WQ0033455_Engineering cals and product bulletins_20081119

01
kL
NOV 2 12663
THE CLIFFS AT HIGH CAROLIN�k
� pvnl�'
BUNCOMBE COUNTY, NORTH CARO
WASTEWATER IRRIGATION
SYSTEM
CALCULATIONS AND PRODUCT
BULLETINS
PREPARED FOR:
THF, CLIFFS COMMUNITIES
MR. DON NICKELL
3598 HIGHWAY 1 1
TRAVELER's REST, SOUTH CAROLINA 291590
ORIGINAL: OCTOBER 21, 200a
REVISED: NOVEMBER 1 9, 2008
aROOKS ENGINEERING ASSOCIATES
PROJECT No. 307808
17 Arlington Street
Asheville, NC 28801
828.232.4700

THE CLIFFS AT HIGH CAROLINA
BUNCOMBE COUNTY, NORTH CAROLINA
WASTEWATER IRRIOATION SYSTEM
CALCULATIONS AND PRODUCT
BULLETINS
PREPARED FOR:
THE CLIFFS AT HIGH CAROLINA, LLC
359B HIGHWAY I I
TRAVELERS REST, SC 29690
FINAL DESIGN - NOT RELEASED FOR CONSTRUCTION
ORIGINAL: 013TOaER 22, 200B
REVISED: NOVEMBER 19, 2008
BROOKS ENGINEERING AssocIATES PROJECT No.: 30780B

I
TABLE OF CONTENTS
1.0 Calculations
1.1 Design Flow Table and Phasing Summary
1.2 WWTP Head Calculations and Process Calculations and Supporting Charts
1.3 Pump Curve for Irrigation Dose Pumps and Pump Curve for
Pumps in Series
1.4 Pump Curve and TDH Calculations for Return Pumps and Tanks
1.5 Return Pump Tank Sizing Calculations
1.6 Irrigation Zone Pressure and Flow Analysis
1.7 irrigation Schedule Spreadsheet
1.8 Rainfall Data Analysis for Short -Term Wet Weather Storage
Requirements
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 WVVTP Pumps: forward
flow/recycle pumps, sand filter flow pumps, equalization tank
grinder pumps, sludge tank decanting pump.
Bulletin C
Cut -Sheets for WV\1TP Blowers
Bulletin D
Cut -Sheets and Pump Curve for Irrigation Dosing/Flushing Pump
Bulletin E
Cut -Sheets for Flushing Return Pumps
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 0
Turbidity Meter

1.0 Calcu ations
1.1 Design Flow Table and Phasing Summary
1.2 WWTP Head Calculations and Process Calculations and Supporting
Charts
1.3 Pump Curve for Irrigation Dose Pumps and Pump Curve for
Pumps in Series
1.4 Pump Curve and TDH Calculations for Return Pumps and Tanks
1.5 Return Pump Tank Sizing Calculations
1.6 Irrigation Zone Pressure and Flow Analysis
1.7 Irrigation Schedule Spreadsheet
1.8 Rainfall Data Analysis for Short -Term Wet Weather Requirements

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.4
1.1 Design Flow Table and Phasing Summary

BEA Project # 307808
The Cliffs at High Carolina
Design Flow Calculations
Priase I uesign mow: wo'v IV
Phase 11 Design Flow: 103780
Total Design Flow: 199,690 gpd
Site I —F—
Phase I Buildings
Floors
I unitalfloor I
brl unit
tlowlbr
51
21
120
—
Site 2
Phase I Buildings FRoars I units1floor I brl unit flowl br
000 gpd
Site 3
Phase I Inn bedrooms HOW&
48 1201 5,760 gpd
Phase I Restaurant seats flowlseat 1
120 401 4,800 gpd
Phase I Market Area (sq. ft) gall 1000 sq. ft
9000 100 900 gpd
Phase I Banquet seats flowl seat
60 30 1,800 gpd
Phase I Spa persons Flow1person
200 101
site 5
Phase I I Village Wellness Sq. Ft I Flowl 100 sq. ft
J09�
1 1 8-0001 4 70 0: d—
Site 7
Phase I I Clubhouse w1person
1 601
site 9
Phase I Strauss Lake SF units brl unit
161
Site 10
Phasel Practice Goff SF
41 1201 3,840
1 gpd
masp I I Goff Maintenance I sq. Ft W/ 100 sq. ft
1 7.50(
Site 4
Sq. Ft Flowl 100 sq, tt
5,0001 1 1 2,5001 gpd
Site 6
Tn—its—lbldg
[brlunit
I flowl br I-
81
Site 8
brl unit lflowlbr I
site 11
Phase H Clubhouse Cottage SF units brl
F-,
41
Site 12
—Lunits I brl Iflow1br
1 :1:�9�,2009pc
n��e
�LotsSF
1 401 4
Site 14
Phasell 1011age Lake OverlooK �Buildings - I units jbr1un=itflow1br
Prepared by: Matthew Rice Brooks Engineering Associates, PA 11118/2008

1.2 WWTP Head Calculations and Process Calculations &
Supporting Charts

PROCESS CALCULATIONS
The Cliffs at High Carolina
Aqueonics Treatment Plant
PUMP HEADLOSS CALCULATIONS
A. Egualization Tan
Average daily flow 100,000 gpd equalized at 70 gpm. for Phase 1. 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 I - 2" — 90'ell
3 - 6" - 90'ell
Pipe length 161-2110
61-6110
Friction Loss/Ft. of Pipe
211 o loss = 15.87100'
6"o loss= 0-17100'
Fitting loss in equivalent feet of pipe,
211 ell = 5.2'x 1 pe. 5.2'
6" ell = 15.3'x 3 pc. 45.9'
Total frictional loss:
2"o=[l6'+5.2']xl5.8/l00= 3.34'
61 o = [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 247
Approximately 25'TDH for pump sizing,
P. I

I
I
Since 26.4 lbs. of ammonia -nitrogen remain, we have available 7418 f� per lb. of influent
ammonia (195840ft�/ 26.41b). On first iteration, therefore, Figure 4-15 tells us that
approximately 1.5mg/I effluent ammonia concentration could be predicted, which is more
than the 1.0 mg/I 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 11; (Iteration 2 - regycle.)
By recycling flow from Aerobic stage III to the suction of stage 1, 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/I x 70 gpin + 2.27 mg/I x 74 gpm = 26.17 mg/I x 144 gpin
26.17 mg/I x 8.34 x.144 MGD = 31.43 #/d of BOD, or 10.92 lb/d/1000 cuft.
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 gpmJsq. ft., resulting in a discharge concentration of .3 3 x 26.17 = 8.63 mg/l
Tower 11 discharae:
BOD = 8.63 mg/l, 10.36 lbs/day
Ammonia -N = 22.31 mg/l, or 21.2 lbs/day
Nitrate -N = 22.3 mg/l, or 26.8 lbs/day
G. Stage 111; (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 111. 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- __ refore 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/l = 17.8 lbs/day
p. 7

I
I
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 flow 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 111, compared to that coming from Tower I. Submerged weirs in Anaerobic I and 11, 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/l, = 1.9 lbs/day
AmmoniaNitrogen <lmg/1=0.83lbs/day
Nitrite Nitrogen = 0 mg/1 = 0 lbs/day
Nitrate Nitrogen < 3 mg/I = 2.5 lbs/day
H. Anaerobic Calculations
The tianaerobic" 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 ft�/fL3 placed
atop precast concrete hoppers on fiberglass beams within the tankage. Influent enters each
itanaerobic" 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/I nitrate -nitrogen has been achieved in similar facilities
The process of anoxic denitrification is confirmed by EPA design data. (Process Desi n Manual
for Nitrogen Control. U.S. EPA Technology Transfer. October, 1975.)
Figure 5-13 shows that submerged high -porosity media reactors remove, at 130 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 :
P. 8

0
I
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 IN /1,000 ft3/day of fixed media
= 0.0696 lbs N per W of fixed -film media/day
= 0.069 lbs N /W media using 30 W1ft3 media
= .00232 lbs N 1W 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 ft� or more of surface per
gpd, which is the nitrogen removal capacity of 0.00232 lbs N/ft�/day x.33 ft�/gpd =.00076 lbs
N per gallon per day.
However, the influent N concentration, at 60 mg/l, 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 1, 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 NITRWICATION- EFFICIENCY
EFFECT OF ORGANIC10AD ON NITRIFICATION -EFFICIENCY
MW
OF ROCK TRICKLING FILTERS
too
r
Z
NO RECIRCULATION'
80
M RECIRC04ATION
f Kq y 6 2,4 1 b 'BOD5/1 000 Cu f t/daY
/M
40=-
rc
20-
0,
0
20 30 40 50 60
BOD5 LOAD LB11000 CU FTIDAY
I
Ai
7

FIGURE 4-15 SURFACE AREA REQUIRED FOR NITRIFICATION
FIGURE 4-15
WRIACE MtLA
ItEQUIRLMENTS FOR
NITRIFICATION -
MIDLAND MICHIGAN
W100D
A
@
Lnitluent D013, (mean)
15 - 2 0 mq/t
C4
Organic iN 1- 4 ma/l
N, 11 N 8 - M M-
4
B00�,/TKW
1
Oil
r�, �
0
44
'0
(D
7 to
b*1
Lu
4,0,0*
to 19C
Key:
�r 7 to stc
1 SF/lb/day
0, M�/ Pg /ony
Z) T 13 iG 13C
3,0
4,0 5,0 6D
EFFLUOVT AMMOMIT-N, fnql�
4-64

VC — 5.0-477-1 BFGoodrich Information Bulletin
OFGocWrich
General Products Division
DESIGN CALCULATION RESULTS
TREATABILITY FACTOR K 20 = 0.07
Influent Wastq Temperature — 4VC
A 21PIO
INFORMAi N
BULLETIN
500souvlMaivslmol
Akron, Ohio 44318
DepaAmOnl 0444. WHB-3
VC -5,0-477-i
VINYL CORE'y'
Influent Waste Temperature — 130 C
%
BOD
RernOyeCl
Media Depth
Raw Flam Expn:9!:;E)
Media Depth
RawFjowEVressedin
PM/ft.- of Tower Surface Area
0.5
Feet
—F2—
—14---
16 -
—0,3 0.45
7�57 '
63
-77 67
-0�7 2
86 79
9 81
91 84
92. 86
--�i3 88-85
94 89
-95 91
5 93
O�-6
54,
.59
ft$41
�-8E
72
76
79
81
83
87
-W---87
go
91
2
O�7
51
56
bi
66
6
73
79
--- 81
83
85
88
go
, 91
0.8
49
64
59
6-3
67
7D
74
76
79
81
83—
8-5
8,6
88
89
0.9
47,
52
57
6-1-59
65
68zk
72
74
77
79
81
B-3
85
86
88
1,0,
4-!Y—;F3
50
55-
6377671--
66
-:7 p
72
75
77
9-0
81
83
85
8;
1.1
48
53
57
�05
ub
71
73
76
78
80
82
83
85
1,2
42
47
52
—
6
63
66
69
�2
74
77
79
80
82
84
1.3
41
50
54-53
58
62
-65
68
70
73
75
77
79
81
82
1.4
40
44
49
57
60
�3
66
69
72
74
76
78
-�Q
81
1-5
39
43
48
52
56
59
62
65
68
70
73
75
77
�9
80
1 �8
—0—
22
24
28
30
'34
36
�38
—
40
Influent Waste Temperature — 130 C
% 130D Hemovea
Media Depth
Raw Flam Expn:9!:;E)
.1, c)f Tower Sijrface Area
Feet
0.3
0.5
O�6
0.7
0.b
U.0
1.0 1A
1�2
1,3
1,4
1.5
12
52
50
45
44
43
42
14
75
6-0
66
7-1
i
—68
0
65
58
63
56
60
—5-�
59, 67
50
55
49
54
48
62
47
51
18
84
75
72
69
67
6,5
63 61
60
58
57
55
201
87
79
�76 ----
73
---
7 1
69
6 7 65—
63
62
61
59
22
79
76
74
72
70. 6p�
6
65
64
63
24
91
I--
85
82
79
� I
77
--
80
75
,
3
73 7.2
6 74
70
73
69
7i--7-0
67
66
6-9
26
28
93
94
87
89
84
-- 86 --
84
82
so
79 77
--
75
74
73
72
30
9.5
----
go
88
---9-6--84
82
61 79
78
76
7-
5
74
32
95
92
--
90
88
86
84
83 81
80
79
77
76
34
95
!�3
91
89
88
86
85--,- , 83
82
81
79
78
36
96
94
4
Q-2
3
91
89
go
88
8g
86 k6§�7
4
85
82
84
81
83
80
82
38
40
95
88
87
83

FIGURE 5-12 VOLUME DENITRIFICATION RATE
I
Mlrolyo-
Q
Z 2000
u
1600
ku
12(X
40
FIGURE, 5-13
VOLUME DENITRIFICATION RATE FOR SU13MERGED
HICH POROSITY FINE MEDIA COLUMNS (REFERENCE 39)
to 4u
TEMPERATURE) C
ut
to 4u
TEMPERATURE) C

1.3 Pump Curve for Irrigation Dose Pumps and Pump Curve
for Pumps in Series

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

I
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-1/16/2008 12:21pm wwS1
1111 Alla C 0
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pumps
lProject: Waste Water Svstema
f-1 ov,
I
0� 6o
I
40
20
0
7702766535
LC - 20953 Configured Curve
Tag # P -I P-2
Model: 20953
Oty; 2
Service:
#439 Page 11/12
By: TGJ
Date: I0/9/20nR
Rev. #
.0. #
SPE
0 so 100 150 260 300 350 400 450 Soo 550 600 650 700
Capacity - usgpm
9.60 in Max
... . ...... . ..... j
J
.................... .
. ....... .........
. ...... ...........
Fluid: Water
Power
. .. .
-------
Temp: 69.00 dog F
. ... ............ -
�Autoff Head-,
363 ft
... . . ......
Diff. Press:
0 so 100 150 260 300 350 400 450 Soo 550 600 650 700
Capacity - usgpm
9.60 in Max
100
-90
'80
,70
-60
-50
-40
30
.20
.10
IN
0 so 100 ISO 1.00 260 300 350 400 450 500 Sso 600 650 700
Capacity - usgpm
V- 40
POO
�20
0
0
50
. ....... .........
. ...... ...........
Fluid: Water
TQ.S4 In Rated
. .. .
.................. .. .
Temp: 69.00 dog F
Die. Press,
�Autoff Head-,
363 ft
. . . . .............
Diff. Press:
PSHr,
7.04 ft
Visc.; 1.00 op
SHP: 30.3 hp_
17p--U—la
. ............ .... ... .
Fump Eff.: 58.16
4
Ob Of Stages,
I
ISEP: 426 USgpm_
III's
Mbtdr Data,
. ..... .
I i!
40
Voltage: 208-2301460
jEff;
W;m1nal RPM:
3500
Phase: Three phase
F.; 1.15
Actual RPM,
3500
Hz., an
jEnol.-_ ODP
7.00 in Kin
.. ..... . .....
.... ... . ..
...... . ....
. .........
100
-90
'80
,70
-60
-50
-40
30
.20
.10
IN
0 so 100 ISO 1.00 260 300 350 400 450 500 Sso 600 650 700
Capacity - usgpm
V- 40
POO
�20
0
PSHr 1
.......... . .............
..... ............... . 7
Capacity - usgpm
M
0
50
W;
200 USqpm
Fluid: Water
Suet Press: 0-00_psi.a
)H:
PSHr 1
.......... . .............
..... ............... . 7
Capacity - usgpm
M
Desl�n Data`,._',:.`,
W;
200 USqpm
Fluid: Water
Suet Press: 0-00_psi.a
)H:
350 ft
Temp: 69.00 dog F
Die. Press,
�Autoff Head-,
363 ft
S.C., 0.998
Diff. Press:
PSHr,
7.04 ft
Visc.; 1.00 op
SHP: 30.3 hp_
17p--U—la
9.54 In
Fump Eff.: 58.16
4
Ob Of Stages,
I
ISEP: 426 USgpm_
III's
Mbtdr Data,
I i!
40
Voltage: 208-2301460
jEff;
W;m1nal RPM:
3500
Phase: Three phase
F.; 1.15
Actual RPM,
3500
Hz., an
jEnol.-_ ODP

WWSI 7792766535 #439 Page 12/12
�4
MOTOR DRIVE
B,'r,>, T P M S
Nominal RPM 3600 1:3-a s ed o n F resi-r- Wclerr E*- &B-- d-�b-q, F
rrnpt�rrer Dirarnutur.
J 0
J
9.0
tat W
)W
1 L
12;q r,_Vre
POW.
25 so 75 100 125 150 275 3C
CAPACITY IN (WA.014C, PER MINUTE
7-&
70
ZZ
L.1 LAJ
1AJ
65
L.0
60
0:
LLJ
"10.0
OL
OL -
0
SIELECTWYN
CONMTTOWSS
1111!!1
PRL K
200.0 GPM
Priming Type:
9 E
Total Dynamic Head:
140.0 feat
I�A-ot-or Loading.
Stand"ard
PUMP DESCRIPTION
�4
MOTOR DRIVE
B,'r,>, T P M S
Nominal RPM 3600 1:3-a s ed o n F resi-r- Wclerr E*- &B-- d-�b-q, F
rrnpt�rrer Dirarnutur.
J 0
J
9.0
tat W
)W
1 L
12;q r,_Vre
POW.
25 so 75 100 125 150 275 3C
CAPACITY IN (WA.014C, PER MINUTE
7-&
70
ZZ
L.1 LAJ
1AJ
65
L.0
60
0:
LLJ
"10.0
OL
OL -
0
QUOTED BY -
TAS
Q UOTED TO.
brooks jo-b cliffs,
SIELECTWYN
CONMTTOWSS
Flow:
200.0 GPM
Priming Type:
Standard
Total Dynamic Head:
140.0 feat
I�A-ot-or Loading.
Stand"ard
PUMP DESCRIPTION
Pump Model-
E32TPMS
Priming Type:
Stan-dard
Impeller Diameter:
6. 1 a a i -n.
I-rnp-ial-ler Material;
Iron
Suction:
2Yz"KPT
Dircharge-
2"NPT
Shaft Seal;
Mechanicar
FUMF PERFOH24ANCE
Flow:
200-0 GPM
Flo.wer-
9_7 E�.H.p
ToLal Dynamic Head;
1 40.6 feet
Efficiency:
7 3-.4 %
Nominal SpL-_ed:
3600 RPM
NPSHR;
'14.2 feet
Shut—Off Head:
154.3 feet
Max Flower:
T'T_0
Sest Eff; 73.7 (9� 21-4,gr OF"K4
MOTOR
Size:
10 HP
Enclosure:
TEFC
voltaye.; CorisulL Catalog/Facto.ry
HZ/Phn.se.,
PRICE/ORDER
Ela�RMATIGN
Catalog No..,
Fo oto ry
wcighl::
200 lbs.
QUOTED BY -
TAS
Q UOTED TO.
brooks jo-b cliffs,

1.4 Pump Curve and TDH Calculation for Return Pumps

BUNCOMBE COUNTY, NC THE CLIFFS AT HIGH CAROLINA PROJECT #307808
TDH = AH + h,
where:
AH elevation head
h, major pipe losses, utilize Hazen Williams equation with equivalent lengths for fittings
hm (4.727 U d 4.17) (Q/c)1.85 where: Q in cfs, L in feet, d in ft.
n o user input
user input req'd
Piping: inal) equals 2.047 inches (11))
Diameter vlwwa 0.1705833 ft.
i
Q (gpm)
AH
hm (feet)
TDH
PSI
Velocity
5
173.001
0.34
173.34
75.0
0.51
10
173.00
1.24
174.24
75.4
1.02
Is
173.00
2.63
175.63
76.0
1.53
20
173.00
4.48
177.48
76.8
2.04
22
173.00
5.35
178.36
77.2
2.25
25
173.00
6.78
179.78
77.8
2.55
30
173.001
9.50
182.50
79.0
3.07
35
173.00
12.64
186.64
80.4
3.58
40
173.00
16.19
189.19
81.9
4.09
45
173.00
20.14
193.14
83.6
4.60
173.00
24.47 1
197.471
85.5
5.11
Brooks Engineering Associates, PA P. I of 1 10/21/2008

