I A I
RM 540 -�
0.42 GPH
Flows (6PH):
-32_42-53-62-92
1 �Iw 4 i
Wall thickness (mil): 45
..... . ........ .. . ....... . . ...
I 2r'
Flows (GPH):
.32, A2_53-62-92
Wall thickness (mil): 45
RAM 690
Flows (GPH):
.32, A2, �53_62_92
Wall thickness (inil): 48
WO
F
Law!
RAM 820
flows (GPH):
RAM 570
Flows (6PH):
-32_42-53-62-92
1 �Iw 4 i
Wall thickness (mil): 45
..... . ........ .. . ....... . . ...
RAM 620
Flows (GPH):
.32, A2_53-62-92
Wall thickness (mil): 45
RAM 690
Flows (GPH):
.32, A2, �53_62_92
Wall thickness (inil): 48
WO
F
Law!
RAM 820
flows (GPH):
-32� .42_53-62, .92
Wall thickness (mill: 45

110
.8
s .6
.4
,2
RAM Flow Rate vs. Pressure '
to, 20 30 40 50 60
Pressuri'psi)
Drii;per L�iglth Pep4h Width
PACKAGING DATA
1=
C1
-470
4
3,
A20 1
-4
Ih
20 coils pet pullet.
VineLlne Vineyard Solutions
Pro -installed Adjustable Dripperline Ring
• Easily adjustable — moves from one end of the dapperline to the other preventing water migration
• Economical — saves labor costs
• Flexible options — available with Rom or Tirilon Heavywall Dripperlines
• Available for 540, 620, and 690 siizes.
• Pre-installed at Netalhim USA
Netofifm USA — Delivering Total Growing Solutions
#Dripperlines oFilters -Valves oAirVenfs -Sprinklers -Autornation *FlowMeters
For Agriculture, Greenhouse & Nursery and Landseape
Too" 0 f`
lagak-Z&L
FIT'. k7F1T1T1;rM.- I* - . L_
Cornpensating Operation . .......... . ... - ...........
Ram's self-cleaning pressure compensating
dripper is a fully self-contained unit welded
to the interior wall of the dripper tubing.
Both tubing and dripper are manufactured.
from high quality synthetic elastorners to
withstand chemicafs and fertflizers. The Rain
dripper contains a diaphragm that
continuously adjusts to varying water
pressure to ensure a constant flow rate, The
diaphragm allows particles to pass through
the dripper, promoting reliable performance
and a longersystern. life.
This continuous flushing feature and wide
flow path keep drippers flowing at optimal
rates without clogging or interrupting
operation.
Particles that may
accumulate at the
dripper outlet cart
cause a reduction of
flow.
Pressure a.-ov.-
PRECISION IRRIGATION"
For more information call your Authorized
Netafim USA Dealer or call Nelahm USA
Customer Service at [phone],
A007 8,/02

BULLETIN M
Pole Blower Curve and Cut -Sheet

4W
Description
Dayton PSC and Shaded Pole blowers provide economical air delivery for general
heating, cooling, ventilating, or component cooling. Typical applications include
cooling greenhouses, blowers for wood and corn stoves, ventilating small buildings,
cooling electrical enclosures and removing heat from machinery. The blowers
are exact replacements for many OEM blowers with the same physical footprint.
Forward curve wheels driven by Dayton motors are rated for continuous duty
with all -position mount. These units incorporate balanced ball or sleeve -bearing
motors with cast aluminum end shields. This provides greater heat dissipation
and protection, reducing down time due to component failure and accidental
damage. Direct drive blower wheels are dynamically balanced to reduce noise
and vibration and to maintain CFM at higher static pressures.
Specifications
1TDT9* 794 780 750 690 670
Replaces 4C668
NOTE: Includes Conduit Box with 81' Lead Length.
NOTE: Not suitable for use with speed -controlled devices.
Dimensions
in. (mm)
13.109
(332,98)
/07j.0 13 1
;0 7 8. 0 0)
0
-7-
Li r*�
Ln Ln
I I
610 570 —
(261.00)
115/230 2.75 @1 15V 60
1.45 @230V
Features
• PSC motor
• Baked enamel Gray finish
• Heavy gauge steel housing
• All position Mounting
• Maximum Ambient Temperature
1040F
Suitable for 50Hz operation
Additional Benefits
9 Permanently Lubricated Ball -Bearings
. Extruded Aluminum Blower Frame
for Increased Rigidity
9 Auto -Thermal Protection
Inv
Motor Component Recognition C US E47479