Will
H P
Part Number
H P
Voltage
Phase Amps
Stages
Height
2 9-
--9032 0-005 1/2 115 1 12.0 4
80-
5030-0005
1/2
115
10 GPM Models
6
2248�'
5032-0009 1-1/2 230 1 13.1 10
HP� 10 STAGE
314
PUMP PERFORMANCE CURVE
112
230
10GPM
6
22-318'
11/4" NPT DISCHARGE
1 98
120- 400-
1 1 1
31� HP- 12
V2
112 - 360
FAGE
8
1 04 -
�Q
1/2 K P� 4 STAGE
1-1/2
9 320
5030-0008
112
': 280
1 6.0
8
60-
112 HP- 8 STAGE
72- 240-
—TO3-0-0009
314
64
1 8.0
12
200-
S6-
112 H 6 ST GE
1 24-
0
48- 160-
ID
40- 120-
32-
2u ILI
40-
24- 80-
16 40-
k_.
0-
8-
10 4 66 60 60 I�B 40
6 8 10 12 14 16 18
5 10 15 20 25 30
GALLONS
UTERS
8' JS 24' 3'2 410 48 5'6 64
FLOW PER MINUTE
FLOW PER MINUTE
015413
Will
H P
Part Number
H P
Voltage
Phase Amps
Stages
Height
2 9-
--9032 0-005 1/2 115 1 12.0 4
80-
5030-0005
1/2
115
1 12.0
6
2248�'
5032-0009 1-1/2 230 1 13.1 10
HP� 10 STAGE
314
5030-0006
112
230
1 6.0
6
22-318'
230
1 98
9
—TO -30-0007
V2
115
1 120
8
24-1/8'
�Q
1/2 K P� 4 STAGE
1-1/2
230
5030-0008
112
230
1 6.0
8
24-1/8"
FN N\\
24-
—TO3-0-0009
314
230
1 8.0
12
28-7/8'
Will
H P
300-
H P
88-
Phase Amps
27 GPM Models
Height
2 9-
--9032 0-005 1/2 115 1 12.0 4
80-
WWI
PUMP PERFORMANCE CURVE
27 GPM
ko^
240-
I 114'NPT DISCHARGE
26-7116'
5032-0009 1-1/2 230 1 13.1 10
HP� 10 STAGE
314
Will
H P
300-
H P
88-
Phase Amps
I Stages
Height
2 9-
--9032 0-005 1/2 115 1 12.0 4
80-
260-
21-1/8'
72
240-
foR,
26-7116'
5032-0009 1-1/2 230 1 13.1 10
I
314
;ac -,PM 0
1 8.0
64-
203- In#
314 HP
1
230
1 98
9
18D
64-
48-
50
4
24-16/16'
�Q
1/2 K P� 4 STAGE
1-1/2
230
56-
13.1_
3 2-
1 D- -.1i V, x
FN N\\
24-
00- — —
112 HP
0G.
5 STAGE
1 24-
0
80----
ID
1 -
2u ILI
40-
—
W
-CNS
0-
UTERS
10 4 66 60 60 I�B 40
FLOWPERMINUTE 015046
5 10 15 20 25 30
GALLONS
Will
H P
Part Number
H P
Voltage
Phase Amps
I Stages
Height
115
--9032 0-005 1/2 115 1 12.0 4
21-118'
5032-0006 1/2 230 1 6.0 4
21-1/8'
5032-0007 314 230 1 8.0 6
24-5116'
-T --6658 —1 — 230 1 9.8 7
632
26-7116'
5032-0009 1-1/2 230 1 13.1 10
31 -718 -
Will
015414
Part Number
H P
19 GPM Models
Phase Amps
Stages
Height
5031-0005
112
115
PUMP PERFORMANCE CURVE
5
21-15116'
19 GPM
112
230
1114" NPT DISCHARGE
5
280 -
---4,1 HP - 9 STAGE
314
80-
1 8.0
72-
240 -
314 HP
1
230
1 98
9
7 STAGE
64-
1
9.8
4
24-16/16'
200
1-1/2
230
56-
13.1_
48-
16.0
< 40-
120 -
112 HP
32-
5 STAGE
1 24-
0
80----
NA
1 -
40-
—
8-
0-
5 10 15 20 25 30
GALLONS
LITERS 210 4'0 110 80 100
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
21-15/16'
5031-0007
314
230
1 8.0
7
25-1/16'
5031-0008
1
230
1 98
9
28-1/8'
35 GPM Models
PUMP PERFORMANCE CURVE
75 35 GPM
2" NPT DISCHARGE
56- ISO- i-ir).4-5siAGE
48- 160-
140--IHP-48
40-
120-
W4 HP - 3 STAGE
9 32 -
loo
24- So- 112HP-2STAGE
6
is -
40
a- 2()]
LLONS lo 1� 4o 10 10
LITERS I
40 80 120 160 200
FLOW PER MINUTE 015044
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
19-7/16'
5033-0007
314
230
1
8.0
3
22-3116'
5033-0008
1_
230
1
9.8
4
24-16/16'
5033-0009
1-1/2
230
1
13.1_
6
29-15116"
@ Copyright 2007 Zoeller Co. All rights reserved.

BUNCOMBE COUNTY, NC THE CLIFFS AT HIGH CAROLINA PROJECT #307808
TDH = AH + h,
where:
AH elevation head
h, major pipe losses, utilize Hazen Williams equation with equivalent lengths for fittings
hm (4.727 U d 4.117) (Q/C)1.85 where: Q in cfs, L in feet, d in ft.
no user input
user input req'd
'I
Piping:
Diameter
fflinches (!-ominal) equals 2.047 inches (ID)
0.1705833 ft,
Q (gpm)
1�s
hm (feet)
TDH
PSI
Velocity
6
175.001
2.10
177.10
76.7
0.51
10
175.001
7.59
182.59
79.0
1.02
16
175.00
16.09
191.09
82.7
1.53
20
175.00
27.41
202.41
87.6
2.04
24
176.00
�38.42
213.42
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
175.001
77.28
252.28
109.2
3.58
40
175.00
98.96
273.96
118.6
4.09
45
175.00
123.08
298.081
129.0
4.60
50
175.00
149.60
1
Brooks Engineering Associates, PA P. I of 1 10/21/2008

10 GPM Models
ffi PUMP PERFORMANCE CURVE
10 GPM
1 1/4" NPT DISCHARGE
120 - 400- —
- T-1 1
112 - 360 314 HP- 12 STAGE
104 -
96 320-
88 280-
80 V2 P, 8 67AGE
72 240 -
64
5 200, 6 STAGE
112 Hp� 6
6 112 HR� 6
160
40
120-
32
24
le
40-
8
0
0 12 14 16 18
GALLONS
LITERS 8' 16 24 j2 �0 �e 66 6�
FLOW PER MINUTE 015413
Part Number
H P
Voltage
Phase
Amps
Stages
Height
-�-03-0-0005
- 112
115
1
12.0
—
6
—
22-318"
-�2-31&-
- —
R30-0006
---
112
—
230
—
1
6.0
6
21-1/8'
r
�030 0-007
—1/2
115
1
—
12.0
—
8
24-1/8"
0008
�0-3-0
—
1/2
—
230
1
—
60
—
8
—
24-1/8'
r—
_�()30_0009
—
3/4
—
230
1
8.0
12
28-7/8 -
c
27 GPM Models
H P
PUMP PERFORMANCE CURVE
Phase
W GPM
1 11,4'NPT DISCHARGE
;11 H
+c>
1 112 Hp- �12S I
00 1 1 1
x I I
wwTF'
72 240- 1 HP- 7 STAGE
220-
- STAGE H
209 om HP "70
4B 160
W2 HP- 4 STAGE
120-
2
4
2
2,
1
1
0
2.
M
32 106.
80
60
16
40
20-
5 1 1�5 10 15 �0 55 40
GALLCNS
1 140
6C 80 100
UTERS 40
1 20
FLOWPERMINUTE 015045
Part Number
H P
Voltage
Phase
Amps
Stages
Height
-�-03-2-0005
12
115
1
19 GPM
4
21-1/8'
8
Fo3-2-0006
1/2
P34
230
1
P12.0
6.0
4
—
21-1/8'
r
-�0-32--0007
1
230
1
8.0
6
51
24-5/16'
--R-31 0008
1
230
1
9.8
7
26-7/16'
-T63-2-66og
1-1/2
230
1
1
13.1
1 10
1
31-7/8
015414
Part Number
H P
19 GPM Models
Phase
Amps
Stages
Height
�0-31--0005
PUMP PERFORMANCE CURVE
11-5
1
19 GPM
5
21-15/16'
1W NPT DISCHARGE
112
280 -
I HP -I STAGE
1 HP-ISTAOE
80
5
-
72
240 -
P
314 P
14HN
2-30
—1
STAGE
7 STAGE
64
1 9.8
--R-31 0008
1
200 -
1
56
9
5
48
ISO -
< 40
120 -
1/2 HP
3E
a2
5STAGE
24
80-
16
40 -
8
0
5 10 15 20 25
F
GALLONS
LITERS 1 2'0 40 60 so 10
FLOW PER MINUTE
015414
Part Number
H P
Voltage
Phase
Amps
Stages
Height
�0-31--0005
1/2
11-5
1
12.0
5
21-15/16'
5031-0006
112
230
1
6.0
5
-
21-15/16"
-E-1/16
--�031 0-007
-5�4-
2-30
—1
8-0
7
1 9.8
--R-31 0008
1
230
1
98
9
5
0 1 1 1
GALLONS I 10 5'0 60
T---T—
LITERS 0' �o 80 120 160 200
FLOWPERMINUTE 015044
Part Number
35 GPM Models
IHP-48TAGE
40
PUMP PERFORMANCE CURVE
Height
35 GPM
120-
2" NPT DISCHARGE
56 180-
2
314 HP - 3 STAG
1-1/24-55�AGE
100-
230
48
160-
1/2HP-2STAC
5033-0007
0 1 1 1
GALLONS I 10 5'0 60
T---T—
LITERS 0' �o 80 120 160 200
FLOWPERMINUTE 015044
Part Number
140-
IHP-48TAGE
40
Stages
Height
5033-0005
120-
116
9 32
2
314 HP - 3 STAG
-Z
z
100-
230
24
so-
1/2HP-2STAC
5033-0007
314
230
1 8.0
so -
22-&16'
5033-0008
1
M
1 9.8
40
24-15/16'
0 1 1 1
GALLONS I 10 5'0 60
T---T—
LITERS 0' �o 80 120 160 200
FLOWPERMINUTE 015044
Part Number
H P
Voltage
Phase Amps
Stages
Height
5033-0005
112
116
1 12.0
2
19-7116'
5033-0006
1/2
230
1 6.0
2
19-7116'
5033-0007
314
230
1 8.0
3
22-&16'
5033-0008
1
230
1 9.8
4
24-15/16'
5033-0009
1-1/2 .
230
1 13.1
5
29-15/16'
@ Copyiright 2007 Zoeller Co. All rights reserved.

1.5 Return Pump Tank Sizing Calculations

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

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1A-1
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
j operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unle
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H U.2
2 Total Segment Headloss (ft) = Friction + Elev.
I Inputs I Dose Flow �a)j Flush Flow (b)l
0.016 0.014
12.016 12.014
711� I Brooks Engineering Associates, PA p.2 of 3 10120/2008
61
Hydraulic Unit
H.U. Elev NEW
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to A
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (In)5
3.058
2.778
4 Friction Headloss (ft)
0,306
0.278
Minor Losses (ft)
Line Velocity (ft/s)
2.27
2.16
A to J2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
0.434
0.902
Mq
5 Friction Headloss (ft)
0.043
0.090
Minor Losses (ft)
Line Velocity (ft1s)
1.16
1.73
J2 to 1A-SM2
Segment Flow Rate (gpm)
Line Length (ft)
MW
Line Size ID (In)5
1.512
4.770
6 Friction Headloss (ft)
0.151
0.477
Minor Losses (ft)
1.25
2.33
Line Velocity (ft/s)
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
4
Win
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Lateral5
Elevation (ft) from Manifold to Bottom Feed Lateral5
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
0.700
3.213
9 Total Segment Headloss (ft) = Friction + Elev.
-26.300
-30.787
Return Force Main Friction Losses
rllffl�
1A-RM2 to J2
[
Segment Flow Rate (gpm)
Willi
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
10.131
r
Friction Headloss (ft)
2.54
Line Velocity (ft1s)
J2 to A
Segment Flow Rate (gpm)
Line Length (ft)
49 11 0
Line Size ID (in.)
Minor Losses (ft)
1.853
Friction Headloss; (ft)
Line Velocity (ft/s)
2.03
A to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
W9
Minor Losses (ft)
3.782
Friction Headloss (ft)
2.03
Line Velocity (ft/s)
ido t
Return Line Elevation Delta
Elevation (ft) from Return Manifold to VVWTF
EMEM
711� I Brooks Engineering Associates, PA p.2 of 3 10120/2008
61

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. F—
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)
164.3
66.5
PRV setting utilized
127.1
W,10
Low Pressure Check: P at Min. Flush Flow at Return Manifold
39.1
16.9
Flush Pressure at WWTF for Min. Flush Rate
113.3
49.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
146.4
63.4
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

I
N
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engine i'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.) 4, 7) (Q/c)1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d 8
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A E I th Re uired Flush ate plus a Dose low Rate
0 -1
K2
leg1A-2
No. L. Eali
. La ' s
1 15 1
.
Tubin : 15D in)
0.79
mitters h
E tt
0.62
Emitter S acin it
'd Flush Rate (gpm)':
Total Foota a:
1 6908
Deskin Flow (9pm):
I UO.b'd
Application Flow �gprr):
35.7 -
Min. Desig Scour Vel. (itts)
2.0
1�ng ID (in)
0.787
Residual Flow for Scour (gp
2.30 _
'd Flush Rate (gpm)':
70.2
Supply Manifold EleV.
lA-SMl
Return Manifold E
Run
IA-RMl
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Len th
# Emitters
Flow ,_�7
1 Pnnth ft
- '-- -
-
1 1
121
1.3
484
2.5
4.8
2
121
1.3
2 3
120
1.2
478
2.5
4.8
4
119
1.2
3 5
118
1.2
472
2.4
4.7
6
118
11.2
4 7
117
1.2
466
2.4
4.7
8
116
1.2
5 9
116
1.2
462
2.4
4.7
10
115
1.2
6 11
115
1.2
458
2.4
4.7
12
114
1.2
7 13
113
1.2
448
2.3
4.6
14
ill
1.1
8 15
108
1.1
434
2.2
4.5
16
109
1.1
9 17
110
1.1
442
2.3
4.6
18
Ill
1.1
10 19
114
1.2
462
2.4
4.7
20
117
1.2
11 21
119
1.2
480
2.5
4.8
22
121
1.3
12 23
123
1.3
490
2.5
4.8
24
122
1.3
13 25.
122
1.3
488
2.5
4.8
26
122
1.3
14 27
104
1.1
418
2.2
4.5
28
105
1.1
15 29
106
1.1
426
2.2
4.5
30
107
1.1
-
-
RQnR
:14b4
50.1
35.7
70.2
Brooks Engineering Associates, PA p.1 of 3
10/20/2008

n 3.782
Friction Headloss (ft) 2.03
Line Velocity Ws)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
P"! Brooks Engineering Associates, PA p.2 of 3 10/20/2008
�maii I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE IA -2
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
In
LINE
1 —Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unie
Line length (ft) from P.T. to H.U.5
M"
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.2
0.016
0.014
2 Total Segment Headloss (ft) Friction + Elev.
12.016
12.014
no,
Hydraulic Unit
H.U. Elev [ISM
3 Headloss from H.0 (ft.)3 RaffifflEMEMEW
Supply Force Main Friction Losses
H.U. to A
Segment Flow Rate (gpm)
Line Length (ft)
MW=2.778
Line Size ID (In)a
4,
4 Friction Headloss (ft)
0.306
0.278
Minor Losses (ft)
2.27
2.16
Line Velocity (ftts)
A to J2
Segment Flow Rate Wpm)
Line Length (ft)
Line Size ID 0n)5
5 Friction Headloss (ft)
0.434
0.902
no�
Minor Losses (ft)
0.043
0.090
Line Velocity (ftfs)
1.16
1.73
J2 to I A-SM1
Segment Flow Rate (gPm)
Line Length (ft)
Line Size ID (in)5
1.078
3.426
6 Friction Headloss (ft)
0.108
0.343
Minor Losses (ft)
1.92
3.58
Line Velocity (ft/s)
Supply Force Main Elevation Delta 82
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results 4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Latera15
Elevation (ft) from Manifold to Bottom Feed Lateral5
Line Size ID (1n)5 Bottom Feed Lateral2
Friction Headloss (ft) from Manifold to
0.933
3.504
9 Total Segment Headloss (ft) = Friction + Elev.
-42.067
-46.496
Return Force Main Friction Losses
1A-RM1 to J2
—NMffljj7jM
Segment Flow Rate Wpm)
Line Length (ft)
big
Line Size ID (in.)
W6
Minor Losses from Check Valve
0.438
FNction Headloss (ft)
1.50
Line Velocity (ft1s)
J2 to J1
MEMMEN
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
1,853
FNction Headloss (ft)
3.66
Willi
Line Velocity (ft/s)
if to WWTF
MENEM
Segment Flow Rate (gpm)
I'll
Line Length (ft)
Line Size ID (in.)
KA; -,I OSSeS (ftl
n 3.782
Friction Headloss (ft) 2.03
Line Velocity Ws)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
P"! Brooks Engineering Associates, PA p.2 of 3 10/20/2008
�maii I

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

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineers Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
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.) 4.87) (Q/ )1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d 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.
A Enuals the Reauired Flush ate [DAus a Dose low Rate
Zone:
No. Laterals:
13
Tubing: ID (in)
0.79
Emitters (gph):
alA-3
0.62
Emitter Spacing ft
2
Total Footage:
7736
Design Flow (gpm
39.97
Supply Manifold Elev.
1A-SM1
Return Manifold E
1A-RM1
Run
Run
Lateral Run Elev.
Len th
1 1
69.9
2
3
4
2 5
6
7
608
8
5.4
3 9
10
11
12
4 13
14
5 15
586
16
5.3
6 17
18
7 19
20
8 21
22
9 23
606
24
5.4
10 25
26
11 27
610
28
5.5
12 29
30
13 31
604
72
74
78
79
70
73
82
81
68
es
76
153
150
155
150
153
149
148
145
148
147
147
144
148
150
150
150
149
148
146
144
3868
Ai3olication Flow (gPm):
400
Min. Design Scour Val. (ft/s)
2.0
Tubing ID (in) . - -
0.787
Residual Flow for ScourTg­p­m)�'
2.30
Req'd Flush Rate (gpm)8:
69.9
Dose
Flow (gprn�
Lateral
Length.(ft)
Lateral
Dose (gpm)
Min. Flush
Flow (9prn)
0.8
594
3.1
5.4
0.7
0.8
0.8
0.8
608
3.1
5.4
0.7
0.8
0.8
0.8
586
3.0
5.3
0.7
0.7
0.8
1.6
606
3.1
5.4
1.6
1.6
610
3.2
5.5
1.6
1.6
604
3.1
5.4
1.5
1.5
586
3.0
5.3
1.5
1.5
590
3.0
5.3
1.5
1.5
582
3.0
5.3
1.5
1.5
596
3.1
5.4
1.6
1.6
600
3.1
5.4
1.6
1.5
594
3.1
5.4
1.5
1.5
580
3.0
5.3
Brooks Engineering Associates, PA p.1 of 3 10120/2008

I
nor 4.192
Fdcflon Headloss (ft) 2.15
Line Velocity (ft1s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WVVrF
T11"I Brooks Engineering Associates, PA p.2 of 3 10/20/2008
601
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1 B-6
i
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
inputs I
Dose Flow (a)l �Flush FIOW�b)
LINE
1 Operating Head from Pump Curve' MENNESEEMEM
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unie
Line length (ft) from P.T. to H.U.5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.2
0.016
0.014
2 Total Segment Headloss (ft) Friction + Elev.
12.016
12.014
Hydraulic Unit
H.U. Elev MEW
3 Headloss from H -U (ft.)3
Supply Force Main Friction Losses
H.U. to A
Segment Flow Rate WPM)
Line Length (ft)
Line Size ID 0n)'
3.058
2.778
4 Friction Headloss (ft)
0.306
0.278
Minor Losses (ft)
2.27
2.16
Line Velocity (ft1s)
A to J3
Segment Flow Rate (gPm)
Line Length (ft)
Line Size ID Cin)5
0.081
0.278
5 Friction Headloss (ft)
0.008
0.028
Minor Losses (ft)
1.11
2.16
Line Velocity ON
J3 to 1 B -SM 1
Segment Flow Rate (gpm)
Line Length (ft)
NW=4
ff"
Line Size ID (in)5
454
6 Friction Headloss (ft)
0.142
0.445
Minor Losses (ft)
1.75
3.24
Line Velocity (ft1s)
Supply Force Main Elevation Delta
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 4
Feed Manifold to Bottom Lateral
I Igo
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Laterd
Elevation (ft) from Manifold to Bottom Feed Laterals
PIN
Line Size ID Cin)5 12
Friction Headloss (ft) from Manifold to Bottom Feed Latera
1.491
4.759
9 Total Segment Headloss (ft) = Friction + Elev.
-49.509
-53.241
Return Force Main Friction Losses
M"
1 B -RM I to J3
3475
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
3.072
Friction Headloss (ft)
-0.38
Line Velocity (ftts)
J3 to J1
Segment Flow Rate (gpm)
Line Length (ft)
100
Line Size ID (in.)
Minor Losses (ft)
0.419
Friction Headloss (ft)
2.15
Line Velocity (fits)
ii to WW-rF
Segment Flow Rate (gpm)
n"
Line Length (ft)
1000
L,-�
Line Size ID (in.)
-1 1 .. as if+%
nor 4.192
Fdcflon Headloss (ft) 2.15
Line Velocity (ft1s)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WVVrF
T11"I Brooks Engineering Associates, PA p.2 of 3 10/20/2008
601

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARYZONEIB-5
Feet
Psi
Total Headloss at Min. Flush Rate at Return Manifold
190.5
82.
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
Pressure loss required (high pressure - 60 psi)
Feet
309.9
Psi
61.2
Pressure at manifold before PRV
469.0
117.7
PRY setting calculated (pressure at manifold - pressure loss required)
154.3
66.15
PRV setting utilized
104.0
16.0
�45�O
6.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at VVWTF for Min, Flush Rate
82.3
35.6
High 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

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Ennineer'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.) 487 (Q/C)1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A Enuals the Reauired Flush ate lus he Dose low Rate
Zone: 1 B-6
No. Laterals:
10
Tubing: ID (in)
0.79
Emitters (gph):
0.62
Emitter Spacing (ft)
Req'd Flush Rate (gPm)a:
Total Footage:
51 k22
Design Flow (gpm�)�t216(.95
0.2
Supply Manifold E�ev. IB-SM2
Return Manifold E a I B-RM2
Run Run
2
3
4
5
6
7
8
2 9
10
11
12
3 13
14
4 15
16
5 17
18
6 19
20
7 21
22
8 23
24
9 25
26
10 27
11
15
19
24
31
49
55
62
62
69
79
81
102
108
113
118
123
129
131
133
136
138
140
143
145
146
83
Application Flow TV:
25.9
Min. Desi n Scour Vel . (ft/s)
2.0
Tubing ID (in) --7-776-
0.787
Residual Fl for Scour (gpm)
2.30
Req'd Flush Rate (gPm)a:
48.9
Dose
Lateral
Lateral
Min. Flush
w (gprn�
Length (ft)
Dose (gpm)
Flow (gpm)
0.1
532
2.7
5.0
0.2
0.2
0.2
0.3
0.5
0.6
0.6
0.6
582
3.0
5.3
0.7
0.8
0.8
1.1
420
2.2
4.5
1.1
1.2
462
2.4
4.7
1.2
1.3
504
2.6
4.9
1.3
1.4
528
2.7
5.0
1.4
1.4
548
2.8
5.1
1.4
1.4
566
2.9
5.2
1.5
1.5
582
3.0
5.3
1.5
0.9
298
1.5
3.8
0.7
25.9
25.9
48.9
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 1B- 6
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT Inputs [Dose Flow (a)jF1u.=h =Flow(b)
LINE
I Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unie
Line length (ft) from P.T. to H -U-5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev MIM
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
0.016 0.014
12.016 12.014
H.U. to A
w1affiffilmn
Segment Flow Rate (gPm)
Line Length (ft)
MW
Line Size ID (In)"
3.058
2.778
4 Friction Headloss (ft)
0.306
0.278
Minor Losses (ft)
2.27
2.16
Line Velocity (ft/s)
A to J4
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
0.597
2.042
5 Friction Headloss (ft)
0.060
0.204
Minor Losses (ft)
1.11
2.16
Line Velocity (ft/s)
J4 to 1 B-SM2
25.9
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID OnP
0.324
1.047
6 Friction Headloss (ft)
0.032
0.105
Minor Losses (ft)
1.13
2.13
Line Velocity (fUs)
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
Elm
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed LateraI5
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera 12
0.280
1.519
9 Total Segment Headloss (ft) = Friction + Elev.
-24.720
-30.481
Return Force Main Friction Losses
I B-RM2 to J4
Segment Flow Rate (gpm)
Line Length (ft)
185
Line Size ID (in.)
Minor Losses from Check Valve
- -
5.983
Friction Headloss (ft)
3.63
Line Velocity (flfs)
J4 to A
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
1 178
Friction Headloss (ft)
,
1.28
Line Velocity (ft1s)
A to VVWTF
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
�A; I -sses fff%
nor 4.192
Friction Headloss (ft) 2.15
Line Velocity Ws)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3 10/2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE I 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
A64.3
201.0
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
273.7
Psi
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
115.5
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 10120/2008

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.) 4 (Q C)i 85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A Eauals the Reauired Flush ate plus the Dose Flow Rate
Izone: T 3A-7
No L8 aL
18
:�.t __
,!.eL
in ID �,n)
0.79
Emitters (gph):
0.62
ErnitterS acin
Ren'd Flush Rate (.QPm)':
Total Footage:
9620
Desion Flow (gipm):
49.70
Supply Manifold Elev. 3A-SM1
Return Manifold 3A-RM1
Run Run
f. -I Pm Flpv� Lenath #
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
Ap lication Flow (gpm):
49.7
Min. Design Scour VeL
2.0
Tubing ID (in)
0.787
a
Residual Flow for Scour (gpm
2.30
Ren'd Flush Rate (.QPm)':
91.1
Dose Lateral Lateral Min. Flush
2
3
4
5
6
"M
7
8
1 Vt,"
9
10
12
13
14
16
5 41 ""@Y' I
17
18
19
6
20
ff'W"
21
'R- -E"'i
22
23
24
U
25
A, 1,
26
'X;
27
28
N
29
30
31
32
33
34
35
36
37
38
39
AT
Z�'
378
432
448
462
476
494
540
552
558
564
580
588
594
600
600
600
600
2.0
2.2
2.3
2.4
2.5
2A
2.8
2.9
2.9
2.9
3.0
3.0
3.1
3.1
3.1
3.1
3.1
4.3
4.6
4.6
4.7
4.8
4.9
5.1
5.2
5.2
5.2
5.3
5.3
5.4
5.4
5.4
5.4
5.4
Brooks Engineering Associates, PA p.1 of 3 11/18/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3A-7
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
211.2
91.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
287.8
124.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
409.1
177.1
Flush Pressure at backwash tank for Min. Flush Rate
470.1
203.5
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
270.5
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
115.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
34.5
14.9
Flush Pressure at WWTF for Min. Flush Rate
1 21 ' 5
526
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
143.6
62*i_j
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 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
I 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.) 4.17) (Q/C)1.81
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
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 Eauals the Required Flush Rate plus the Dose Flow Rate
Zone: 3A-8
No. Laterals:
8
Tubing: ID (in)
0.79
Emitters (gph):
0.62
Emitter Spacing (ft)
2
Total Footage:
4148
Design Flow (gpm):
21.43
Application Flow (gpm):
Min. Design Scour Val. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scou�_(_gpmr
2.30
Req'd Flush Rate (gpm)6:
Supply Manifold E ev.
2ev.
3A -SMI
Return Manifold
3A -RM 1
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Length
# Emitters
Flow (gpM)7
Length (ft)
Dose(gpm)
Flow (gpm)8
1 1
16
0.2
510
2.6
4.9
2
17
0.2
3
19
0.2
4
21
0.2
6
24
0.2
6
26
0.3
7
29
0.3
8
311
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
27
60
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
SUMMARY ZONE 3A-8
Zbl.o
01.
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
218.2
94.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
280.8
121.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
400.1
173.2
Flush Pressure at backwash tank for Min. Flush Rate
463.1
200.5
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
Zbl.o
01.
Pressure at manifold before PRV
469.9
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154�3
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
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
I 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.) 4.17) (Q/C)1-111
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d
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: 1113-9
No. Laterals:
3
Tubing: ID (in)
0.79
Emitters (gph):
0.62
Emitter Spacing (ft)
2
Total Footage:
1358
Design Flow (glarn):
7.02
Supply Manifold Elev.
1 B-SM3
Return Manifold E
1 B-RM3
Run
Run
Lateral Run Elev.
Lenath
1 1
�.q
13.9
2
3
4
2 5
6
3 7
470
8
4.7
9
10
Application Flow (gpm):
7.0
Min. Design Scour Val. (ft1s)
2.0
Tubing ID (in)
0.787
a2.3
Flow for Sc�
0
.Residual
Req'd Flush Rate (gpm)':
�.q
13.9
Dose
mitters Flow (gpm)7
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (9prr)
I 1 0.1
398
2.1
4.4
16 0.2
89 0.9
83 0.9
82 0.8
470
2.4
4.7
153 1.6
70 0.7
490
2.5
4.8
67 0.7
58 0.6
50 0.5
7.0
13.9
Brooks Engineering Associates, PA P. 1 of 3 10120/2008

-Aj
I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
F"
ZONE 1113-9
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
Inputs I Dose Flow fall Flush Flow (b)
1 Operating Head from Pump Curve'
JW
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic UnIt5
Line length (ft) from P.T. to H.U.'
M
Line Size ID (in)
Friction Headloss (ft) from Pump to H U.2
0.016
0.014
2 Total Segment Headloss (ft) Friction + Elev.
12.016
12.014
Hydraulic Unit
H.U. Elev EMM
3 Headloss from H.0 (%)3
Supply Force Main Friction Losses
H.U. to J3
Segment Flow Rate (gpm)
01MEMMEM
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
J3toJ4
Segment Flow Rate (gpm)
EMMEMEINNEM
Line Length (ft)
Line Size ID (in)s
5 Friction Headloss (ft)
0.503
0.620
Minor Losses (ft)
0.060
0,062
Line Velocity (ft/s)
1.11
1.24
J4 to 1 B-SM3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size I D (in)s
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
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold 4
Feed Manifold to Bottom Lateral
4
1 J4
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Laterar
Elevation (ft) from Manifold to Bottom Feed LateraI5
Line Size ID (Inf
Friction Headloss (ft) from Manifold to Bottom Feed LateraI2
0.769
2.642
9 Total Segment Headloss (ft) = Friction + Elev.
-18.231
-23.458
Return Force Main Friction Losses
Fig
1 B-RM3 to J4
Segment Flow Rate (gpm)
61
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
0.394
Line Velocity (ft1s)
0.66
J4 to A
Segment Flow Rate (gpm)
milmim
Line Length (ft)
Line Size ID (in.)
!
Minor Losses (ft)
A
Friction Headloss (ft)
0.993
Line Velocity (ft/s)
1.28
J I to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
A
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
"I Brooks Engineering Associates, PA p.2 of 3 10/20/2008
1 Ldiii

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 1 B-9
PSI
Ti.2
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
142.9
61.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
357.1
154.6
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
441.9
191.3
Flush Pressure at backwash tank for Min. Flush Rate
450.7
195.1
PRV NEEDED? YES
ZONE SUMMARY W1 PRV Feet
Pressure loss required (high pressure - 60 psi) 303.3
PSI
Ti.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
5&0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
59.1
25.6
Flush Pressure at WVVTF for Min. Flush Rate
107.1
46.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
138.3
59.9
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.) 4-87) (Q/C)1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A Enuals the Reouired Flush Rate plus the Dose Flow Rate
Zone:
No. Laterals:
Design Sco6(rVel. (fVs)
Tubing: ID (in)
0.79
Emitters (gph):
;ffi4
0.62
Emitter Spacing ft
2
Total Footage:
1992
Design Flow (gp m
10. 9
10.29
ication Flow pm):
10.3
Design Sco6(rVel. (fVs)
2.0
Tubing ID (in)
- 0,787
Residual Flow for Scour (opm)'
2.30
Req'd Flush Rate (gpmf..
19.5
Supply Manifold Elev.
I B-SM3
Return Manifold E
Run
I B-RM3
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Len th
# Emitters Flow (gpM)7
Length (ft)
Dose (gpm)
Flow (gpm)
1 11
73 0.8
604
3.1
5.4
12
73 0.8
13
76 0.8
14
80 0.8
2 15
74 0.8
600
3.1
5.4
16
72 0.7
17
73 0.8
18
81 0.8
3 19
96 1.0
386
2.0
4.3
20
97 1.0
4 21
99 1.0
402
2.1
4.4
22
102 1.1
1 nnq
oar in.14
10.3
19.5
Brooks Engineering Associates, PA p.1 of 3 11118/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE IB -10
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
I 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.5
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.2
2 Total Segment Headloss (ft) = Friction + Elev.
0.016 0.014
12.016 12.014
p.2 of 3
Brooks Engineering Associates, PA
11/18/2008
Hydraulic Unit
H.U. Elev ME=
3 Headloss from H. U (ft.)3
Supply Force Main Friction Losses
H.U. to J3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in )5
3.373
3.056
4 Friction Headloss (ft)
0.337
0.306
Minor Losses (ft)
2.27
2.16
Line Velocity (ft/s)
J3 to J4
Segment Flow Rate (gpm)
Allu
Line Length (ft)
Line Size I D (in)s
0.503
0.620
ram
5 Friction Headloss (ft)
0.050
0.062
Minor Losses (ft)
1.11
1.24
Line Velocity (ft/s)
J4 to 1 B-SM3
Segment Flow Rate (gpm)
Line Length (ft)
MW
Line Size ID (in)5
6 Friction Headloss (ft)
Minor Losses (ft)
0.071
0.007
0.231
0.023
1.01
1.91
Line Velocity (ft/s)
r17
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold MINEEMEWEE
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold'
Line Length (ft) from Supply Manifold to Bottom Feed Latera 15
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID (in)5
2
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)
Line Length (ft)
50
Line Size I D (in.)
wwr��
Minor Losses from Check Valve
0.394
Friction Headloss (ft)
0.88
Line Velocity (ft/s)
J4 to A
Segment Flow Rate (gpm)
Line Length (ft)
620
Line Size ID (in.)
MW
Minor Losses (ft)
0.993
Friction Headloss (ft)
1.28
Line Velocity (ft/s)
A to WWTF
�1
Segment Flow Rate (gpm)
Line Length (ft)
Willi
Line Size ID (in.)
WC
Minor Losses (ft)
4 6`1
Friction Headloss (ft)
2.15
Line Velo(:ity (ft/s)
: WIN i
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
p.2 of 3
Brooks Engineering Associates, PA
11/18/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 1B-10
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
162.9
70.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
337.1
145.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
434.1
187.9
Flush Pressure at backwash tank for Min. Flush Rate
430.7
186.5
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
ztl .0
. I..
Pressure at manifold before PRV
469.6
154.3
117.7
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
PRV setting utilized
127.1
39.1
16.9
Low Pressure Check: P at Min. Flush Flow at Return Manifold
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
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
I 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.) 4-87) (QIC)1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
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 I th Re uired Flush Rate plus the Dose Flow Rate
one'- 2A-12
L-Lf�
No. Laie-ral;_..
L s'
15
ID in
Tubin : ID 'n
0.79
h
Emitters h
0
0.62
.
S a_n ft
Emitter S acin
2
ota a
Total Foote a:
7962
Design Flow (gpm):
'+ 1. 1-+
Supply Manffold E ev.
ev. I= 2A-SMl
Return Manifold 2 2A-RM1
Run Run
Lateral Run Elev. L th
I I Nia
2
9
4
5
6
7
8
9
10
11
12
13
14
15
2
3
4
7
8
9
10
11
12
13
14
15
16
17
is
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
7
9
11
14
18
48
53
59
64
66
68
70
71
74
73
77
72
72
74
80
96
100
104
108
ill
115
119
123
127
132
135
139
143
147
152
150
150
150
150
150
150
Applicatio Flow (9pn1):
41.1 -
Min. Design Scour Val. (ft/s)
Z�u
Tubing ID (in)
0.787
Residual Flow for Scour (�p_mf
2.30
Rea'd Flush Rate (gpm)5: -
75.6
Dose Lateral
N (gpM)7 Length.
0.1 438
0.1
0.1
0.1
0.2
0.5
0.5
0.6
0.7 536
0.7
0.7
0.7
0.7 590
0.8
0.8
0.8
0.7 596
0.7
0.8
0.8
1.0 392
1.0
1.1 424
1.1
1.1 452
1.2
1.2 484
1.3
1.3 518
1.4
1.4 548
1.4
1.5 680
1.5
1.6 604
1.6
1.6 600
1.6
1.6 600
1.6
1.6 600
Lateral Min. Flush
2.8 5.1
3.0 5.3
3.1 6.4
2.0 4.3
2.2 4.5
2.3 4.6
2.5 4.8
2.7 5.0
2.8 5.1
3.0 5.3
3.1 5.4
3.1 5.4
3.1 5.4
3.1 5.4
-41.1 75.(
Brooks Engineering Associates, PA p.1 of 3 10120/2008

0
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 2B-14
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
I Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unle
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H U.2
2 Total Segment Headloss (ft) = Friction + Elev.
I Inputs Lb �—se Flow ja)1 Flush Flow JbI,
0.017 0.016
12.017 12.016
Hydraulic Unit
H.U. Elev REM
3 Headloss from H.0 (ft.)3 Ruffiliffimmom
Supply Force Main Friction Losses
H.U. to A
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID Qn)r'
4 Friction Headloss (ft)
3.301
3.178
Minor Losses (ft)
0.330
0.318
Line Velocity (ft1s)
2.37
2.32
J1 to J7
Segment Flow Rate (gpm)
Line Length (it)
Line Size ID (in)6
6.919
6.662
5 Friction Headloss (ft)
0.692
0.666
Minor Losses (ft)
Line Velocity (ft/s)
2.37
2.32
J7 to 2B-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (In)5
6 Friction Headloss (ft)
0.342
1.303
Minor Losses (11)
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
Drip System Headloss Results
4
a Total Headloss (ft.) in drip system from supply manifold to return manifold
now
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 Lateral5
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral�
1.578
4.726
9 Total Segment Headloss (ft) = Friction + Elev.
-22.422
-26.274
Return Force Main Friction Losses
2B-RM1 to J7
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
1,551
Line Velocity (ft/s)
2.03
J7 to A
Segment Flow Rate (gpm)
Line Length (ft)
20 1 96
Line Size ID (in.)
Minor Losses (ft)
7.928
Friction Headloss (ft)
Line Velocity (ft/s)
2.03
it to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
Wjif���
Minor Losses (ft)
-
3.782
Friction Headloss (ft)
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
i�
10/20/2008

j,
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 2A-16
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE I Inouts I Dose Flow
I operating Head from Pump Curve' I is
ft��
4da
Pump Tank to H. U.
Elevation (ft) from Pump to Hydraulic Unle
Line length (ft) from P.T. to H.U.5
Line Size ID (in)
2
Friction Headloss (ft) from Pump to H.U.
0.017
0.016
2 Total Segment Headloss (ft) Friction + Elev.
12.017
12.016
Hydraulic Unit
H.U. Elev MINN
liffim
3 Headloss from H, U (ft.)3
Supply Force Main Friction Losses
H.U. to J1
Segment Flow Rate (gpm)
Line Length (ft)
Me=
Line Size ID (in)'
4 Friction Headloss (ft)
0.330
0.311
Minor Losses (ft)
2.37
2.29
Line Velocity (fVs)
A to J7
Segment Flow Rate (gpm)
REWHEEMEEM
Line Length (ft)
Line Size ID 0n)'
6.919
6.512
5 Friction Headloss (ft)
0.692
0.651
Minor Losses (ft)
2.37
2.29
pk%�
Line Velocity (fVs)
J7 to 2A-SM1
'rAj
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)
0.165
0.513
6 Friction Headloss (ft)
0.017
0,051
Minor Losses (ft)
1.24
2.29
Line Velocity (ftfs)
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
MENIMEM
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)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
0.648
3.049
9 Total Segment Headloss (ft) Friction + Elev.
-51.352
-55.951
Return Force Main Friction Losses
2A-RM1 to J7
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
0.692
Friction Headloss (ft)
2.15
Line Velocity (fUs)
J7 to A Segment Flow Rate (Qpm)
ONIMM
Line Length (ft)
68d
Line Size ID (in.)
Minor Losses (ft)
8.786
Friction Headloss (ft)
2.15
Line Velocity (ft1s)
J1 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
1000
Line Size ID (in.)
Minor Losses (ft)
4,192
Friction Headloss (ft)
2.15
Line Velocity (fVs)
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
10/20/2008
Brooks Engineering Assodlates, PA p.2 of 3

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARYZONE -15
set
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
ZONE SUMMARY W/ PRV
Feet
Psi
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
-"",�45.0' ,
Low Pressure Check: P at Min. Flush Flow at Return Manifold
15.0
6.6
Flush Pressure at WWTF for Min. Flush Rate
159.3
69.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
1482
64.2
Brooks Engineering Associates, PA P.3 of 3 10/20/2008

I
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:
Lateral
all emitters operate between 7 and 70 psi,
Len th # Emitters Flow (-N?
--th Ift)
there is sufficient pressure to return the flush to the Hydraulic Unit,
1
a flushing flow velocity of 2 ft/s is provided.
89
2. The source of either the calculations or the data inputs are indicated In the footnotes.
368
3. The
inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
I From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
95
(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 4,87) (QIC)I."
3
From Wastewater Systems Inc. Data
95
4
Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
2.0
5
From Engineering Drawings
4
6
Calculated from Q = VA
7
Equals the # of emitters in the run times the individual emitter flow rate in gpm.
3
8
E ual, the R uired Flush Rate pWhe Dose low Rate
1.0
408
2.1
213-16
plication Flow (opm):
67.
1.1
L. 26
Min. Design Scour Val. (fVs)
7
110
1.1
Tubln 11 in 0.79
2.3
-ijbing ID (in)
8
114
Emitters h 0.62
WF
S
!2,�ivall' afor Scour (gionn)
5
9
Emitter S adin ft 2
1.2
(gpin)'
2.4
4.7
Total Foote a: 13132
119
1.2
, M 67.85
Desi n -1
6
11
122
Supply Manifold Elev. I= 2B-SM1
494
2.6
Return Manifold Elev. 2B-RM1
Run Run Dose Lateral Lateral
Min. Flush
Lateral
Run Elev.
Len th # Emitters Flow (-N?
--th Ift)
-
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
1 6
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
I 1
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
W
'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
M
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
24
0.2
:10
24
0.2
13132 5566
WX
67.8
127.6
Brooks Engineering Associates, PA p.1 of3 10/2012008