=w
6,A

I
MM
Cummins Power Generation commercial generator sets
are fully integrated power generation systems providing
optimum performance, reliability and versatility for
stationary and prime power applications.
MMM�
Cummine heavy-duty engine - Rugged 4 -cycle,
industrial diesel delivers reliable power, low emissions
and fast response to load changes.
Alternator - Several alternator sizes offer selectable
motor starting capability %vith low reactance 2/3 pitch
windings, low waveform distortion With non-linear loads
and fault clearing short-circuit capability.
Contmil system - The PowerCommando 1.1 electronic
control is standard equipment and provides total genset
system integration including automatic remote
starting/stopping, precise frequency and voltage
regulation, alarm and status message display, output
metering, auto -shutdown at fault detection and NFPA
110 Level 1 complianm The opirional PowerCommand
2.2 control is UL 508 Uisted and provides AmpSentry",
protection.
Cooling system - Standard integral set -mounted
radiator system, designed and tested for rated ambient
temperatures, simplifies facility design requirements for
rejected heat.
Enclosures - Optional weather protective and sound
attenuated enclosures are available.
NFPA - The genset accepts full rated load in a single
step in accordance with NFPA 110 for Level 1 systems.
Wamanty and service - Backed by a comprehensive
warranty and worldwide distributor network.
D2008 I Cumm4is Power Generation Inc. I All rights reserved I specifications subject to change without notice I Cummins Power Generation
and Cummins are negisterad tradernaft of Cummins In. Power0ornmand, InPower and 'Our energy working for you,' are trademarks of
Cummins Power Generation, Other company, product or service names may be trademarks or service marks of others,
,-J
This generator set is designed in facifffies
certified to IS09001 and manufactured in
facilibes certified to IS09001 or IS09002.
The Prototype Test Support (PTS) progr
,, , am
verifies the performance integrity of the
generator set design. Cummins Power
Generation products bearling the PTS symbol
meet the prototype test requirements of NFPA
110 for Level 1 systems.
All low voltage models are CSA cerfified to
product class 4216-01.
The generator set is available Listed to
UL2200, Stationary Engine Generator
Assemblies.
U.S. EPA
Engine certified to U.S. EPA Nonroad Source
Emissions Standards, 40 CFR 89, Tier 3.
MMM�
Cummine heavy-duty engine - Rugged 4 -cycle,
industrial diesel delivers reliable power, low emissions
and fast response to load changes.
Alternator - Several alternator sizes offer selectable
motor starting capability %vith low reactance 2/3 pitch
windings, low waveform distortion With non-linear loads
and fault clearing short-circuit capability.
Contmil system - The PowerCommando 1.1 electronic
control is standard equipment and provides total genset
system integration including automatic remote
starting/stopping, precise frequency and voltage
regulation, alarm and status message display, output
metering, auto -shutdown at fault detection and NFPA
110 Level 1 complianm The opirional PowerCommand
2.2 control is UL 508 Uisted and provides AmpSentry",
protection.
Cooling system - Standard integral set -mounted
radiator system, designed and tested for rated ambient
temperatures, simplifies facility design requirements for
rejected heat.
Enclosures - Optional weather protective and sound
attenuated enclosures are available.
NFPA - The genset accepts full rated load in a single
step in accordance with NFPA 110 for Level 1 systems.
Wamanty and service - Backed by a comprehensive
warranty and worldwide distributor network.
D2008 I Cumm4is Power Generation Inc. I All rights reserved I specifications subject to change without notice I Cummins Power Generation
and Cummins are negisterad tradernaft of Cummins In. Power0ornmand, InPower and 'Our energy working for you,' are trademarks of
Cummins Power Generation, Other company, product or service names may be trademarks or service marks of others,
,-J