I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
�Ao
ZONE2B46
TOP LOAD MANIFOLD PRESSURE ANALYSIS
LAW INPUT
LINE Inputs Dose Flow W1 Flush Flow jbil
1 0 erating Head from Pump Curve' RIENNEIMEMMEM
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Units
Line length (ft) from P,T. to H.U.6
Line Size ID Cin)
Friction Headloss (11) from Pump to H.U.,
0.017
0.016
2 Total Segment Headloss (ft) Friction Elev.
12.017
12.016
Hydraulic Unit
H.U. Elev INUM
3 Headloss from H.0 (ft.)
EMEM
Supply Force Main Friction Losses
H.U. to A
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)s
3.301
3.178
4 Friction Headloss (ft)
0.330
0.318
Minor Losses (ft)
2.37
2.32
Line Velocity (ft/s)
A to J7
Segment Flow Rate (gpm)
KNIERMEMMEM
Line Length (ft)
Line Size ID (in)'
6.919
6.662
5 Friction Headloss (ft)
0.692
0.666
Minor Losses (ft)
2.37
2.32
Line Velocity (ft1s)
J7 to 2B -SMI
Segment Flow Rate (gpm)
offlummimm
Line Length (ft)
Line Size 10 (in)'
a F(Iction 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
Drip System Headloss Results 4
Total Headloss (ft.) in drip system from supply manifold to return manifold
8
Feed Manifold to Bottom Lateral
4
Headloss (ft) in manifold
Une, Length (ft) from Supply Manifold to Bottom Feed Latera is
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)6
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 -RM I to J7
Segment Flow Rate (gpm)
Une Length (ft)
Line Size 10 (in.)
Minor Losses from Check Valve
1.551
Friction Headloss (ft)
2.03
Line Velocity (1`11s)
J7 to A
MIRIAM
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
7.928
Foction Headloss (ft)
2.03
Line Velocity (fUs)
it to VVWrF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft) 3.782
Line Velocity ON 2.03
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF Em�
Brooks Engineering Associates, PA p2 of 3
10/2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARYZONE21346 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 1941 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 W/ 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
45.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
14.0
6.0
Flush Pressure at VVWTF for Min. Flush Rate
180.7
78.2
1 High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
150.2
65.0
Brooks Engineering Associates, PA P.3 of 3 10/2012008

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.) 487) 85
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.
A Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 4A-17
No. Laterals:
7
Tubing: ID (in)
0.79
Emitters (gph):
0.6 -2 -
Emitter Spacing (ft)
2
Total Footage:
3664
Design Flow (gpm):
18.93
Supply Manifold E ev. 4A-SM1
Return Manifold E:ev 4A -RM 1
Run Run
f-1 Pm Rev- Lenath #
2
3
4
2
3
10
4 11
12
13
14
6 15
16
7 FBI=
Application Flow (9prn):
18.9
Min. Design Scour Vel. (ftfs)
2.0
Tubing ID (in)
0.787
a2.3
Residual Flow for Scour (opm)'
0
Req'd Flush Rate (gp��) :
� 0
35.0
Dose Lateral Lateral Min. Flush
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
1113
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
1QQ
189
35.0
Brooks Engineering Associates, PA p.1 of 3 10120/2008

PRESSURE ANALYSIS
1 44 TOP FEED MANIFOLD SYSTEM
ZONE 4A-17
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE I —np
1 —ODeratina Head from Pump Curve' ults I Dose Flow I
H.U. To ilu
Segment Flow Rate (gPm)
Numlifflifflomm
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 (ft1s)
1.51
2.30
J20 to J1 1
Segment Flow Rate (gPm)
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 (ft1s)
1.37
2.07
J1 1 to 4A -SMI
Segment Flow Rate Wpm)
090UPINIMM
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 (ft1s)
1.24
2.34
Supply Force Main Elevation Delta
Manifold
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
4
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Lateral5
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.831
5.139
9 Total Segment Headloss (ft) = Friction + Elev.
-12.169
-15.861
Return Force Main Friction Losses
4A-RM1 to A 1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
1.871
Line Velocity (ft1s)
2.41
,111 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
6.072
Line Velocity fts)
2.26
J20 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (ft1s)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3 10/20/2008

LAO
I ww 1
1 61� 1
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4A-17
Feet
112.0
PSI
51.2
Feet
psi
Total Headloss at Min. Flush Rate at Return Manifold
357.3
1547
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
ZONE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 psi)
Feet
112.0
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 O��'�
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
I High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
143.8
62.2
Brooks Engineering Associates, PA
p.3 of 3
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Enalneer'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
I From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d'-87) (Q/C)"8'
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 (gph):
0.62
Emitter Spacing (ft)
2
Total Footage:
1872
Design Flow (gpm):
9.67
Supply Manifold E ev. 4A-SM1
Return Manifold E�e 4A-RM1
Run Run
2
3
4
8
9
Application Flow (gpm):
9.7
Min. Design Scour Vel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour
2.30
Rea'd Flush -Rate (gpm)8:
18.9
Emitters
24
27
27
65
63
86
104
100
97
93
89
79
46
36
�RV
Dose
Lateral
Lateral
Min. Flush
N (gpM)7
Length (ft)
Dose (gpm)
Flow (gpm)
0.2
584
3.0
5.3
0.3
0.3
0.7
0.7
0.9
1.1
408
2.1
4.4
1.0
1.0
380
2.0
4.3
1.0
0.9
500
2.6
4.9
0.8
0.5
Brooks Engineering Associates, PA p.1 of 3 10/2012008

I W"i i
I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 4118
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unie
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.2,
2 Total Segment Headloss (ft) = Friction + Elev.
Brooks Engineering Associates, PA p.2 of 3 10/20/2008
Hydraulic Unit
H.U. Elev so=
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 I D (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)
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 1 to 4A-SM1
Segment Flow Rate (gpm)
Line Length (ft)
"Pip,
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
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold4 kwwafflvffilx�
FINJ
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold 4
Line Length (ft) from Supply Manifold to Bottom Feed Lateral5
Elevation (ft) from Manifold to Bottom Feed Lateral5
Line Size ID (in)5
Lai
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.323
4.297
9 Total Segment Headloss (ft) = Friction + Elev.
-12.677
-16.703
Return Force Main Friction Losses
4A -RMI to A 1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
1.871
Line Velocity (ft1s)
2.41
J1 I to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size I D (in.)
Minor Losses (ft)
Friction Headloss (ft)
6.072
Line Velocity (ft/s)
2.26
J20 to WWTF
Mffl�
Segment Flow Rate (gpm)
;
I !!
Line Length (ft)
64
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (ft/s)
2.26
ww I
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WVVTF
Brooks Engineering Associates, PA p.2 of 3 10/20/2008

LWW01
A
I Llj� I
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
Low Pressure Check: P at Min. Flush Flow at Return Manifold
55.6
24.i
Flush Pressure at WVTrF for Min. Flush Rate
264.5
114.5
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
144.3
1 62.5
Brooks Engineering Associates, PA
p.3 of 3
10/20/2008

I um�
L4
i 64 1
V q
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Ennineer'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
I 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)'-"
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
4A-SM3
Application Flow (gpm): 22.2
No. Laterals: 8
Min. Design Scour Vel. (ft/s) 2.0
Tubing: ID (in) 0.79
Return Manifold Elev.
Tubing ID (in) 0.787
Emitters (gph): 0.62
Residual Flow for Scour (gpm)' 2.30
Emitter Spacing (ft) 2
Req'd Flush Rate (gpm)': 40.6
Total Footage: 4288
Design Flow (gpm): 22.15
Lateral
Supply Manifold Elev.
4A-SM3
Return Manifold Elev.
4A-SM3
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Lenqth
# Emitters
Flow (gpM)7
Length (ft)
Dose(gpm)
Flow (gpm)e
1 1
98
1.0
398
2.1
4.4
2
101
1.0
2 3
135
1.4
540
2.8
5.1
4
135
1.4
3 5
136
1.4
544
2.8
5.1
6
136
1.4
4 7
137
1.4
548
2.8
5.1
8
137
1.4
5 9
1
1 37
1.4
548
2.8
5.1
10
137
1.4
6 111
139
1.4
558
2.9
5.2
12
140
1.4
7 13
141
1.5
568
2.9
5.2
14
143
1.5
8 15
145
1.5
584
3.0
5.3
16
1 47
1.5
4288
2144
22.2
22.2
40.6
Brooks Engineering Associates, PA
P.1 of3
10120/2008

I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
ZONE 4A-20
TOP LOAD MANIFOLD PRESSURE ANALYSIS
Line Length (ft)
ffm
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
4 Friction Headloss (ft)
Elevation (ft) from Pump to Hydraulic Unie
5.061
Line length (ft) from P.T. to H.U.'
Minor Losses (ft)
Line Size ID (in)
0.506
Friction Headloss (ft) from Pump to H U.2
a
2 Total Segment Headloss (ft) = Friction + Elev.
1.51
Hydraulic Unit
J20 to J1 3
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)
ffm
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 J1 3
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
J 13 to 4A-SM3
Segment Flow Rate (gpm)
KAWWWWWROW—M
Line Length (ft)
Ku
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
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 4
Line Length (ft) from Supply Manifold to Bottom Feed LateraI6
Elevation (ft) from Manifold to Bottom Feed Latera15
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 J 13
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
3.531
Line Velocity (ft/s)
2.90
J13 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.228
Line Velocity (ft1s)
2.26
J20 to WWTF
Segment Flow Rate (gpm)
W&WHO
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (ft1s)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
77 i Brooks Engineering Associates, PA p.2 of 3 10/2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 4A-20
43.5
51.2
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
418.8
181.Y—
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
Pressure loss required (high pressure - 60 psi)
43.5
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
60.6
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
LAI
Brooks Engineering Associates, PA p,2 of 3 10/20/2008
Wki
ZONE 5A-21
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
Inputs I Dose
Flow (a)l
Flush Flow
I Operating Head from Pump Curve'
NNINAIMIN1111am
jbj
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.2
0.015
0.0114
2 Total Segment Headloss (ft) Friction + Elev.
12.015
12.014
Hydraulic Unit
H.U. Elev NEW
3 Headloss from H. U (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
9.784
Minor Losses (ft)
1.051
0.978
fqoq
Line Velocity (ft1s)
2.25
2.16
J20 to J14
Segment Flow Rate (gpm)
NERMIMMIM
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
6.094
5.675
Minor Losses (ft)
0.609
0.567
Line Velocity (ft/s)
2.03
1.95
J14 to 5A-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
6 Friction Headloss (ft)
0.572
1.685
Will!
Minor Losses (ft)
0.057
0.169
Line Velocity (ft1s)
1.51
2.71
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold4
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
1.865
5.193
9 Total Segment Headloss (ft) = Friction + Elev.
-12.135
-15.807
Return Force Main Friction Losses
5A -RMI to J14
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
2.550
Line Velocity (ft/s)
2.64
J14 to J20
Segment Flow Rate (gpm)
110-0-5m
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
12.060
Line Velocity (ft/s)
2.26
J20 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
16.186
Line Velocity (fUs)
2.26
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WVVTF
Brooks Engineering Associates, PA p,2 of 3 10/20/2008
Wki

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 5A-21
44.6
51.2
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
416,2
180.2
Low Pressure Check: P at Min. Flush Flow at Return Manifold
83.8
36.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
183.2
79.3
Flush Pressure at backwash tank for Min. Flush Rate
623.5
269.9
PRV NEEDED? YES
Pressure loss required (high pressure - 60 Psi)
44.6
51.2
Pressure at manifold before PRV
455.1
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
48.6
21.0
Flush Pressure at WWTF for Min. Flush Rate
305.8
132.4
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
143.7
62.2
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.) 487) (Q/c)1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
A Equals the Required Flush Rate plus the Dose Flow Rate
n SA -22
0 0*
.':i
No. L. erali..
K2 f -
7
Tubin ID in
079
"-
Emitters (Qph):
0.62
Emitter S adin ftt
2
Total Foot. a.
3 722
Design Flow (gpm):
19.23
Supply Manifold E ev.
Return Manifold 2ev-
Run
Lateral Run Elev.
5A-SM`1
5A-RM1
Run
Len th
# Ernitte
1 1
Tubing ID (in)
23
2
2.30
27
3
2.7
44
4
47
5
0.5
55
6
61
2
68
0.6
70
0.6
80
83
3
3.1
74
12
77
13
0.8
79
14
82
4 15
75
16
624
77
17
0.8
56
18
59
6 19
59
20
61
21
0.8
59
22
5.1
59
7 23
59
24
59
25
0.6
60
26
60
8 27
2.5
61
28
62
29
0.6
62
�Lp�ation Flow Opm):
19.2
Min. Design Scour Vel. (ft1s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour Opm?
2.30
d Flush Rate (g
T.�-RMt�
35.3
Dose
Lateral
Lateral
Min. Flush
,V (gpM)7
Length (ft)
Dose (gpm)
Flow (gpm
0.2
514
2.7
5.0
0.3
0.5
0.5
0.6
0.6
0.7
602
3.1
5.4
0.7
0.8
0.9
0.8
624
3.2
5.5
0.8
0.8
0.8
0.8
534
2.8
5.1
0.8
0.6
0.6
0.6
476
2.5
4.8
0.6
0.6
0.6
0.6
476
2.5
4.8
0.6
0.6
0,6
0.6
496
2.6
4.9
0.6
0.6
0.7
19.2
19.2
35.3
Brooks Engineering Associates, PA p. I of 3 10/20/2008

-1
ZONE SA -22
TOP LOAD MANIFOLD PRESSURE ANALYSIS
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
-A Brooks Engineering Associates, PA p.2 of 3 1012012008
INPUT
inputs
LINE
I — 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 EMM
3 Headloss from H.Ll (ft.)3
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
10.507
9.784
4 Friction Headloss (ft)
1.051
0.978
Minor Losses (ft)
2.25
2.16
Line Velocity (ft/s)
J20 to J14
Segment Flow Rate (gpm)
Line Length (ft)
la=6
Line Size ID (in)s
676
5 Friction Headloss (ft)
0.609
0.567
Minor Losses (ft)
2.03
1.95
Line Velocity (ft1s)
J14 to 5A-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
2=1
.685
6 Friction Headloss (ft)
0.057
0.169
Minor Losses (ft)
1.51
2.71
Line Velocity ON
P"
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
4
MUM
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 Lateral5
Line Size ID (in)s
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.303
4.263
9 Total Segment Headloss (ft) = Friction + Elev.
-25.697
-29.737
Return Force Main Friction Losses
5A-RM1 to J1 4
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
2.550
Friction Headloss (ft)
2.64
Line Velocity (ft/s)
J14 to J20
Segment Flow Rate (gpm)
Line Length (ft)
rr,
Line Size ID (in.)
aw
Minor Losses (ft)
12.060
Friction Headloss (ft)
2.26
Line Velocity (fUs)
J20 to WWTF
Segment Flow Rate (gpm)
-
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
16.186
Friction Headloss (ft)
2.26
Line Velocity (ft/s)
: LWO
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
-A Brooks Engineering Associates, PA p.2 of 3 1012012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 5A-22
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
419.2
181.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
80.8
35.0
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
196.8
85.2
Flush Pressure at backwash tank for Min. Flush Rate
620.5
268.6
PRV NEEDED? YES
ZONE SUMMARY W1 PRV
Pressure loss required (high pressure - 60 psi)
Feet
58.2
PSI
51.2
Pressure at manifold before PRV
455.1
154.3
117.7
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
PRV setting utilized
138.6
45.6
19.7
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at WWTF for Min. Flush Rate
302.8
131.1
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
157 R
68.1
Brooks Engineering Associates, PA
p.3 of 3
10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineers Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
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
I 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.) hf = (4.727 U d 4.87) (Q/C)1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation:
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.
Ft E I th Re uhred Flush Rate plus the Dose Flow Rate
K. 6A'23
" '
11
Tubing: ID (in
0.79
Emitters h
0.62
Emitter Spacing ft
2
Total Footage7
4784
Design Flow (APrn):
24.72
Supply Manifold E ev.
2e
24.7
5A-SM2
Return Manifold
Tubing ID (in)
5A-RM2
Residual Flow for Scour (gpm)
Run
Run
Lateral Run Elev.
Len th #
1
6
Applicatio Flow (gpm):
24.7
Min. Design Scour Val. (ft/s)
2.0
6
Tubing ID (in)
0.787
a2.3O
Residual Flow for Scour (gpm)
0
�eq'd Flush Rate (gpm)':
50.0
Dose Lateral Lateral Min. Flush
N (gpM)7 Length (ft) Dose (gpm) Flow (9pM
n Ft sno 3.1 5.4
392
70
0.7
384
69
0.7
376
88
0.9
2 5
98
1.0
6
98
1.0
3 7
96
1.0
8
96
1.0
4 9
94
1.0
10
94
1.0
5 11
94
1.0
12
93
1.0
6 13
92
1.0
14
91
0.9
7 is
110
'11
16
112
1.2
8 17
109
1.1
18
105
1.1
9 '19
103
1.1
20
102
1.1
10 21
100
1.0
22
99
1.0
11 23
88
0.9
24
85
0.9
25
70
0.7
qa
63
0.7
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 10120/2008

�A
PRESSURE ANALYSIS
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 U.2
2 Total Segment Headloss (ft) = Friction + Elev.
Inouts �e Figgw (all Flush Flow (b
MOOMMMMM
0.015 0.014
12.015 12.014
N
I
I
Drip System HeadlosS Results 4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
I I i
Feed Manifold to D—orn a era
Headloss (ft) in manifold 4
Line Length (ft) from Supply Manifold to Bottom Feed Lateral,
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID (in)r
Friction Headloss; (ft) from Manifold to Bottom Feed Lateral2
Total Segment Headloss (ft) = Friction + Elev.
Return Force Main Friction Losses
5A-RM2 to J 15
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
Line Velocity (ft/s)
J15 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft1s)
J20 to VVWTF
Segment Flow Rate (gPm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
i; n It
meturn Line Eleva on e a
Elevation (ft) from Return Manifold to WWTF
1.923 5.286
-19.077 -22.714
p.2 of 3 10/20/2008
Brooks Engineering Associates, PA
Hydraulic Unit
-h
H.U. Elev Emw
3 Headloss from H.0
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
r"
Line Length (ft)
Line Size ID (in)s
9.784
4 Friction Headloss (ft)
1.051
0.978
Minor Losses (ft)
Line Velocity (ft/s)
2.25
2.16
J20 to J15
Segment Flow Rate (gpm)
Line Length (11)
Line Size ID (in)5
6.678
6.218
5 Friction Headloss (ft)
0.668
0.622
Minor Losses (ft)
Line Velocity (ft/s)
2.03
1.95
J 15 to 5A-SM2
Segment Flow Rate (gpm)
mass=
Line Length R
Line Size ID (in)5
0.391
1.348
6 Friction Headloss (ft)
0.039
0.135
Minor Losses (ft)
Line Velocity (ft/s)
1.46
2.85
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
N
I
I
Drip System HeadlosS Results 4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
I I i
Feed Manifold to D—orn a era
Headloss (ft) in manifold 4
Line Length (ft) from Supply Manifold to Bottom Feed Lateral,
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID (in)r
Friction Headloss; (ft) from Manifold to Bottom Feed Lateral2
Total Segment Headloss (ft) = Friction + Elev.
Return Force Main Friction Losses
5A-RM2 to J 15
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
Line Velocity (ft/s)
J15 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft1s)
J20 to VVWTF
Segment Flow Rate (gPm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
Line Velocity (ft/s)
i; n It
meturn Line Eleva on e a
Elevation (ft) from Return Manifold to WWTF
1.923 5.286
-19.077 -22.714
p.2 of 3 10/20/2008
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
MMARY ZONE 5A-23
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
2677
PRV NEEDED? YES
NE SUMMARY W/ PRV
Pressure loss required (high pressure - 60 Psi)
Feet
59.1
Psi
51.2
Pressure at manifold before PRV
454.7
154.3
117.7
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
'60.6
PRV setting utilized
115.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
25.5
11'6
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 ftis 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.) 4.137) (Q/C)1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
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.
R Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 513-25
No. Laterals:
11
Tubing: ID (in)
0,79
Emitters (gph):
0
Emitter Spacing
RAn'd Flush Rate (aprn)':
Total Footage:
5986
Design Flow (gpm):
30.93
Supply Manifold Elev.
30.9
5B-SM1
2.0
Return Manifold E
0.787
5B-RM1
2.30
RAn'd Flush Rate (aprn)':
Run
Run
Lateral Run Elev.
Lenqth
# Ernittf
1 1
1.4
136
2
136
2 3
2.8
136
4
137
3 5
1.4
137
6
5.2
138
4 7
139
8
562
139
5 9
1.5
140
10
141
6 11
2.9
141
12
142
7 13
1.5
142
14
5.2
143
8 15
110
16
432
106
9
1A
12
75
588
3.0
67
0.8
70
10 21
0.7
70
22
65
23
63
24 60
11 57
53
48
43
IN In 41
p fication Flow (gpm):
30.9
Min. Design Scour V 1. (ft1s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scou
2.30
RAn'd Flush Rate (aprn)':
Dose
w (gprn�
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
Flow (gpm)
1.4
544
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
556
2.9
5.2
1.4
1.4
562
2.9
5.2
1.5
1.5
566
2.9
5.2
1.5
1.5
570
2.9
5.2
1.5
1.1
432
2.2
4.5
1A
0.8
588
3.0
5.3
0.8
0.7
0.7
0.7
516
2.7
5.0
0.7
0.7
0.6
0.6
556
2.9
5.2
0.5
0.5
0.4
0.4
0.4
,in a
9
56.2
Brooks Engineering Associates, PA p. 1 of 3 10/20/2008