Generator set specifications
Engine specifications
Alternator specifications
Available voltages
60 Hz Three phase line-neutmililine-line
410 Hz Single phase fino-neutralfilifte-line
6110/190 *115/23ODelta
*1271220 *240/416
-110/220 1151230
1201240
*110/220 -1201208
e139/240 o255/440
*115/2-00 120/240 Delta
-220/380 o277/480
* 23CV400 &347/600
Note. Consult factory for other volitages.
Generator set options and accessoeies
Engine
Alterwator
Exhaust system
IN
PowerCommand Network
* 120V, 150WIubeoil heater
13 105 IC rise alternator
El Heavy duty exhaust elbow
Communications Module
* 120/240 V, 1500 W coolant
ill 125 �C rise alternator
El Slip on exhaust connection
(NOM)
heater
0 120 V, 100 W anti -condensation
0enerator set
0
Remote annunciator panel
Fuel System
heater
11 PMG excitation
fill Battery
0
EJ
Spring isolators
UL 2200 Usted
6 24 hour dual wall sub -base
0 Single phase
N Battery charger
0
2 year prime power warranty
tank
IN Enclosure.- aluminum, steel,
0
2 year standby power
weather protective or sound
warranty
attenuated
11
5 year basic power warranty
IN Main line circuit breaker
Notw. Some options may not be available on all models - consult factory for availability,
E �j 1,"7,j7=, ,
T,t W,
e2M I Cumn�na Power Generation Inc, I All righu. resemad I Specifications subject to change without notice I Cummins Power Generation Power
ard Cummins an regivered Vacrernaft of cummlins Inc, PoweTCornmand. InPower and *Our "rgy worldng for you.'are ItademeAs of Generation
Gummins Power Gener0m. other company, produot or service nurnes may be trademaft Or service fraft of others.
S-15441' (4/08) ce

bz
Control system
Operator panel features
PowerCommand control - An integrated generator set
control system providing voltage regulation, engine
protection, generator protection, operator interface and
isochronous governing (optional).
ConUot - Provides battery monitoring and testing
features and smart -starting control system.
InPower"m - PC-based service toot availaWe for detailed
diagnostics.
PCCNet RS485 - Network interface (standard) to
devices such as remote annunciator for NFPA 110
applications.
Control boards - Potted for environmental protection.
High ambient operation - Suitable for operation in
ambient temperatures from -40 OC to +70 OC and
attitudes to 13,000 feet (5000 meters).
Prototype tested - UL, GSA and CE compliant.
Standard control functions
Engine data
• DC voltage
• Lube oil pressure
• Coolant temperature
Other data
• Genset model data
• Start attempts, starts, running hours
• Fault history
• R6485 Modbue interface
• Data logging and fault simulation (requires InPower
service t000
Digital governing (optional)
Integrated digital electronic isochronous governor
Temperature dynamic governing
Digital voltage regulation
* Integrated digital electronic voltage regulator
* 2 -phase line -to -line sensing
a Configurable torque matching
Control functions
• Time delay start and cooldown
• Glow plug control (some models)
• Cycle cranking
- PCCNet interface
a (2) Configurable inputs
- (2) Gonfigurable outputs
- Remote emergency stop
Options
o Auxiliary output relays (2)
11 120/240 V, 100 W anti -condensation heater
ii Remote annunciator with (3) configurable inputs and (4)
oonfigurable outputs
a PMG alternator excitation
n PowerCornmand for Windows! remote monitoring
software (direct connect)
Ei Auxiliary, configurable signal inputs (8) and
configurable relay outputs (8)
u AC output analogue meters
EJ PowerCommand 2,2 control with AmpSantry
protection
Standard PowerCommand
1.1 control opemtor/dIsplay
panel
u2008 I Cummins Power Generation Inc. I At right,. reserved I Specifications subject to change without noitivs I Cummins Power Goneration
and Cummins ore registered tradernaftotCummins; Inc. PowerCornmand, InPower and 'Our energy wo*fng for you." are tradernaft of
Cummins Power Generation. other company, product or service names may be trademarks or service Marks of others,
SAWt (4MB)
Uf, VA
=
Optional AC output
analog meters
CP0,47wer
e oerkeration
AC protection
Over current warning and shutdown
Over and under voltage shutdown
Over and under frequency shutdown
Over excitation Poss of sensing) fault
Field overload
Engine protection
- Overspeed shutdown
- Low oil pressure warning and shutdown
a High coolant temperature warning and shutdown
o Low coolant level warning or shutdown
* Low coolant temperature warning
e High, low and weak battery voltage warning
e Fail to start (overcrank) shutdown
e Fail to crank shutdown
L—A
* Redundant start disconnect
a Cranking lockout
e Sensor failure indication
e Law fuel level warning or shutdown
- Fuel-in-rupture�basin warning or shutdown
Operatorldisplay panel
* Manual off switch
* Alpha -numeric display with pushbutton access for
viewing engine and alternator data and providing setup,
controls and adjustments (English or international
symbols)
# LED lamps indicating genset running, not in auto,
common warning, common shutdown, manual run
mode and remote start
o Suitable for operation in ambient temperatures from
-20 IC to +70 11C
Aftemator data
* Utne-to-neutral AC volts
o Line -to -line AC volts
-P 3-phase AC current
o Frequency
o Total kVA
Our energy worldng for you-rm
AUTAI-QUE it _n 4 112MI'M KSIQ CH
Standard control functions
Engine data
• DC voltage
• Lube oil pressure
• Coolant temperature
Other data
• Genset model data
• Start attempts, starts, running hours
• Fault history
• R6485 Modbue interface
• Data logging and fault simulation (requires InPower
service t000
Digital governing (optional)
Integrated digital electronic isochronous governor
Temperature dynamic governing
Digital voltage regulation
* Integrated digital electronic voltage regulator
* 2 -phase line -to -line sensing
a Configurable torque matching
Control functions
• Time delay start and cooldown
• Glow plug control (some models)
• Cycle cranking
- PCCNet interface
a (2) Configurable inputs
- (2) Gonfigurable outputs
- Remote emergency stop
Options
o Auxiliary output relays (2)
11 120/240 V, 100 W anti -condensation heater
ii Remote annunciator with (3) configurable inputs and (4)
oonfigurable outputs
a PMG alternator excitation
n PowerCornmand for Windows! remote monitoring
software (direct connect)
Ei Auxiliary, configurable signal inputs (8) and
configurable relay outputs (8)
u AC output analogue meters
EJ PowerCommand 2,2 control with AmpSantry
protection
Standard PowerCommand
1.1 control opemtor/dIsplay
panel
u2008 I Cummins Power Generation Inc. I At right,. reserved I Specifications subject to change without noitivs I Cummins Power Goneration
and Cummins ore registered tradernaftotCummins; Inc. PowerCornmand, InPower and 'Our energy wo*fng for you." are tradernaft of
Cummins Power Generation. other company, product or service names may be trademarks or service Marks of others,
SAWt (4MB)
Uf, VA
=
Optional AC output
analog meters
CP0,47wer
e oerkeration

Ratings definitions
Emergency standby power (ESP):
Prime power jPRP).-
Applicable for supplying power to varying electrical load
with ISO 8528. Ten pment overload capability is
available �in accordance with ISO 3046, AS 2789, DIN
6271 ai�d BS 5514.
I r, ZI , — - , I ,
2789, DIN 6271 and BS 5514.
Dim "All I Dirn "S"
M
NIMES Z
This outline drawing is for reference only. See respective model
data sheet for specific model outline drawing number-
zWi
172�7 �
Note: Weights represent a set With standard tures� See outline drawings for weights of other configurations.
Curnmins Power Generation
140D 73' Avenue NE.
Minneapolis, MN 55432 USA
Telephone, 763 574 5000
Fax: [phone]
ILM
Important: Back feed to a utility system can cause electrocution and/or property damage. Do not connect to any building's electrical system
except through an approved deAce or after building main sm(itch is open.
02008 1 Cummiris RmW Generation InG, I All rights resmed I SWtheations subject to ctianqewiOw rotim j Cummins Power Generittion Power
mid Cummins are registered trademarks of C=rrins Inc- PowerCornmaM, InPower and *Out energy worldng for yoa' are trademarks of Gerweration
Curriffflin Power Generation. Other company, product or service names may be tradernaft or service maft Qf others.
S-1 544 f S(41M Cs