I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5B-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 Unit'
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H.0 .2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev BMWs
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)
MNIWWWRWAMN�
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-SM1
Segment Flow Rate (gpm)
mfflmm��
Line Length (ft)
Line Size ID (in�
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
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
4
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
EMMEM
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 LateraI5
Line Size ID (in)5
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 J16
--
Segment Flow Rate (gpm)
MOM
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
2.511
Line Velocity (ft1s)
2.93
A6 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
11.262
Friction Headloss (ft)
Line Velocity (ft1s)
1.91
J20 to VVVVTF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.883
Line Velocity (ft1s)
1.91
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WVVTF
71 Brooks Engineering Associates, PA p.2 of 3
10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 513-26
78.3
51.2
Pressure at manifold before PRV
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
26SZ A
PRV NEEDED? YES
Pressure loss required (high pressure - 60 psi)
78.3
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
116.5
50.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
28.5
112.3
Flush Pressure at WVVTF 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 10/2012008

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
I 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.) 4.11)
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
a Equals the Required Flush Rate plus the Dose Flow Rate
Zone: 513-26
No. Laterals:
8
Tubing: ID (in)
O�79
Emitters (oph):
062
Emitter Spacing (ft)
45
Total Footage:
4714
Design Flow (gpm):
24.36
Supply Manifold Elev.
Return Manifold E
Run
Lateral Run Elev.
5B-SM1
5B-RM1
Run
Lenqth
# ErnittE
1 1
Tubing ID (in)
39
2
2.30
45
3
3.0
49
4
50
5
0.5
51
6
53
2
76
0.5
76
0.5
75
75
3 11
3.1
74
12
74
13
0.8
73
14
74
4
75
0.8
590
75
5.3
0.8
75
75
5 19
75
20
74
21
0.8
74
22
5.4
74
6
75
0.8
75
0.8
75
74
7 27
3.1
75
28
74
29
0.8
74
30
74
8
71
0.8
598
7 1
5.4
0.8
70
68
Application Flow (gpm):
24.4
Min. Design 1
2.0
Tubing ID (in)
-
OJ87
Residual Flow for Scour
2.30
Req'd Flush Rate (gpm)':
42.8
Dose
Lateral
Lateral
Min. Flush
N (gpM)7
Length (ft)
Dose(gpm)
Flow (gprn�
0.4
574
3.0
5.3
0.5
0.5
0.5
0.5
0.5
0.8
604
3.1
5.4
0.8
0.8
0.8
0.8
590
3.0
5.3
0.8
0.8
0.8
0.8
600
3.1
5.4
0.8
0.8
0.8
0.8
594
3.1
5.4
0.8
0.8
0.8
0.8
598
3.1
5.4
0.8
0.8
0.8
0.8
694
3.1
5.4
0.8
0.8
0.8
0.7
560
2.9
5.2
0.7
0.7
Brooks Engineering Associates, PA p.1 of 3 1012012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engineers Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
all emitters operate between 7 and 70 psi,
there is sufficient pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 fUs is provided.
2. The source of either the calculations or the data inputs are indicated in the footnotes.
3. The inputs for the calculations of the Summary data is indicated by the Input Line number
Footnotes
1 From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
(Flush flow is for single zone and Dose flow is for dual zones.) 4.81) (Q/C)1.85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Engineering Drawings
6 Calculated from Q = VA
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
a Equals the Required Flush ate plus the Dose Flow Rate
Zone: SB -27
No. Laterals:
9
Tubing: ID (in)
0.79
-'�-62
Emitters (gph):
Residual Flow for Scour
Emitter Spacing (ft)
2
Total Footage:
3986
Design Flow (gpm):
20.59
Application Flow (gpm):
20.6
Min. Design Scour Vel. (ft1s)
2.0
Tubing ID (in)
0.787
Residual Flow for Scour
2.30
Rea'd Flush Rate (gpm)':
41.3
Supply Manifold E ev.
2e
5B-SM2
Return Manifold -
5B-RM2
I
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Length
# Emitters
Flow (gpM)7
Length (ft)
Dose (gpm)
Flow (gpm
1
1 1
144
1.5
574
3.0
5.3
2
2
143
1.6
3
2 3
137
1.4
542
2.8
5.1
4
4
134
1.4
5
3 5
131
1.4
516
2.7
6.0
6
6
127
1.3
7
4 7
123
1.3
484
2.5
4.8
8
8
119
1.2
9
5 9
114
1.2
446
2.3
4.6
10
1 0
109
1.1
1 1
6 11
106
1.1
416
2.1
4.4
12
102
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 1012012008

I
I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE SB -27
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
I Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unit5
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H. U.2
2 Total Segment Headloss (ft) = Friction + Elev.
inputs [Dose Flow (all Flush Flow (b)
lam
0.015 0.013
12.015 12.0`13
! P� , p,2 of 3 10/20/2008
Brooks Englneedng Associates, PA
Hydraulic Unit
H.U. Elev NEW
3 Headloss from H.0 (ft.)3
MINMENSIMIM
Supply Force Main Friction Losses
H.U. to J20
Segment Flow Rate (gpm)
ffliffilmlimm
Line Length (ft)
Line Size ID (in)'�
L401,
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
04�
Minor Losses (ft)
0.775
0.648
Line Velocity (ft1s)
2.03
1.84
J16 to 5B-SM2
Segment Flow Rate (gpm)
mlfflm���
Line Length (ft)
Line Size ID (in
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
to Manifold
7 Elevation (ft) from H.U.
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold4
Feed Manifold to Bottom Lateral
'Alo
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Latera
Elevation (ft) from Manifold to Bottom Feed Lateral5
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera,2
0.867
3.478
9 Total Segment Headloss (ft) = Friction + Elev.
-17.133
-21.522
Return Force Main Friction Losses
6B-RM2 to J 16
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headioss (ft)
6.497
Line Velocity (ft/s)
2.16
J16 to J20
Segment Flow Rate (gpm)
Line Length (ft)
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)
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 WVVTF
! P� , p,2 of 3 10/20/2008
Brooks Englneedng Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE SB -27
(31.0
0 1 Z
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
Pressure loss required (high pressure - 60 Psi)
(31.0
0 1 Z
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 1012012008

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
I 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.) 4.17) (Q/C)1.81
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
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 (gph):
E-6-2
Emitter Spacing (ft)
2
Total Footage:
2684
Design Flow (gpm):
13.87
Supply Manifold Elev. 5B-SM2
26
2684
Brooks Engineering Associates, PA
45
47
48
51
53
56
59
63
64
67
70
71
70
69
69
68
67
67
37
36
32
28
24
21
17
Application Flow (gpm):
13.9
Min. Design Scour Val. (ft/s)
6
2.0
Tubing ID (in)
0.787
Residual Flow for Scour
2.30
Req'd Flush Rate (gpm)':
25.4
Dose
Flow (gpM)7
Lateral
Length (ft)
Lateral
Dose (gpm)
Min. Flush
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
2.6
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
10/20/2008

I
!-TM
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 5B-28
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
I 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.2
2 Total Segment Headloss (ft) = Friction + Elev.
Brooks Engineering Associates, PA p.2 of 3 10120/2008
Hydraulic Unit
H.U. Elev Mom
3 Headloss from H.0 (ft.)3
Wad
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
J 16 to 5B-SM2
Segment Flow Rate (gpm)
Raiku
M -
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
p#p�
Supply Force Main Elevation Delta
i
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold4
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.443
4.501
9 Total Segment Headloss (ft) = Friction + Elev.
-26.557
-30.499
Return Force Main Friction Losses
56-RM2 to J 16
Segment Flow Rate (gpm)
i
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
6.497
Line Velocity (ft/s)
2.16
J1 6 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
11.262
Line Velocity (ft/s)
1.91
J20 to WV\fTF
�77
Segment Flow Rate (gpm)
Line Length (ft)
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
FRINIM
Brooks Engineering Associates, PA p.2 of 3 10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 613-28
71.0
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
209.6
90.8
Flush Pressure at backwash tank for Min. Flush Rate
606.9
262.7
PRV NEEDED? YES
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
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
63.5
Brooks Engineering Associates, PA P.3 of 3 10/2012008

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
I 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.) 4.17) (Q/C)1.81
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ d
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mrn 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 (gph):
0.62
Emitter Spacing (ft)
Rea'd Flush Rate (gpm)':
Total Footage:
5018
Design Flow (gpm):
25.93
Applicat on Flow (gpm):
25.9
Min. Design ScourVel. (ft/s)
2.0
Tubing ID (in)
0.787
Residual Flow for S Aiu5p-f
2.30
Rea'd Flush Rate (gpm)':
48.9
Supply Manifold E ev.
4B-SM1
Return Manifold Et.
4B-RM2
Run
Run
Dose
Lateral
Lateral
Min. Flush
Lateral Run Elev.
Length
# Emitters
Flow (gpm�
Length (ft)
Dose (gpm)
Flow (gpm)8
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
20
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
1A
13
102
1.1
410
2.1
4.4
14
103
1.1
16
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
In
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
.48 -
18
0.2
8
20.0
Brooks Engineering Associates, PA p.1 of 3 10120/2008

r4l�
I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 413-29
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
1 Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unie
Line length (ft) from P.T. to H.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H U.2
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev MEW
3 Headloss from H. U (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)
5.061
0.920
Minor Losses (ft)
0.506
0.092
Line Velocity (ft1s)
1.51
0.60
J20 to J16
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
0.209
0.679
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
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
H.U. to Manifold
7 Elevation (ft) from
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold 4
Feed Manifold to Bottom Lateral
4
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Lateral5
Elevation (ft) from Manifold to Bottom Feed Lateral5
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral2
1.453
4.518
9 Total Segment Headloss (ft) = Friction + Elev.
-30.547
-34.482
Return Force Main Friction Losses
4B-RM1 to J16
Segment Flow Rate (gpm)
--
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
4.958
Line Velocity (ft1s)
1.54
J16 to J20
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
1.237
Line Velocity (ft/s)
0.58
J20 to WWTF
Segment Flow Rate (gpm)
OEM
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
1.305
Line Velocity (ft/s)
0.58
Return Line Elevation Delta
Elevation (ft) from Return Mangold to WWTF
p.2 of 3
Brooks Engineering Associates, PA
10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 413-29
Feet
104.8
PSI
51.2
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
Pressure loss required (high pressure - 60 psi)
Feet
104.8
PSI
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
60.�
Low Pressure Check: P at Min. Flush Flow at Return Manifold
23.5
10.2
Flush Pressure at WVVTF for Min. Flush Rate
27:�l
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
2
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

I
I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
P�"!
I I Engineer's Notes & Instructions:
"Na, 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,
Rlq� 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.) I
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 L/ 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 ate plus the Dose Flow Rate
Zone: 3BU-30
No. Laterals:
48
Tubing: ID (in)
0.79
Emitters Oph).
0.62
Emitter Spacino (ft)
2
Total Footage,
18398
Design Flow (qpm):
95.06
Supply Manifold Elev. 3B-SM1
Return Mani 3B-RM1
Run Run
1
1
156
2
2
167
3
3
169
4
4
171
5
5
173
6
6
175
7
7
177
8
a
179
9
9
182
10
10
183
11
11
184
12
12
185
13
13
185
14
14
185
15
15
186
16
16
186
17
17
187
18
18
188
19
19
iss
20
20
190
21
21
192
22
22
194
23
23
196
24
24
199
25
25
202
26
26
205
27
27
209
28
28
212
29
29
216
30
30
220
31
31
217
32
32
216
33
33
216
34
34
217
35
35
215
36
36
214
37
37
213
38
38
208
39
39
204
40
40
200
41
41
197
42
42
193
43
43
188
44
44
183
45
45
178
46
46
172
47
47
166
48
4.5
161
432
__48
18398 91 9�
Application Flow (apm):
95.1
M1 Design Scour Vel. (ft1s)
2.0
Tubing ID (in)
0787
Residual Flow for Scour (gpm)'
2.30
Req'd Flush Rate (gpm)B:
205.5
Supply Manifold Elev.
3B-SM2
Return Manifold
Elev.
3B-RM2
Dose
Lateral
Lateral
Min. Flush
Flow (gpM)7
Length (ft)
Dose(gpm)
Flow (gpm)'
1.6
312
1.6
3.9
1.7
334
1.7
4.0
1.7
338
1.7
4.0
1.8
342
1.8
4.1
1.8
346
1.8
4.1
1.8
350
1.8
4.1
1.8
354
1.8
4.1
1.8
358
1.8
4.1
1.9
364
1.9
4.2
1.9
366
1.9
4.2
1.9
368
1.9
4.2
1.9
370
1.9
4.2
1.9
370
1.9
4.2
1.9
370
1.9
4.2
1.9
372
1.9
4.2
1.9
372
1.9
4.2
1.9
374
1.9
4.2
1.9
376
1.9
4.2
1.9
376
1.9
4.2
2.0
380
2.0
4.3
2.0
384
2.0
4.3
2.0
388
2.0
4.3
2.0
392
2.0
4.3
2.1
398
2.1
4.4
2.1
404
2.1
4.4
2.1
410
2.1
4.4
2.2
418
2.2
4.5
2.2
424
2.2
4.5
2.2
432
2.2
4.5
2.3
440
2.3
4.6
2.2
434
2.2
4.5
2.2
432
2.2
4.5
2.2
432
2.2
4.5
2.2
434
2.2
4.5
2.2
430
2.2
4.5
2.2
428
2.2
4.5
2.2
426
2.2
4.5
2.1
416
2.1
4.4
2.1
408
2.1
4.4
2.1
400
2.1
4.4
2.0
394
2.0
4.3
2.0
386
2.0
4.3
1.9
376
1.9
4.2
1.9
366
1.9
4.2
1.8
356
1.8
4.1
1.8
344
1.8
4.1
1.7
332
1.7
4.0
Brooks Engineering Associates, PA P. I of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 38-30
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.U.'
Line Size ID (in)
Friction Headloss (ft) from Pump to H U.2
0.005
0.019
2 Total Segment Headloss (ft) Friction + Elev.
12.005
12.019
Hydraulic Unit
H.U. Elev 11SM
3 Headloss from H. U (ft)3
Supply Force Main Friction Losses
H.U. to 313-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
. : 11 1 ; .1
1.17
2.53
ne a oc ty � s,
Supply Force Main Elevation Delta
5 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
6 Total Headloss (ft.) in drip system from supply manifold to return manifold4 Riffismilliffimm
Feed Manifold to Bottom Lateral
Headloss (ft) in manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12 0.587 2.378
7 Total Segment Headloss (ft) = Friction + Elev, -50.413 -55.622
Return Force Main Friction Losses
313-SM2 to WWTF
Segment Flow Rate (gpm) REZ�
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
8 Friction Headloss (ft) 17.538
Line Velocity (ft1s) 2.78
Return Line Elevation Delta
9 Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3 10120/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 3B-30 SUBMANIFOLD 313-SM2
�510.j
01,/
Pressure at manifold before PRV
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
160.7
%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)
�510.j
01,/
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
A5,6
Low Pressure Check: P at Min. Flush Flow at Return Manifold
44.0
19.0
Flush Pressure at VVWTF for Min. Flush Rate
94.4
40.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
147.4
63.8
Note: Return Flush Tank needed, See Pressure Calcs for Zone 313-30 Submanifold 1.
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 313-30 SUBMANIFOLD 3B-SM1
;610.4
Pressure at manifold before PRV
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
Pressure loss required (high pressure - 60 psi)
;610.4
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 WVVTF 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 WWTF 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
Engineers 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: hf = (4.727 U d 4
1) (Q/C)l .85
3 From Wastewater Systems Inc. Date
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 Reaulred Flush Rate cilus the
Dose low Rate
Zone:
lication Flow (opm):
No. Laterals: 18
tff Deslan Scour Val. (ft/s)
2.0
Tubing: 10 (in) 0.79
Tubing ID (in)
0
Emitters (oDh): 0.62
a 1 us, Fg for gcouy
1 _Y__ 1 __ ('prn)'
130
Emitter Spacina (ft) 2
Rod "ush "T
91.8
Total Footage: 9760
Desian Flow (opm 50.43
Supply Manifold Elev. 6A-SM5
Return Manifold Elev. 6A-RM5
supply Manifold Elev. 6A-SM4
Return Manifold Elev. SA-RM4
Supply Manifold Elev. 6A-SM3
Return Manifold Elev. SA-RM3
Run
Dose Lateral Lateral
Min. Flush
Lateral Run Lenath # Emitters
Flow kiprn� Len* (ft) Dose Opm)
Flow (gpm?
1 1
105
1.6 630 3.3
5.6
2
157
1.6
2 3
1 57
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
1 54
1 .6 616 3.2
5.5
8
154
1.6
5 9
1 53
1.6 612 3.2
5.5
10
153
1.6
6 11
124
1.3 496 2.6
4.9
1 2
1 24
1 ' 3
7 13
126
1.3 506 2.6
4.9
14
1 27
1.3
8 1 5
129
1 3 518 2.7
6.0
1 6
130
1 1
9 17
131
1.4 526 2.7
5.0
18
132
1 A
10 19
11
1 538 2.8
5.1
20
35
'�4
11
67
0.7 622 3.2
5.5
54
0.6
51
0.5
48
0.
46
45
0.5
12
44
0,5 514 2.7
5.0
45
0.5
45
0.5
45
0.5
46
0.5
32
0.3
13
49
0.5 392 2.0
4.3
49
0.5
49
0.
49
0.5
14 37
49
0.6 698 3.1
5.4
38
60
0.5
39
50
0.5
40
50
0.5
41
50
0.5
42
50
0.5
15 43
51
0.5 612 3.2
5.5
44
50
0.
45
51
46
51
0.5
47
51
0.6
48
52
0.5
16 49
52
0.5 624 3.2
5.5
60
52
0.6
51
52
a 5
52
52
0 5
53
52
0.5
54
52
0.5
17 55
49
0.5 485 2.5
4.8
56
45
0.5
57
42
0.4
58
3:
0.4
59
3
(), 4
60
33
0.3
18 61
31
0.3 218 1.1
3.4
62
2
0.3
63
2:
3
.4
24
-n
2
50.4
91.8
Brooks Engineering Associates, PA p.1 of 3 1111812008

N
I
M11i I I Brooks Engineering Associates, PA p.2 of 3 11/1812008
Willi
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE SA -31
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE I inputs Dose
Flow Flush Flow (b)
1 Operating Head from Pump Curvel
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.'
0.010
0.011
2 Total Segment Headloss (ft) Friction I Elev.
12.010
12.011
Hydraulic Unit
H.U. Elev §0NM
3 Headloss from H.0 (It.?
Supply Force Main Friction Losses
H.U. to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Une Size ID (in?
4 Friction Headloss (ft)
5.052
0.505
5.635
0.564
Minor Losses (ft)
Line Velocity (ft/s)
1.78
1.89
3B-SM2 to 3B-SM1
Segment Flow Rate (gpm)
RUNWHOM
Line Length (ft)
ON
Line Size ID (Imp
5 Fricti n Headloss (ft)
0,410
0.458
MinooLosses, (ft)
0.041
0.046
Line Velocity (ft1s)
1.78
1.89
38 -SMI to SA_SM3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
6 Friction Headloss (ft)
0.731
2.174
Minor Lomas (ft)
0.073
0.217
Une Velocity (ftfs)
1.30
2.35
Supply Force Main Elevation Delta
7 Elevation (ft) from H.U. to Manifold
DHp System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold4
SA -31 _,9M-3 Feed Manifold to Bottom Lateral
Headloss (ft) in manifold'
Une Length (ft) from Supply Manifold to Bottom Feed Latersl'
100
1
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line Size ID finP
Friction Headloss, (ft) from Manifold to Bottom Feed Lateral'
0.000
0.000
a Total Segment Headloss (ft) - Friction + Elev.
-49.000
-56.000
Return Force Main Friction Losses
6A-RM3 to 38 -SMI
Segment Flow Rate (gpm)
Une Length (ft)
Line Size tD (in.)
Minor Losses from Check ValVe
5.261
Friction Headloss (ft)
Line Velocity (ft1s)
2.78
3B-SM1 to 38-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Une Size ID (In.)
Minor Losses (ft)
0.515
Friction Headloss, (ft)
1 -me Velocity (ft/s)
1.61
3B-SM2 to WWTF
Segment Flow Rate (gpm)
Line Length (ft) 2585
wir��
Line Size ID (in.)
Minor Losses (ft)
6.341
Friction Headloss (ft)
1.61
Line Velocity (ftfs)
Return Une Elevation Delta
Elevation (ft) from Return Manifold to VhVTF
I
M11i I I Brooks Engineering Associates, PA p.2 of 3 11/1812008
Willi