BULLETIN 0
Turbidity Meter

1 720Lg
experience + accuracy + simplicity
CW

�Sl
PRINCIPLE OF OPERA11ON
NEPHELOMETRIC MEASIi�MENT
6
Incandescent light directed from the sensor head �down into the turbidirritter body is
a ss'r
scattered by suspended particles in the sample. The se sor`� submerged photocell detects light
scattered at 90, from the incident beam. Ie
T�
SAMPLE FLOW PATH
Sample enters the center column of the tUr'bidimeter, rises into the measuring chamber and ,0
spills over the weir into the drain port. TV
Is configuration results in an optically flat surface
free of turbulence.
6�
SIMPLIFIED CIALIBRATIO
One -point calibration ith prep'ar4
w Stab]Cal' Stabilized Formallsolution eliminates the
errors of formazin suspension ��fu'tion, takes less than two minut4 per sensor, and is a
USEPA-accepted method.
BUILT-IN BUBBLE REMOV
Continuously flowing sample flows through the patented* bubble remo system, which vents
entrained air from the sample stream and eliminates the most significantA- erference in
low-level turbidity measurement. The built-in bubble removal system is imm�', to changes in
sample flow and pressure.
COMPLIANT DESIGN
The 1720E Low Range Turbidimettr applies the instrument design and meets performance criteria
established by the U.S. Environmental Protection Agency (USEPA) in Method 180.1, making it
suitable for regulatory reporting.
ptot 5,831,727
Lw
SIMPLE RELIABLE CALI BRA I ION TOOLS
.................. .......... ................. �­�� ....... ............. ...... ............... ..............
. ...............................
.......... ................
..................... .......
JCE-PIC 1 STABLCALO," �STABILIZED
VERIFICAT ION, MODULE FORMAZIN PRIMAR Y, S ANDA
. ................................. .............................. ...........
I RDS
........... ................ ................ .. . .....................................................................
TheICE-PIQ'Modult i's a new&, fastt'r,way to calibrate and check i > Disposable and nlon�tbxic,
.............. .........
the ance of:Hach 1 72b, st
ptrfor m ries turbidimeters., The,benefits ,
> AVo id preparation and dilution of formazin standards
of -using �tht� ICE�PIC Module include: StablCal st a n d'� r ds
with
�Sl

I 720E
SPECIFICATIONS*
Range
0.001-100 Nephelo metric Turbidity Units (NTU)
Accuracy"
± 20/b ofreading or ± 0.015 NTU (whichever is grnter) from 0 to 10 NTU;
± SO/o ofreading from 10 to 40 NTU; ± 10% of reading from 40 to too NTU
Displayed Resolution
uool NTLI from o to 9.9999 NTUI o.00l NTIJ from 10.000 to 99.999 NTU
Repeatability"
Better than ± 1.0% of reading or ± 0.002 NTU, whichever is greater
Response Time
For a full-scale step change, initial response in I min ute, 15 seconds
Signal Average Time
User Selectable ranging from 6, 30, 60, 90 seconds; user default
30 seconds
Sample Flow Required
200 to 750 ml-Iminute (3.1 to 11.9 galthour)
Storage Temperature
-20 to +60' C (-4 to 140' F)
Operating Temperature
0 to SO: C (32 �22' F) for single sensor system,
tto
0 to 40 C (32 o 04' F) for two sensor system
Operating Humidity
5 to 95% non -condensing
Sample Temperature
0 to So' C (32 to 122' F)
Recorder Outputs
Two selectable for 0-20 mA or 4-20 ni Output span programmable
over any portion of the c -loo NTU range; built into the scloo
Controller
Alarms
Three set -point alarms, each equipped witl- an SPDT relay wth
unpowered contacts rated 5A resistive load at 230 VAC; built into the
scloo Controller
Power Requirements
100-230VAC, 50160 Hz, auto selecting; 40VA
Sample Inlet Fitting
114" NPT fernale, 7/4" compression fitting (provided)
Drain Fitting
1/2" NPT fernale, 1/2" hose barb (provided)
Enclosures
NEMA-4XIIP66 Controller
Digital Communications
Network card compatible; MODBUS/RS485, MODBUSIRS232,
LonWoike protocol (optional)
Wireless Communication
IR Port on the scloo Controller to download into a h@ndheld Personal
Digital Assistant (PDA) or laptop computer via MODBUS
Compliance
Standard Methods 2130B, USEPA 180.1, Hach Method 8195
Certification
Safety:
Listed by ETL to UL 6101OA-1: Certified by ETL to CSA C22.2
No. 1010.1: CE certified by Hach Company to EN G1010-1
Immunity:
CE certified by Hach Company to EN61326 (industrial levels)
Emissions
Class A:
EN 61326, CISPR 11, FCC Part 15, Canadian Interference -Ca using
Equipment Regulation ICES -003
Dimensions
Turbidimeter Body and Cap: 10 x 12 x 16 inches �25.4 x 30.5 x 40.6 cm)
scloo Controller: S.67 x 5.67 x 5.91 inches (14.4 X 14.4 X 15.0 cm)
Mounting
Turbid imeter Body a nd Head Assembly: wal I a nd floor stand
sc100 Controller: wall, pole, panel, and floor stand
Shipping Weight
1720F Tuibidimeter and sc100 Controller: 13.5 bs. (6.12 kg)
1720E Turbidirneter: 10 hs, (4.54 kg�
S.bj,�t to eh�q, �Rhut �t­
Defined according to ISO 15839.
671

HOW TO ORDER
60101-00 1720E Turbidimeter with scloO Controller
60 101-01 1720E Turbidimeter. Sensor Only
1720E with DigitalDirect communications
60101-02 1720EIsclOO with MODBUS/RS485 output
60101-03 1720EIscloo with MODBUSIRS232 output
60101-04 1720E/scIC)o with LonWorks output
60101-05 1720E/scloo with PROFIBUS output
CABLES*
66-1 57960-00 25 fL (7.7 M) Eytension Cable
Power Cord with Strain Relief (125 VAQ
46308-00 Power Cord with Strain Relief (230 VAQ, European Style Plug
*Note: Power cables must be ordered separately.
6AI OPTIONAL ACCESSORIES
ICE -PIC Verification Module/1720E:
52250-00 20 NTU
52215-00 1 NTU
STABLCAL COMPARATIVE CALIBRATION STANDARDS (for 1720E, 1720D,
and 1720C Tu rb id !meters)***
26601-53 20.0 NTU, I L each
— Note: Calibration Cylinder must be ordered separately.
STABLCAL VERIFICATION STANDARDS
26598-S3 1.o NTU, 1 L each
27463-53 40.0 NTU, 1 L each
26979-53 0.3 NTU, 1 L each
26980-53 o.s NTU, 1 L each
27233-53 0.1 NTU, I Leach
FORMAZIN CALIBRATION STANDARDS
44156-00 Formazin Calibration Kit for user -prepared calibration includes 4000 NTU Formazin, (500 mQ, TenSette, Pipet,
and Calibration Cylinder
2461-49 Formazin Primary Standard, 4000 NTU, 500 ml_ replacement for kit #44156 -Go
44153-000 Calibration Cylinder, 1L
57432-00 Floor Stand
MODEL SCJOOTM CONTROLLER
The Model scloo Controller receives data from one or two
sensors. Its "plug and play", mix -and -match operation lets it
fit into any facility or workflow. Digital communication with
any Hach digital sensor or probe is simple and reliable.
i, s,,,
MODEL SCI OOOTM CONTROLLER
Get the same great features as the scl 00 Controller above—
"plug and play", all digital operation and communication—but
with the Hach sc1000 Controller, up to eight Hach sensors
can be used with one controller in any combination. The
sc`1000 Controller is also expandable and upgradeable to
easily adapt to you needs.
F7
Lit. No. 2446
155 Printed in U.S.A
0 Hach Company, 2005. Ad[ rights reserved.

ATTACHMENT M
Pole Blowe Curve and Cut -Sheet

ATTACHMENT N
Back -Up Generator Cut -Sheets

ATTACHMENT 0
Turbidity Meter
6-d