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
UMMARY ZONE SA -31 SUBMANIFOLD 6A 3
Feet
psi
Total Headloss at Min. Flush Rate at Return Manifold
45.7
j139�B
Low Pressure Check: P at Min. Flush Flow at Return Manifold
546.7
7
High Pressure Check: ' 0�om Dose Flow
696.2
301.4
Flush Pressure at I'.. =kol.'r.,n FlLu=
200.0
86.6
PRV NEEDED? YES
ZONE SUMMARY W! PRV
Feet
PSI
Pressure loss required (high pressure - 60 posi)
557.6
51.2
Pressure at manifold before PRV
473.2
117.7
PRV :etfingg calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV etdn utilized
116.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
20.5
8.9
Flush Pr 'or Min. Flush Rat'
-151.6
.65.6
Frlqh liter I on tio. Lateral at ... Now
P==F.
157.5
68.2
Note: Return Flush Tank needed. Flush Pressure at WWTF is too low. May not have sufficlent pressure
to return the flush.
Brooks Engineering Associates, PA p,3 of 3 11/18t2008
Lmi

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
MARY ZONE 6A-31 Submanifold SA-SM4
Feet
Psi
Total Headloss at Min. Flush Rate at Return Manifold
10" 3
4.4
Low Pressure Check: P at Min. Flush Flow at Return Manifold
..7
212.4
High Pressure Check: Emitter P on Bottom Lateral at Dos. Flow
624.2
2 0.2
Flush Pressure at backWaSh tank for Min. Flush Rate
254.0
11700
PRV NEEDED? YES
ONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high Pressure - 60 Psi)
485.6
473.2
51.2
117.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - Pressure loss required)
154.3
66.5
PRV setting utilized
115.5
Low Pressure Check; P at Min. Flush Flow at Return Manifold
20.5
8.9
Flush Pressure at WWTF for Min. Flush Rate
-97.6
-42.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
141.5
61.3
Note: Return Flush Tank needed. Flush Pressure at WWTF 1. too low. May not have sufficient Pressure
to return the flush.
Brooks Engineering Associates, PA p.3 of 3 1012012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE SA -31 SUBMANIFOLD 6A -SMG
Feet
PSI
Total Headlow, 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 W1 PRV
Feet
Psi
Pressure low required (high pressure - 60 psi)
431.6
51.2
Pressure at manifold before PRV
473.2
154.3
117.7
66.5
PRV setting calculated (pressure at manifold - pressure low required)
PRV setting alized
115.5
50.0,',�
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
High Pressure Check: Emitter P on Bottom Lateral at Dose Flo.
149.5
64.7
Note: Return Flush Tank needed. Flush Pressure at WWTF is too low. May not have sufficient pressure
to return the flush.
Brooks Engineedng Associates, PA p.3 of 3 10120/2008

L4
I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
Engine rs 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
I 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.) 4-87) (Q/C)i 85
2 Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d
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
I
Supply Manifold E ev. 6A-SM2
Return Manifold 2ev. 6A-RM2
Run Run
Lateral Run Elev. Length
1 111111110 loom
2
3
4
6
7
10
11
12
8
9
10
11
12
Is17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
�0
43
44
44
45
47
48
50
53
56
57
59
60
66
70
74
78
106
112
148
'157
154
152
150
1 46
143
140
136
128
123
67
57
50
44
37
12
Ap_ lication Flow (gpm):
Zone: I 6A.32
No. Laterals: 12
Tubing: ID (in) 0.79
Emitters (gph): 0.62
Emitter Spacing (ft) 2
Total Footage: 6350
Design Flow (gpm): 32.81
I
Supply Manifold E ev. 6A-SM2
Return Manifold 2ev. 6A-RM2
Run Run
Lateral Run Elev. Length
1 111111110 loom
2
3
4
6
7
10
11
12
8
9
10
11
12
Is17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
�0
43
44
44
45
47
48
50
53
56
57
59
60
66
70
74
78
106
112
148
'157
154
152
150
1 46
143
140
136
128
123
67
57
50
44
37
12
Ap_ lication Flow (gpm):
32.8
Min. Design Scour Val. (ft
2.0
Tubing I (in)
0.787
Residual Flow for Scour gpm
2.30
Rea'd Flush Rate (gpm)':
60.4
Supply Manifold Elev.
6A-SM1
Return Manifold Elev.
6A -RMI
Dose Lateral
Lateral
Min. Flush
Flow (gpM)7 Length (ft)
Dose (gpm)
Flow (gPM)8
0.4 530
Z. f
5.0
0.4
0.5
0.5
0.5
0.5
0.5 646
3.3
5.6
0.5
0.5
0.6
0.6
0.6
0.6 540
2.8
5.1
0.7
0.7
0.8
0.8 322
1.7
4.0
0.9
1.0 400
2.1
4.4
1.1
1.2 520
2.7
5.0
1.5
1.6 622
3.2
5.5
1.6
1.6 604
3.1
5.4
1.6
1.5 578
3.0
5.3
1,5
1.4 552
2.9
5.2
1.4
1.3 502
2.6
4.9
1.3
0.7 534
2.8
5.1
0.6
0.5
0.5
0.4
q p " ! Brooks Engineering Associates, PA p.1 of 3 10/20/2008
Nk;

I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 6A-32
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
I Operating Head from Pump Curve'
Pump Tank to H.U.
Elevation (ft) from Pump to Hydraulic Unie
Line length (ft) from P.T. to H.U.5
Line Size ID (in)
Friction Headloss (ft) from Pump to H U.2
2 Total Segment Headloss (ft) = Friction + Elev.
F -
Inputs IDoseFlow(a I lFlush low b
KJO&M
0.010 0.011
12.010 12.011
p.2 of 3 10/20/2008
Brooks Engineering Associates, PA
Hydraulic Unit
H.U. Elev OEM
3 Headloss from H.0 MY
4
Supply Force Main Friction Losses
H.U. to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (In)5
5.062
5.635
4 Friction Headloss (ft)
Minor Losses (ft)
0.505
0.564
Line Velocity (ft/s)
1.78
1.89
3B-SM2 to 3B-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)5
5 Friction Headloss (ft)
0.410
0.458
Minor Losses (ft)
0.041
0.046
Line Velocity (ft1s)
1.78
1.89
3B -SMI to 6A-SM3
Segment Flow Rate (gpm)
Line Length (ft)
Line Size 10 (in)5
6 Friction Headloss (ft)
0.731
2.174
0.217
Minor Losses (ft)
0.073
Line Velocity (ft/s)
1.30
2.35
Supply Force Main Elevation Delta
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
4
6A -32 -SM -1 Feed Manifold to Bottom Lateral
4
Headloss (ft) in manifold
Line Length (ft) from Supply Manifold to Bottom Feed Lateral
A*
Elevation (ft) from Manifold to Bottom Feed Latera15
Line Size ID (in)5
Friction Headloss (ft) from Manifold to Bottom Feed Latera12
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
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headloss (ft)
5.261
Line Velocity (ft1s)
2.78
313-SM1 to 3B-SM2
Segment Flow Rate (gpm)
REMEM
Line Length (ft)
Line Size ID (in.)
Minor Losses (ft)
Friction Headloss (ft)
0.515
Line Velocity (ft/s)
1.61
36-SM2 to WWTF
Segment Flow Rate (gpm)
Line Length (ft)
alli
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
p.2 of 3 10/20/2008
Brooks Engineering Associates, PA

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6A-32 Submanifold 6A -SMI
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 W1 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
50.0
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
H1 h 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
Feet
PSI
Pressure loss required (high pressure - 60 psi)
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
A97 n
181"
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
304.2
51.2
Pressure at manifold before PRV
473.2
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
PRV setting utilized
115.5
Low Pressure Check: P at Min. Flush Flow at Return Manifold
23.6
16.2
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 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
Enolneer's No s & lnstructions�
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,
2
there is sufficient pressure to return the flush to the Hydraulic Unit,
0.8
a flushing flow velocity of 2 file 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
80
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.)
4
2 Headloss from pipe friction calculated from Hazen -Williams Equation: h, = (4.727 Ll d"') p1c)"s
3 From Wastewater Systems Inc. Data
4 Headloss estimated from dosing and flushing curves for 20 mm Drip Tubing
5 From Enpineerinq Drawingis
5
6 Calculated from Q = VA
0.9
7 Equals the # of emitters in the run times the individual emitter flow rate in gpm.
1.8
8 Equals the Required Flush Rate olus
the Dose
Flow Rate
90
0�9
Zone: 6
pplicatton Flow (9prn):
3
7
No. Laterals: 30
1. 0
376
�2j
4.2
Tubing ID (in) 0.79
8
Tubin ID in
1.0
Emitters (cph): 0.62
Residual Flow for Scour (gpm)'
2.30
98
Emitter Spacing (ft) 2
398
1 Ph -h Q.t. opir)': _
128.6
Total Footage: 1152e
101
1.0
Desion Flow (cDrn): 59.56
5
Supply Manifold Elev,11 68-SM3
1 04
Return Manifold Elev. 68-RM3
414
Supply Manifold Elev. 6S.SM2
4.4
Return Manifold Slay. 6B.RM2
12
Supply Manifold Elev, 6MM1
1.1
Return Manifold Elev. 68-RM1
Run Run Dose Lateral Lateral
Min. Flush
Lateral Run Eley. Lenqth #EnnitteEE Flow(gpnri� Length(ft) Dose(OPM)
Flow (gpm)g
1 1 74 0.8 628 3.2
5��
Brooks Engineering Associates, PA p.1 of 3 10120/2008
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
1 1
1 04
1 1
414
2.1
4.4
12
103
1.1
6
13
101
1.0
400
2.1
4.4
1 4
99
1 0
7
1 5
98
lo
388
2.0
4.3
16
as
1.0
8
1 7
96
1 .0
380
2.0
4.3
18
94
1.0
9
'a
93
1.0
372
1.9
4.2
20
93
1'0_368
10
21
92
'.o
1.9
4.2
22
92
1.0
11
23
91
0.9
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
is
31
88
0.9
352
1.8
4.1
32
88
0.9
16
33
88
0.9
350
1.8
4.1
3
87
o' 9
17
35
87
0.9
348
1.8
4.1
3
87
0.9
18
37
86
0.9
346
1.8
4.1
3
87
0.9
19
39
87
0.9
348
1.8
4.1
40
87
0.9
20
41
87
0
348
1.8
4.1
42
0�:
-
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
88
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
1
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
0.8
60
73
0.8
29
61
70
0.7
518
2.7
5.0
62
as
0.7
63
63
0.7
64
60
0.6
30
65
58
0.6
440
2.3
4.6
66
56
0.6
67
54
0.6
Brooks Engineering Associates, PA p.1 of 3 10120/2008

I
I
I
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
ZONE 6B-33
TOP LOAD MANIFOLD PRESSURE ANALYSIS
INPUT
LINE
I Inputs I Doss Flm fall Flush FICW
1 Operating Head from Pump Curve'
Pump Tank to H.U,
Elevation (ft) from Pump to Hydraulic Uni?
Line length (ft) from P.T. to H.0 5
No
Line Size ID (in)
Friction Headloss (ft) from Pump to H.U.'
0.010
0.011
2 Total Segment Headloss (ft) Friction + Eley,
12.010
12.011
Hydraulic Unit
H.U. Elev 01aw
3 Headloss from H.0 (ft.?
Supply Force Main Friction Losses
H.U� to 3B-SM2
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID fln)"
4 Friction Headloss (ft)
5.052
5.635
Minor Losses (ft)
0.505
0.564
Line Velocity (ft1s)
1,78
1.89
3B-SM2 to 3B-SM1
segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (10
5 Friction Headloss (ft)
0.410
0A58
Minor Lomas (ft)
0.041
0.046
Line Velocity (fils)
1 .78
1.89
3B-SM1 to 6A_SM3
segment Flow Rate (gpm)
REMEMEMMIMM
Line Length (ft)
Line Size ID 0n)'
6 Friction Heachoss (ft)
0,731
2.174
Minor Losses (ft)
0 . 073
0.217
Line Velocity (1`116)
1 . 30
2.35
Supply Force Main Elevation Delta
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'
11SEEM
68 -33 -SM -1 Feed Manifold to Bottom Lateral
Headloss (ft) In manifold4
Line Length (ft) from Supply Manifold to Bottom Feed Lateral'
01
Elevation (ft) from Manifold to Bottom Feed Lateral'
Line size ID (In�
Friction Headloss (ft) from Manifold to Bottom Feed Later@12
1.412
4.449
9 Total Segment Headloss (ft) = Friction + Elev.
-5&588
.57.551
Return Force Main Friction Losses
6A-RM3 to 3B -SMI
segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in.)
Minor Losses from Check Valve
Friction Headlow (ft)
5.261
Line Velocity (fl/s)
2.78
3B-SM1 to 3B-SM2
Segment Flow Rate (gipm)
Line Length (ft)
Line Size ID (in.)
Minor Lomas (ft)
Friction Headloss (ft)
0.515
Line Velocity (ft/$)
1.61
3B-SM2 to VVWTF
Segment Flow Rate (gpm)
Line Length (ft)
Line Size 10 (in.)
Minor Losses (ft)
Friction Headloss (ft)
6.341
Lin. Velocity (ft)
1.61
Return Line Elevati- Delta
Elevation (ft) from Return Manifold to VVWTF
Brooks Engineering Associates. PA p.2 of 3 10/2012008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 6B-33 Subinanifold l
Feet
Psi
Total Headloss, at Min. Flush Rate at Return Manifold
.47.7
-20.7
Lm Pressure Check, P at Min. Flush Flow at Return Manifold
552.7
239.3
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
700�8
303.4
Flush Pressure at backwa.h tank for Min. Flush Rate
194.0
-8410
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
562 ' 2
51.2
Pressure at manifold before PRV
473.2
117.7
PRV calculated (Pressure at manifold - Pressure low required)
154.3
66.5
:etting
PRV sting utilized
115.5
500
Low Pressure Check: P at Min. Flush Flow at Return Manifold
22.5
9.7
Flush Pressure at VAVTF for Min. Flush Rate
.161.6
-70.0
ni h Pressure ChecW Emitter P on Bottom Lateral at Dose Flow
162.1
702
Note: Return Flush Tank needed. Flush Pressure at WWTF is too iow. May not have sufficient
pressure to return the flush,
Brooks Engineering Associates, PA P.3 of 3 10120t2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 613�33 Submanifold 6B-SM2
Feet
PSI
Total Heactlass at Min. Flush Rate at Return Manifold
18. 3
-
Low Pressure Check: P at Min. Flush Flow at Return Manifold
486.7
- 7
�7
High Pressure Checic. Emitter P on Bottom Lateral at Dose Flow
634.8
S
flush Pressure at backwash tank for Min. Flush Rate
1,4
r
1 �j
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure Ion required (high pressure - 60 Psi)
496.2
51,2
Pressure at manifold before PRV
473.2
117.7
PRV satt ng calculated (pressure at manifold - pressure low required)
154 . 3
66.5
1
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
-95.6
-41.4
Hiah Pressure Checic Emitter P on Bottom Lateral at Dose Flow
162.1
70.2
Note: Return Flush Tank needed. Flush Pressure at WWTF is too 10W. 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 OB -33 Submanifold 6B4M3
Feet
Psi
Total Headloss at Min. Flush Rate at Return Manifold
64.3
27.8
Low Pressure Check: P at Min. Flush Flow at Return Manifold
440.7
190.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
568.8
246.2
Flush Pressure at bacicyash tank for Min. Flush Rate
312,0
135.1
PRV NEEDED? YES
ZONE SUMMARYWI PRV
Feet
PSI
Pressure lose required (high pressure - 60 psi)
430.2
51.2
Pressure at manifold before PRV
473.2
117.7
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRVsefting utilized
115.5
�-'50.Q
Low Pressure Check P at Min. Flush Flow at Return Manifold
22.5
9.7
Flush Pressure at VAVTF for Min, Flush Rate
43.6
-18.9
Hloh Pressure Check', Emitter P on Bottom Lat.nal at Dose Flow
142.1
6115
Note: Return Flush Tank needed. Flush Pressure at VVWTF 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
Engineer's Notes & Instructions:
1. The purpose of this calculation spreadsheet is to determine the pressures in the drip system
at critical points of interest. The governing criteria are:
Brooks Engineering Associates, PA p.1 of 3 10/20/2008
all emitters operate between 7 and 70 psi,
0.2
there is suffident pressure to return the flush to the Hydraulic Unit,
a flushing flow velocity of 2 ft/s is provided.
0.3
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
0.3
Footnotes
1
From PACO 200 GPM 40 hp Pump and Berkeley 200 GPM 10 HP Booster Pumps in Series Curve.
0.3
(Flush flow is for single zone and Dose flow is for dual zones.)
2
4. 7) (
Headloss from pipe friction calculated from Hazen -Williams Equation: hf = (4.727 U d 8 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
2 9
48
Zone: 413-34 Application Flow (9pm):
4161
3.1
No. Laterals: 20 Min. Design S ur Val. (m)
2.0
53
Tubing: ID (in) 0.79 Tubino 10 (in)
0.787
Emitters (aph): 0.62 Residual Flow for Scour (gpm)s
2.30
99
Emitter Spacina (ft) 2 Rea'd Flush Rate (Qpm)`
_79 -46 -
87.1
Total Footage:
12
99
Design Flow (glpm): 41.05
Supply Manifold Elev.11 48-SM4
3 13
99
Retum Manifold Elev. 4B-RM4
396
2.0
Supply Manifold Elev. 4B-SM3
14
99
Return Manifold Elev. 48-RM3
Supply Manifold Elev. 4B-SM2
4 15
99
Return Manifold Elev. 48-RM2
396
2.0
Run Run Dose Lateral Lateral
Min. Flush
99
Lateral Run Elev. Lan th # Emitters Flow j_%7 1 ­fh (M
1 22 0.2 496 2,6
4.9
Brooks Engineering Associates, PA p.1 of 3 10/20/2008
24
0.2
27
0.3
29
0.3
31
0.3
34
0.4
38
0.4
43
0.4
2 9
48
0.5
598
3.1
5.4
10
53
0.5
11
99
1.0
12
99
1'0
3 13
99
1.0
396
2.0
4.3
14
99
1.0
4 15
99
1.0
396
2.0
4.3
16
99
1.0
5 17
99
1.0
396
2.0
4.3
18
99
1.0
19
99
1.0
396
2.0
4.3
20
99
1.0
7 21
98
1.0
392
2.0
43
22
98
1.0
8 23
97
1.0
US
2.0
4.3
24
97
1.0
9 25
96
1.0
382
2.0
4.3
26
95
1.0
10 27
94
1.0
376
1.9
4.2
28
94
1.0
11 29
93
1.0
372
1.9
4.2
30
93
1.0
12 31
92
1.0
366
1.9
4.2
32
91
0.9
3 3
TT 33
3
89
0.9
356
1.8
4.1
3
34
4
89
0.9
3 5
14 35
4
89
0.9
354
1.8
4.1
36
3 a
as
0.9
37
15 37
5
87
0.9
348
1.8
4.1
38
38
87
0.9
6 39
16 39
86
0.9
342
1.8
4.1
40
40
85
0.9
7 41
17 41
85
0.9
338
1.7
4.0
42
42
84
0.9
1 a 43
18 43
82
1
0.8
326
1.7
4.0
44
81
0.8
19 45
79
0.8
314
1.6
3.9
46
78
0.8
20
75
0.8
614
3.2
5.5
61
0.6
53
0.5
47
0.5
39
0.4
32
0.3
7946 3973
41.1
41.1
87.'
Brooks Engineering Associates, PA p.1 of 3 10/20/2008

121
PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
`I
ZONE 48-34
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?
2 Total Segment Headloss (ft) = Friction + Elev.
Hydraulic Unit
H.U. Elev
3 Headloss from H.0 (ft.)3
Supply Force Main Friction Losses
H.U. to 3B-SM2
Segment Flow Rate (gpm) w
agi ®b�ua
a ,ffi me
Line Length (ft)
Line Size ID (in)'
4 Friction Headloss (ft)
5.052
5.635
Minor Losses (ft)
0.505
0.564
Line Velocity (Ws)
1.78
1.89
3B-SM2 to 3B-SM1
Segment Flow Rate (gpm)
Line Length (ft)
Line Size ID (in)'
5 Friction Headloss (ft)
0.410
0.458
Minor Losses (ft)
0.041
0.046
Line Velocity (Ws)
1.78
1.89
3B-SM1 to 6A-SM3
Segment Flow Rate (gpm)
Line Length (ft) I
Line Size ID (in)'
6 Friction Headloss (ft)
0.731
2.174
Minor Losses (ft)
0.073
0.217
Line Velocity (Ws)
1.30
2.35
Supply Force Main Elevation Delta
-156
7 Elevation (ft) from H.U. to Manifold
Drip System Headloss Results
8 Total Headloss (ft.) in drip system from supply manifold to return manifold
4
c
48-34-SM-2 Feed Manifold to Bottom Lateral
Headloss (ft) in manifold"
Line Length (ft) from Supply Manifold to Bottom Feed Laterals
Elevation (ft) from Manifold to Bottom Feed Laterals
Line Size ID (In)5
Friction Headloss (ft) from Manifold to Bottom Feed Lateral 2
0.559
2.865
9Total Segment Headloss (ft) = Friction + Elev.
-40.441
-45.135
Return Force Main Friction Losses
Friction Headloss (ft) 6.341
Line Velocity (Ws)
1.61
Return Line Elevation Delta
Elevation (ft) from Return Manifold to WWTF
Brooks Engineering Associates, PA p.2 of 3 10/20/2008
1

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 413-34 Submantfold 4B-SM2
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
-32.7
"14.2
Low Pressure Check: P at Min. Flush Flow at Return Manifold
537.7
232.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
664.6
287.7
Flush Pressure at backwash tank for Min. Flush Rate
217.0
93.9
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
526.0
51.2
Pressure at manifold before PRV
468.2
154.3
117.7
66.5
PRV setting calculated (pressure at manifold - pressure loss required)
PRV setting utilized
115.5
25.5
5,0.0
11.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at W WTF for Min. Flush Rate
-138.6
-60.0
Hi h Pressure Check: Emitter P on Bottom Lateral at Dose Flow
148.9
64.5
Note: Return Flush Tank needed. Flush Pressure at W WTF is too low. May not have sufficient pressure to return the flush.
Brooks Engineering Associates, PA p.3 of 3 10/20/2008

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 413-34 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.E
264.8
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
86.5
PRV setting utilized
115.5
25.5
50.0
11.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at W WTF for Min. Flush Rate
-98.6
-41.8
Hi h Pressure Check: Emitter P on Bottom Lateral at Dose Flow
139.9
1 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

PRESSURE ANALYSIS
TOP FEED MANIFOLD SYSTEM
SUMMARY ZONE 46-34 Submanifold 4B-SM4
Feet
PSI
Total Headloss at Min. Flush Rate at Return Manifold
-32.7
-14.2
Low Pressure Check: P at Min. Flush Flow at Return Manifold
537.7
232.8
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
664.6
267.7
Flush Pressure at backwash tank for Min. Flush Rate
305.0
132.0
PRV NEEDED? YES
ZONE SUMMARY W/ PRV
Feet
PSI
Pressure loss required (high pressure - 60 psi)
526.0
468.2
51.2
117.7
Pressure at manifold before PRV
PRV setting calculated (pressure at manifold - pressure loss required)
154.3
66.5
PRV setting utilized
115.5
25.5
50.0
11.0
Low Pressure Check: P at Min. Flush Flow at Return Manifold
Flush Pressure at W WTF for Min. Flush Rate
-50.8
-21.9
High Pressure Check: Emitter P on Bottom Lateral at Dose Flow
148.9
1 64.5
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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I
9
1.8 Rainfall Data Analysis for Short Term Wet Weather Storage
Lai Requirements

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

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I
I
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

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 Ni[TX CIONCRETE
P.O. BOX 173
MARION CENTER, PA 15759
[phone] Fax [phone]
WESSITE: WWW.MARIONCEN T>=RSUPPt-Y,COM
DATE: 14-Aug-08
CUSTOMER: ;::-< :.x ::.: �07��
-�- L 0�
FROJECT: Treatment Plant
MATERIALS 94URCE
Cement: Cemex, PittsburghAftmpum, PA
EXL Select- RM Excell Minerals, Sarver, PA
Coarse Aggregate: Hansen Aggregates, Torrance, PA
Fine Aggregate: Glacial Sand & Gravel, Tarrtown, PA
Water. Qnsite Well
Air Entrabting: Master Builders Inc„ MBAE 90
Water Reducer: Master Builders Inc., Pozzoiith 200N
Retarder: Master Builders Inc,, Pozzolith 100XR
super Plasticizier Master Builders Inc., Glenium 3030 NS
Non Chloride Acc, Master Builders Inc,, Pozzollty NC 534
MIX DESIGN 4000 psi Air Entrained
Material
Weight
(lbs,)
Cement
420
EXL Select - RM
140
Coarse Aggregate
1800
Fine Aggregates
1376
Water
195
Air 6.0w1,5%
6.0.0%
TOTAL 3931
ASTM
C-150
C114&1157
C-33
C-33
n!a
C-260
C-494
C-4S4
C-494
C-494
Gallons S.G,
Volume
(cm ft.)
3.15
2.14
2.90
0.77
2,68
10.76
2.87
8.58
23.41 1.00
3.13
1.52
27.00
TYPE
IJII
#57
A
potable
n!a
A-B-D
8-D
AF
C-E
Slump (inches); 4" MaXtmum
Calculated Unit Weight (pCt' 145,60
Water / Ratio: 0.35
Marion Center Supply will not be held responsible for any type of cracking_ Cracking
Is a natural thing which we have absolutely no control over-
` ADMIXTURE NOTES"'
1. At ambient temperatures below 75 degrees, 3 ozlcwt of 200N
2. At ambient temperatures from 75 - 85 degrees, 3 cz/cwt of 100XR
$. At ambient temperatures above 85 degrees, 4 o7lcwt of 1 DOXR
DQSAGE
n/a
n/a
nia
nfa
Na
As Required
See Below
See Selow
As Required
As Required

SCC6SPt. ��-- S,q c.�
ff
Valley City:
Cement
488 lb
3,15 Sp Gr
62.4
2.48 ft3
Ply Ash
102 lb
2.35 Sp Gr
62.4
0.70 ft3
Slag Cement
0 lb
2.35 Sp Gr
62.4
0.00 ft3
Gravel 57
840 lb
2.64 Sp Gr
62.4
5.10 ft3
Gravel 8
560 lb
2.64 Sp Gr
62.4
3.40 ft3
Concrete sand
1568 ib
2.64 Sp Gr
62.4
9.52 ft3
Water gl
30.50 254.065 lb
1 Sp Gr
62.4
4.07 ft3
Air
7% 1.89
1
1
1.89 ft3
6100
48 oz
AEA14
6 oz
NC
50 oz If Needed
Plastiment
15 oz If Needed
27,16 ft3
Comments:
watericem coarselfine cemlfla total agg
agg cu.ft.
2968
590 1400.00
0.43 0.53
22% 40%
8.50

r
Valley City:
Cement
530 lb
3.15 Sp Gr
62.4
2.70 ft3
Fly Ash
110 lb
2.35 Sp Gr
62.4
0.75 ft3
Slag Cement
0 lb
2.35 Sp Gr
62.4
0.00 ft3
Gravel 57
840 lb
2.64 Sp Gr
62.4
5.10 ft3
Gravel 8
560 lb
2.64 Sp Gr
62.4
3.40 ft3
Concrete Sand
1428 lb
2.64 Sp Gr
62.4
8.67 ft3
Water gl
34.00 283.22 lb
1 Sp Gr
62A
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 cemlf/a total agg
agg cu.ft.
2828
640 1400.00
0.40 0.50
22% 40%
8.50

r Al
Cat 1A Slip-OnFittings 2l16r04 12:39 PM Page 1
I
i
Wb91 Z-
Iv 10 1E i C9 0-1 le
IN�, N
olloondor.
lfbur Handrail Source.
Structural Slip -tin fittings used with aluminum, galvanized steel, stainless steel and
black iron pipe on installations around the world for over fifty years,
Hollaender Products are produced from only the highest
quality materials and feature proprietary fasteners
and design features.
Aluminum Alloy 535
• Most corrosive resistant aluminum casting alloy
available today
• High strength as cast
• Bright attractive burnished mill finish
• Conforms to ASTM B26 & B 179
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 pull out and
rotational slip
• Conforms to FF-S-200, ANSIIASNiE 818.3
Type CIG
The Hollaender Advantage
• Speed of Installation — Studies have shown
significant cost savings when compared to the
cost of welded handrail and other structures
• Ease of Installation — Only tools required are a
saw, hex key and tape measure
• Flexibility — Cast fittings can be used with galva-
nized steel, aluminum, stainless steel and black
iron pipe
• Reusability —Structures fabricated with
Hollaender fittings can easily be disassembled
and reconfigured
The Rib® Design . .
Hollaender®
Speed -Rail®
Nu -Rail®
Speed-RailO II
Rackmaster'
Mend-A-Raiie
Interne-Raile
Bumble Bee'
All are registered trademarks of the
Hollaender Manufacturing Company.
Call Toll Free; 8ee-772-8800 • www.hollaender.com
• Strength — Railing systems can be designed using
standard Hollaender products to meet any building
code. Please refer to Technical Section of Catalog,
www.hollaendercom or call our engineers.
• Time Tested - Products are backed by over 50
years of experience
Hollaender Isotopes the World'S best 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 -Rail'
Ideal for repairing broken welds on existing pipe
structures,
Speed -Rail' n
Patented modular fitting system which easily allows
for additions and changes to existing structures
without having to entirely disassemble.
Applications ape limited only by the imagination
Handrails & guardrails, playgrounds and carts,
store fixtures, offshore petro%hemical, industrial
plants, racking systems, warehouses, health &
medical buildings, portable structures, recreational
areas, amusement parks, film industry, government
facilities & public works, displays, and much,
much more.
Instant, Structures'

Cat 1A slip-OnFittings 2/16/04 12:39 PM Page 2
Your Handrail Source.
'nical HollaendeP Slip-01"I HUMUS
Speed -Rail®• Speed -bill 11 • Nu -Rail®• Rackmasteril
Gall Toil Fran: 800-772-0000 • www,hallaendercom
"The Fitting iith the Rib"'

OnFitr_ings 2/16/04 12:39 PM Page 3
I.P.S. Size
Item Number
3X
05020
1'
06020
1-1y
07020
�•
08020
22*
09020
I.P.S. Size Item Number
07030
w I-1i2° 06030
I.P.S. Size Item Number
Ur 05050
d 1 ^ 05050
Cali Tali Free: 800-772-8800 + vim.hallaeuder.eem
Your Handrail Source.
-
I.P.S. Size
Item Number
06060
0" >
¢r
1-ti4°
070fi0
"TheFiWW Kith theRib'"
I.P.S. Size Item Number
07080
08080
I.P.S. Size
item Number
3/4'
05090
1^
06090
1.1(4'
07090
1-1/2'
08090
2"
09090

Cat 1A Slip-OnFittings 2/16/04 12:39 PM Page 4
leftender.
Your Handrail Source.
h,
I.P.S. Sue
item Number
3/4'
05100
i
06100
1-114'
07100
N
I.P.S. Size Item Number
1.112' 10020
Components: (I No.7S8
pl Nn.2SB
I.P.S. We Item Number
3/4'
05123
06120
w
1.1/4'
07120
1-VT
03120
2"
09120
I.P.S. Size
Item Number
3/4'
05130
t°
06130
HAD
2'
09110
I.P.S. Size Rem Number
3/4° 05140
aw
1' 06140
07140
091.d E
Cali Tail Free:860-772-8800 • wwm.Aallaender.cum
NoittESideUlufefTee-E
' '
^
I.P.S. Size
Item Number
3j4'
05180
P
06160
1-114'
07160
1-112'
08160
'TherMngwiththe MY"
I.P.S. Size
Item Number
314'
05170
1•
06170
1.1 /4'
07170
1.1/2'
08170
I.P.S. Size Item Number
1' 06180
1.1/4- 07180
1.1/2, 68180

s;m'O
' Cat 1A Slip—OnFittings 2/16/04 12:39 PM Page 8
ra�^�
ellsendal.
Your Handrail Source.
z :d
,+ fA
I.P.S. Sfze Item Number
I.P.S. Size Item Number
08490
314' 05520
06520
Pj4' 07520
2" 096M
I.P.S. Size Item Number I I.P.S. Size Item Number
y
3/4' 05530
3/4' 05450
r
„� I° 06530
07450 1-1/4' 07530
f ' �� I-1l2' 08450 1 if 08530
2' 09530
W caps not included
1;;. ni t , n I , h '. r . I.P.S. Size Item Number I.P.S. $lie Item Number
I tj417150 1-tr2' 08540
1
¢ A 4.
Components: (11110.99C
" (11 No. 28S8
x .
Us. Size Item Number I.P.S. Size Item Number
314' 05600
rs Y° 06500 „ r i" 06600
1-114' 07500 a "' 1-1i4' 01600
n 1-112` 08600
2° 09500 Y 09800
Compnnenm (II30A
�; itl3oe
I.P.S. Size Item Number I . x, ' Y I I I.P.S. Size Item Number
m nem ir< ---
r
3/4° 05610
05510
1-Ile 07510 1-1r4" 07610

Cat 3a Flanges 2/16/04 12:44 PM Page 1
,9all
Your Handrail Source.
a'
flanges
Hollaender offers an extensive line of flanges for
e:: e
mounting handrail, guardrail, and other pipe structures.
These flanges are available in all the optional
finishes. Selecting the right flange becomes extremely
important in all handrail applications. To aid in the
selection process, please refer to the chart on the
following page, and dimensional drawings on the
subsequent pages.
Our engineering staff is available to answer questions
a
regarding the appropriate hardware. Concrete
anchors and machined bolts may be ordered to
complete the handrail system. Many applications
require toeptate. (Refer to Tech biformation 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 wob page at
wwwhollaendercom for additional technical support.

1"In
EL
P14 -A A
Sulzer Cherntech
Sulzer CompaXTm
The space -saving solution
.....................................
�7 Z7
4Z

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►rr�paX�M 1'echnOlOgy
Sulzer GompaXTm
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

0.0-
Main flo
I! ' Sulzer CompaX
Homogeneity data
® ,:2000
1:,00
• ,:20
0 2 4 UD I-1
Homogeneity curve measured at different mixing ratios
Calculation of the homogeneity with CFD (Computational Fluid Dynamics)
Pressure drop (©p)
The pressure drop can be calculated as follows:
Ap=0.015pv2
Ap = 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
1000
100
-- _
E
-
---
—
-
0,5 1
0,1 Velocity (misj
OR
:
.:Sulzer CompaXT'" �TecI�InQ�����
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

1
1
Headquarters
Sulzer Chemtech Ltd
P.O. Box 65
8404 Winterthur, Switzerland
Phone [phone]
Fax [phone]
[e-mail]
www.suizerchemtech.com
North and South America
Sulzer Chemtech USA, Inc.
4019 South Jackson Avenue
Tulsa, OK 74107, USA
Phone [phone]
Fax [phone]
Asia Pacific
Sulzer Chemtech Pte. Ltd.
10 Benoi Sector
Singapore 629845
Phone [phone]
Fax [phone]
Sulzer Chemtech Ltd, a member of the Sulzer Corporation, with head- The activity program comprises:
quarters in Winterthur, Switzerland, is active in the field of process engi- . Process components such as trays, structured and random
neering and employs some 2500 persons worldwide. packings, internals for separation columns and reaction technology
Sulzer Chemtech is represented in all important industrial countries and . Engineering services for separation and reaction technology such
sets standards in the field of mass transfer and static mixing with its as optimizing energy consumption, plant optimization studies,
advanced and economical solutions. pre -engineering for governmental approval, basic engineering
• Separation and purification of organic chemicals by means of
crystallization and membranes
• Mixing and reaction technology with static mixers
• Mixing and Cartridges Technology
• Tower field services
23.13,06.40 - 11.08 - 50 - Printed in Switzerland
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SIZE: 8 SCALE: 318W"-V-0'
pAw," OORPO AION WLL NOT 9E R6PONSHE
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DATE: 3-22-99 BY. F. J. CAMARGO CHECKED:
P. TATASCIORE
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DESCRIPTION
FOR RAW @iflD Y OMW AM
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PROJECT NUMBER: DRAWING FILE NUMBER: Ncvu
003758-01
PROJECT NAME SHEET NUMBER: 1
1 OF 1

NEMA Premium" Balder 5.0 horsepower totally enclosed, fan -cooled, electric
motors. Specifications: EM3615T
Catalog Number:
EM3615T
Specification Number:
36G271T031
Horsepower:
5
Voltage:
2301460
Hertz:
60
Phase:
3
Full Load Amps:
13/6.5
Usable at 208 Volts:
13.6
RPM:
1750
Frame Size:
184T
Service Factor:
1.15
Rating:
40C AMB-CONT
Locked Rotor Code:
K
NEMA Design Code:
B
Insulation Class:
F
Full Load Efficiency:
90.2
Power Factor:
80
Enclosure:
TEFC
Baldor Type:
3643M
DE Bearing:
6206
ODE Bearing:
6205
Electrical Specification Number:
36WGT031
Mechanical Specification Number:
36G271
Base:
RG
Mounting:
F1

RASCHIG GmbH
Mundenheimer Strasse 100
67061 Ludwigshafen - Germany
Phone: [phone]
Fax: +49,621.5618.604
email: [e-mail]
wwwxaschig.de
Locations/Production Sites
Ludwigshafen and
Espenhain, Germany
Houston, Texas
El Dorado, Kansas
Monterrey, Mexico
D URA -PAC crossflow and vertical
flow PVC sheet media for trickling filters,
submerged fixed beds and other
wastewater treatment applications
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 ft2/fV.
DURA-PACis a plastic sheet media
available in two basic designs. DURA-PAC
XF is a cross flow media recommended
for low to medium BOD loading
applications. DURA-PAC VF is a vertical
flow media recommended for high BOD
loading applications. DURA-PAC's
volumetric void ratios of at least 95% allow
for uniform redistribution of wastewater
and air while maximizing contact between
the biomass and the wastewater.
DURA-PAC is available in specific surface
areas of 30, 31, 48 and 68 ft2/ft3. 31 ft2/ft'
media is typically used for BOD removal
and 48 ft2/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.

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© Siemens AG 2008
-d tat ,g
Continuous level measurement - Ultrasonic controllers
Design
Technical specifications
Mode of Operation
Measuring principle
Ultrasonic level measurement
Measuring range
0.3 to 15 m (1 to 50 ft), transducer
dependent
Measuring points
1 or 2
Input
Analog
0 to 20 mA or 4 to 20 mA, from
alternate device, scaleable (6
relay model)
Discrete
10 to 50 V DC switching level
Logical 0 = < 0.5 V DC
Logical 1 = 10 to 50 V DC
Max. 3 mA
Output
Echomax6 transducer
44 kHz
Ultrasonic transducer
Compatible transducers: ST-H
and Echomax series XPS-10/10F,
XPS 15/15F, XCT-8, XCT-12 and
XRS-5
Relays')
Rating 5 A at 250 V AC, non -
inductive
Model with 1 relay2)
1 SPST Form A
Model with 3 relays2)
2 SPST Form A/1 SPDT Form C
Model with 6 relays
4 SPST Form A/2 SPDT Form C
mA output
0 to 20 mA or 4 to 20 mA
• Max. load
750 St, isolated
• Resolution
0.1 % of range
Accuracy
Error in measurement
0.25 % of range or 6 mm (0.24"),
whichever is greater
Resolution
0.1 % of measuring range or 2 mm
(0.08"), whichever is greater3)
Temperature compensation
• -50 to +150 °C (-58 to +302 °F)
• Integral temperature sensor in
transducer
• External TS-3 temperature sen-
sor (optional)
• Programmable fixed tempera-
ture values
Rated operating conditions
Installation conditions
Location
indoor / outdoor
Installation category
11
Pollution degree
4
Ambient conditions
Ambient temperature (enclosure)
-20 to +50 °C (-4 to +122 `F)
Siemens FI 01 • 2009
Weight
• Wall mount
1.37 kg (3.02 Ibs)
• Panel mount
1.50 kg (3.31 Ibs)
Material (enclosure)
Polycarbonate
Degree of protection (enclosure)
• Wall mount
IP65/Type 4X/NEMA 4X
• Panel mount
IP54(Type 3/NEMA 3
Cabe
Transducer and mA output signal
2-core copper conductor, twisted,
shielded, 300 Vrms, 0.82 mm2
(18 AWG), Belden 8760 or
equivalent is acceptable
Max. separation between trans-
365 in (1200 ft)
ducer and transceiver
_
`
Displays and controls
100 x 40 mm (4 x 1.5") multi -block
LCD with backlighting
Programming
Programming using handheld
programmer or via PC with
SIMATIC PDM software
Power supply"
AC version
100 to 230 V AC ± 15%, 50/60 Hz,
36VA(17W)
DC version
12 to 30 V DC (20 W)
Certificates and approvals
• CE, C-TICKS)
• Lloyd's Register of Shipping
• ABS Type Approval
• FM, CSANRTL/C, UL listed
• CSA Class I, Div. 2, Groups A, B,
C and D, Class II, Div. 2, Groups
F and G, Class 111 (wall mount
only)
• MCERTS Class 1 approved for
Open Channel Flow
Communication
• RS-232 with Modbus RTU or
ASCII via RJ-11 connector
• RS-485 with Modbus RTU or
ASCII via terminal blocks
• Optional: SmartLinxO' cards for
PROFIBUS DP
DeviceNetTM
Allen-Bradley° Remote 1/0
t) All relays certified for use with equipment that fails in a state at or under the
rated maximums of the relays
2) This model is level control only; no open channel flow, differential level or
volume conversion functions
3) Program range is defined as the empty distance to the face of the trans-
ducer plus any range extension
4) Maximum power consumption is listed
5) EMC performance available upon request

O Siemens AG 2008
.,= q`
Continuous level measurement Ultrasonic controllers
W=
a
Selection and Ordering data n
order No. �-Selection and Ordering data order No
Siemens HydroRanger 200 C) 7 M L 5 0 3 4- Siemens HydroRanger 200 C) 7 M L 5 0 3 4-
Ultrasonic level controller for up to six pumps that
fr
Ultrasonic level controller for up to six pumps thatMAN
provides control, differential control and open
at %,SiW N_
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
Wall mount, standard enclosure
^ sor;r =,
1 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')
3 text line, suitable for enclosure
TS-3 Temperature Sensor - see TS-3 on page 5/147
Power supply
A SITRANS RD100 Remote display - see RD100 on
100 to 230 V AC
page 5/263
12 to 30 V DC
B SITRANS RD200 Remote display -see RD200 on
Number of measurement points
page 5/265
-,
Single point model, 6 relays
A pa; e Pa,
Dual point model, 6 relays
B Power Supply Board (100 to 230 V AC) C) 7ML1830.1MD
Single point model, level only, 1 relay2)
C Power Supply Board (12 to 30 V DC) C) 7ML1830-1ME
Single point model, level only, 3 relays2)
0 Display Board C) 7ML1830-1 MF
Communication (SmartLinx)
See SmartLinx product page 5/260 for more infor-
r"r
q
Without module
0 mation.
SmartLinx© Allen-Bradley® Remote 1/0 module
1 --
ea
SmartLinx PROFIBUS DP module
2 i) Available with approval option 1 only
2) This model is level control only; no open channel flow, differential level, or
SmartLinx DeviceNetTM module
3 volume conversion functions
See SmartLinx product page 5/260 for more infor-
C) Subject to export regulations AL: N, ECCN: F-AR99
oration.
t
Approvals
General Purpose CE, FM, CSAusic, UL listed,
1,
C-TICK
CSA Class 1, Div. 2, Groups A, B, C and D; Class It,
2
Div 2, Groups F and G; Class III (for wall mount
applications only)
cf,pss' ns
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 number/identification (max. 16
«,
characters) specify in plain text
;s;iftt'.ft`r =r ;Ftr;e;era!
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 Militronics
manual CD containing the complete ATEX Quick
Start and instruction manual library.
SmartLinxAllen-BradleyRemote 1/0, English
C) 7ML1998-1AP03
SmartLinx PROFIBUS DP, English
C) 7ML1998.1A003
SmartLinx PROFIBUS DP, German
C) 7ML1998-1AQ33
SmartLinx PROFIBUS DP, French
C) 7ML1998-1A012
SmartLinx DeviceNet, English
C) 7ML1998-iBH02
Note: The appropriate SmartLinx instruction manual
should be ordered as a separate line on the order.
Siemens FI 01 2009
k

(9 Siemens AG 2008
gg
Continuous level measurement - Ultrasonic controllers
_-
�y �4 �
Selection and Ordering data
Order No. Selection and Ordering data Order No.
Milltronics HydroRanger 200 C) 7 M L 10 3 4- Militmnics HydroRanger 200 C) 7 M L 1 034
Ultrasonic level controller for up to six pumps that
Ultrasonic level controller for up to six pumps that
provides control, differential control and open
u
provides control, differential control and open
channel flow monitoring. The HydroRanger 200 is
channel flow monitoring. The HydroRanger 200 is
available as a level measurement controller
also available as a level measurement controller
only. Select option from model code below.
also
only. Select option from model code below.
,.
Mounting
Wall mount, standard enclosure
Acc, s_-;ork� r
1 Handheld programmer 7ML1830-2AK
u`ii
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 mounts)
3 text line, suitable for enclosure
"""'r.
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 5/263
SITRANS RD200 Remote display - see RD200 on
Communication (SmartLinx)
page 5/265
•- a
Without module
A
SmartLinx' Allen-Bradley Remote 1/0 module
B
SmartLinx PROFIBUS DP module
C
SmartLinx DeviceNetTM module
R
See SmartLinx product page 5/260 for more infor-
mation.
4 p'
Mill
Approvals
General Purpose CE, FM, CSAusrc, UL listed,
1
.,
C-TICK
CSA Class I, Div. 2, Groups A, B, C and D; Class II,
2
Div 2, Groups F and G; Class III (for wall mount
applications only)
Number of measurement points
Single point model, 6 relays
1
Dual point model, 6 relays
2
Single point model, level only, 1 relay2J
3
'o
Single point model, level only, 3 relays2)
4
r"'czrtf •r curs? r<<s
Order code
Please add "-Z' to Order No: and specify Order
code(s).
�00'
Stainless steel tag [69 mm x 50 mm (2.71 x 1.97")]:
Y15
Measuring -point number/identification
(max. 16 characters) specify in plain text
/rn'shi"c'fhx? !.;antra=
Order No.
English
C) 7ML1998-1FC08
g
French
C) 7ML1998-1 FC14
German
C) 7ML1998.1FC34
Note: The instruction manual should be ordered as
a separate line on the order.
a
This device is shipped with the Siemens Milltronics
manual CD containing the complete ATEX Quick
Start and instruction manual library.
"q
SmartLinx Allen-Bradley Remote UO, English
C) 7ML1998-1AP03
SmartLinx PROFIBUS DP, English
C) 7ML1998-1AQ03
SmartLinx PROFIBUS DP, German
C) 7ML1998-1A033
SmartLinx PROFIBUS DP, French
C) 7ML1998-1AQ12
j
SmartLinx DeviceNet, English
C) 7ML1998-1BH02
9
Note: The appropriate SmartLinx instruction manual
should be ordered as a separate line on the order,
Siemens FI 01 2009
Sp -ore pa�s
Power Supply Board (100 to 230 V AC) C) 7ML1830-1M0
Power Supply Board (12 to 30 V DC) C) 7ML1830-1ME
Display Board C) 7ML1630-1MF
See SmartLinx product page 5/260 for more infor-
mation.
1) Available with approval option 1 only
2) This model is level control only; no open channel flow, differential level, or
volume conversion functions
C) Subject to export regulations AL: N, ECCN: EAR99
'Modbus is a registered trademark of Schneider Electric.
QBelden is a registered trademark of Belden Wire and Cable Company.
OAllen-Bradley is a registered trademark of Rockwell Automation.
TMDeviceNet is a trademark of Open DeviceNet Vendor Association (ODVA)

© Siemens AG 2008
..
Continuous level measurement Ultrasonic controllers
Schematics
_--'1 I imensianai drawings
Wall Mount Version
14.9 mm ifi.3 mm 91 mm 6.6 mm rs1
+ (0.58") 6,325" mounting 3.58"
15.21 m 130mm— ►� holes ( ) (0.2&") rez !n
0.6 5.126 I 04.3mm (m - 1 ®® ref Q L?m.0 1�1
( ) (O.t7") (x4) _� ^ rea
r, ® + T See note 1
0 1 .i. SYNC
O
i +S 12.30 V r
cover'.:. 240 mm 1 DC.versron
o crews. (9.45') ® RELAY 1.
�n R
qa ou7vuts _ .�
i3 �f JRE4AY
QQ RELAY 3. !'+'
rq -
* ---� housing 5m
Suitable: location for :
mounting screw.
conduttengances ® SRELAya F
}(provided by customer) osoREre f��fztt,I
SlemenB.M-lltronics mountingholes �RELays Nwrs GIB
recommends using a hole, (acgessed under lid)
-� punch for dulling the holes. (O j .3 vim (0.17") ®
RELAY 4 R568 A
Panel Mg6rit Version ' S Relays shown m releasedstate
198 vim' 97 mm
(7 80) 36 m
Notes
(140)2-core capper wire twisted wdh shield for expansion up to 365 m (1200
f
0 o
Route ca 46, m grounded metal condwt, separate from other cables,.
y 2 UeriJy that all system components are installed m accordence with instructions
It onned all cable shields to the HydroRanger 200 Shield Connections Avoid differential
ground potentials by not connecting cable shields to ground (earth) anywhere else
278 min 4 Keep eXPpsed conductors o shielded cables as short as possible to reduce noise
0.004") e • on the tine caused by stray transmrsswns and noise pickup.
-ntiA HydroRanger 200 connections
o
HydroRanger 200 dimensions
Siemens FI 01 • 2009

'ry

I'llh-tisolli S;
for naltilstrital app'lic,
A It,
A 1
tJL-941�lT Irsomin: I eNA'ALIF V1411di'mg

j
SPECIFICATIONS: ECHOMAX° NON -CONTACTING ULTRASONIC TRANSDUCERS
Model
Min.Range
Max Range
BeamFHeAica.11y
Angieouing
-3dB
XCT
Foam
Facing
Opt.
Foam
Temp.
Rating
Built in
Temp.
Rating
Temp.Range
Celsius
(Fahrenheit)
Chemical
Immunity
Rating
Thread
Size
FlangeA
Mount,
Opt,
Freq.
kHz
(nom.)
Weight
Kg
(lbs.)
M
Ft,
M
Ft.
THE SURE SHOT XPS SERIES
XPS 10
0,3
1
10
33
12°
Kynaro
(blue)
J
95°
(203°)
Yes
-40° to 95°
-(-40° to 203°)
Excellent
1" NPT
1" BSP
4
43
.75
(1.65)
XPS-15
0,3
1
15
50
6°
Kynar©
(blue)
95°
(203°)
Yes
-40° to 95°
(-40° to 203°)
Excellent
1" NPT
1" BSP
43
1.28
(2.81)
XPS-30
0.6
2
30
100
6°
Kynar®
(blue}
95°
(203°)
Yes
-40° to 95°
(-40° to 203°)
Excellent
lT/2,.
BSP/NPT
Compa
tible
4
30
4,14
(1,12)
XPS-40
0,9
3
40
130
6°
Kynar(
(blue)
65°
(149°)
Yes
i
-40° to 95°
(-40° to 203°)
Excellent
22
7:9
(17.4)
THE HOT SHOT XCT SERIES
XCT-0*
045
1,5
8
2.6
12° :
Kynar®
(white)
—
—
Yes
-40° to 145°
(-40° to 293°)
Excellent
1" NPT
1" BSP
43
.75
(1.65)
XCT=12*
0 45,'
1,5 _
.' 12
40
.6°
Kynar :
(white)
—
—
Yes
-40° to 145°
( 40° to 293°)
Excellent.
1" NPT
1" BSP
43
1.28
(2.81)
THE LONG SHOT XLT /XLS SERIES ■
XLS, 30
0 9
3 •.
30
1'00
5°
Alurrilnum
Yes
-40° to 9lj
Falr
1 NPT
22 :
4.4
(9.7)
Grey;
(-40° to 194°}
XLS 60
1 8 '
6
60
200
5°
Alurimum
Yes
40' to 90°
Fair
1" NPT
13
;. 6,35
(14.0)
(40° to 194°)
XLT 30:
0 9
3
30
100
5
Alltlnmum
Yes
40 to 150p
Fair
1 ".:NPT
`
':Red::
,
.
XLT 60
1 8
' 6
60
20Q
5
Aluminum
Yes
40 to 150'.,
Fair
.`
1" NPT
13
6,35,
(14.0)
Cted
(-90 to 300°)
_..
A All
.r,nrlolc ran
ha hlinrl
Hanna
mnttnted.
Note: Effective maximum range capanu¢y may vary aepenutny un dppN—MI. t 1, 1..,,...,r.....•
Our continuous program to improve products may result in changes in design and specifications without notice,
For XRS-5,'XKS-6, XPS-1 Of: see Technical Specification Sheets:
ECHOMAX® SERIES APPROVALS
CENELEC EEx m II T5: XLS Series. EEx m 11 T4: XPS Series.
EEx m 11 T3: XLT & XCT Series, TS-1
CSA Class 1, 11, Div. 1, Group A, B, C, D/E, F G. Class 111.
FM Class 1, 11, Div. 2, Group A, B, C, D/F, G. Class III,
FM XPS 10115: Class 1, II, Div. 1, Group A, B, C, D/E, F, G.
Class III.
CSA. FM. TS-3 Temperature sensor: Class I, Div. 1, Group C & D.
Class II, Div. 1, Group E, F & G.
NOTE XCT-B, unfaced only, CSA approved.
CONDENSED APPROVALS LiSTiNG, CONSULT AGENCY APPROVAL GUIDE FOR DETAILS.
Representative
■ Polyester covering is standard.
Milltronics versatile tine of sophisticated Ranger TM transceivers provree rename never corn
trot in a single vessel or a multiple tank farm.
.f i.rii':ijlii- I?riC 4'P. f.lE$t )i}Let !,Inver).
f 954 t,.cnro,n9y Dr.. P D. B. 422.SLP:Sn,mnouyn. Onn. Canada 1:91 /81
11 -1 /05]4SG•131 Fax:-11QS ld1U466
-• V 182 Nannnnby Rd.. Bnx J3B. Snun Mc11m,u,w. 3205. Australia
g+ IN.-0115139F95240fi Fnx-+U1161396952M1611
Fc �X Typos, Tan de �- tni•32(01332W6ic4i56,n5,41 2100 nr-ur F aM, 3Z(0 )332G 0mS 2
•LL4 .. Cnazury liouzn.. Bri4ywnc, Roan, Wurrns,er. E191aad Wi'4 9ZQ
f<:1--041305450500 Fax:•4, 106S,6Q501
Prvc na to Salina Virac,rr.. Bat 5. 135901Ac'—, Fransc
tat..Sa 4 42 6169 M Fax: [phone] lit 95
VJnrnsnasve 41. D40549 Guz l '. Cie —y
•49211W25025 Fax:•492t1 i626830
1 lint W-,n S' a .Sync 602, Quauy Bay. Hong Kong
•011 A6228663166 Fax. •Q� i 0s228562982
Am '," No. 1155. Co' ".' _"_ 031Q0 tAax,cr. G F.. Muxic°
ici-.-5255l5:12fl Fnx-52561S2u 86
N1., n nsa, 10. N 4S23 AS Bran.,. The Nn111°11ands
td.: -J t0)Ib 12 1 5­12 ax'. -n t(p11G 54L A 512
/09 S;ad 0! nine; 1 U.S.A.
Ii,Ut i
Ic4.: •1311))1. '4:i Far: r8r][1).38'14
A joint v°niura in Singapore, n Tales °ffiea in Brazil and
diziri6ulars in B6 cawrlrias.
35751080NA 35751082 A4 ba-1
Pmm�d in Canin.=.

WALLACE &TIERNAN
ENCORE"' 700
DIAPHRAGM
METERING PUMP
SB.440.400.GE

rar'g
MORE APPLICATIONS, MORE BENEFITS,
MORE FEATURES ... MORE PUMP
ENCORE' 700 DIAPHRAGM METERING PUMP
Ilydlaulic diapbrvgm pumps am renowned foi- their dcu'abillty, but start -Lip and
rnainternuice can be laborious, partiarlar/y sihen service regcrirrr purging and replacing'
Intermediate fluids. Additionally, ntrtny designs' zuc? very s'c'nsilille to Ch8f7ging.S'lIdion
conditions•. If urrdiaglansed, blocked m-s'turved suction can lead to lridraulic overfill and
su(xsegc.rent dhaphragrn failure.
Me'clronical diaplu'agin pumps are. Jar less sopliisticaled. Star't-trp and .service suer
typically touch aarronther since there aiv no messy internredleMe fluids, internal relief calves
of hydrar.dic rely]] cire'uits to tamper with. &jt, unal n0 y,, ineclra.nical dlaphragm pumps'
haven't shoed lbc bydiauNc diahhragrn purrip's'.rc:putarion .for robustneis•.
Welcome to the &cOr'e"I17O0 admnti3,te...
• A whole new class of metering pine{...
combines the robust ness of hydraul. .
diaphragm drives with the unparalleled
ec:onocny, sinniplicity ami serviceability of
mechanical diaphragm hquiri ends.
" i-'Iamlies capr.iciu..,s to 2,400 1/is,
hack pressures to
• Non -loss motion {arrrplit.urle mo(.1ulation)
stroke adjust meCharlisrn renders unrivaled
efficiency, longevity and reliability.
• Ckioice of two field convertible drives.. -
direct. coupled ur pulley coupled, for an
ac:iditional 4:1. tltrndQ A n on stroke frequency
with a standard induction motor,
• Precision et tgineered liquid ends meter' mild
solut.inns, aggressive chernicals, high viscxrsity'
polyrners and slurries with far greater
r1'13riency than conventional liquid ands.
• Clear f. Vc cartridge valves fix• last, roolproof•
sea -vice with no piping disturbances and
built-in visual indication of operation.
• Jln+miij n diaphragm design ensur"i high
metering ac:ci.n'ac.y; even at varybig discharge
pi'essure5.

I=t
TYPICAL APPLICATIONS,
_ _ 'lyp.ical lnduslries Typiarl Applications, Metering & PlUnping
METERING AND PUMPING
4 VVater and Vda+tewater C;oagi.dants, oxidising agents, disinfectants, corrosion
Tre.ahnent inhibitors, chemicals for taste, odour and pli control
FULL MECHANICAL MOVEMENT
AMPLITUDE MODULATION ADVANTAGE
$wirmning Pools
Food Processing
Chemical Processing
'?� P
a
Brewing & Distillation
*[
Agriculture
Acids, caustics, disinfectants and oxidising agents
Bactericides. algaecides, acids, caustics, detergents,
corrosion inhibitors and luhricants
Additives for petrochemical., I: ilannarei.rtical,
pulp and paper, plastics and textile manurarl:ure,
Filtration and fermentation aids, bactericides, acids,
caustics and detergents
Fertilisers, herbicides, pesticides and
food supplernents
Metering pump rnanufacttarors generally use
one of three diaphragm actuation methods.
Solenoid Pumps,
The rnust simple and economical type of
pump, these provide a pulsed flow with huge
pressure spikes, considerable noise and wear.
Lost -Motion Purnps.
These motor driven pumps are. higher in
capacity Lhan solenoid pumps, but also give
rapid acceleration to the liquid at rest in the
pump head due Ln non -continuous
ciiaphragm rnotion.
Non I.,oss Motion Ptunps.
The diaphragm is driven by a .rotating
crankshaft, where the eccentricity can be
smoothly adjusted during operation. There.
are no return spri.rigs, and the diaphragm
moves with simple harimmic motion. The
Ruld velocity proflle is sinusoldal at all stroke
lengths, adjusting stroke length simply niters
Lhe amplitude of rite sine Wave. This design
provides reliahility and longevity, and pump
valves operate with jar greater efficiency.
This graph shows the velocity profiles for each pomp type. For any given output, the areas
circunvscribed by each curve are identical. Note the difference in non -loss -motion designs.
Encore' 700non-loss .:
in
motion mechanical
`tR
diaphragm pump
s
suit raid, :`
lost motion
s —
utti "�' =i_
p.t.: .
pump
'—
su nun .
SirOi<C .
1 suction_
� __ slrnke
Time Scale

ENCORE® 700 DIAPHRAGM METERING PUMP
``;
ve.re-eery rneered.tlTe.Encure�Tr70 um irrcp o<<i(u1 ail oirr:r;':.°::
�:�,
,„:'':.-.,._�—^.;.s:,•_,.�.`�.:.:
fv�izFte'fPatures!N tth, many liew attntrutes lyplcal y faundton an.Yr:<: c':.:'n...
.::.....:..:.......:.......
,..
mast nred hyrliatrLc diaphragm r%slgru, ,'1 he result is a mechanrtal":.
diaplriagra pump thats unrivaled f rabustnese, economy, simplicity*
L
and set v�cca1111ity Na naattei svfiai yvvi. aoliilcatinn, EnmrerD 700 rxan.
�ri t .-
1landleit,lvitli.ease..:.::r.:...:i:;::::_._:-.>,::':>.,..:.:..
?x
Available with standard induction and variable speed motors
(optional) for wider operating ranges and automatic process control,
Short suction and discharge
porting minimises friction losses
and cavitation, improving
hvdraulic characteristics and
providing far more e.ffrcient fluid
metering than conventional
liquid end designs. l
Our premium composite \
diaphragm is manufactured to \\
stringent specifications to ensure
tong life even under the most
demanding applications.
The design incorporates tcflon-
facing, for the. highest degree of
chemical resistance and nylon
reinforcements, all bonded to a
prc-formed elastomcric support.
�Ve've added convolutions for
unconstrained rolling aebon, ""•��
a steel backing plate to assure
volumetric accuracy even at varying
discharge pressures and an o-ring
groove in the head's diaphragm
cavity for complete sealing.
Higlt precision guided ball -and -scat clear
PVC: cartridge valves (except 165inni head)
provide built-in sight flow indication and fast,
foolproof service. The design includes wide
flow patlis and four -point guides to control
ball rise and assure proper seating. The valve
housing is compression sealed to the pump
head and pipe cormectors by o-rings and
removes easily for service or replacement.
A secondary diaphragm seat
c.onipletcly separates the ptunphead lion)
the drive unit: This double. diaphragm /
isolating design eliminates the risk of
cross -contaminating gearbox lubricant and
Process fluid.

Available in two field convertible
drive arrangements: direct chive or
pulley drive For an additional rl',l.
rangeabiFiiy on stroke frequency with
a standard induction motor. When
the: pulley drive arrangement is
ronlbined with a DC variable
speed motor, total operating
turndown call be as high as 800:11
With double simplex
capability, two drive units,
each with independent
capacity control, can be
multiplexed For blending
applications or future
proces, expansion.
This robust mechanical assembly features liberal use or heavy duty
parts including an epoxy -painted cast iron gearbox For superior
corrosion resistance, 316 SS fasteners, load absorbing tapered roller
bearings, robust gears and steel and nodular iron drive components,
C3btain precise and highly repeatable feed rate settings avith a
10 turn tnicrutnetcr-type stroke length adjuster.
!J� A percent scale and vernier Indicate stroke length in
increrxients. Feed rate is infinitely acl3u.st�ble from Q to
Automatic: capacity control via stroke length is also available.
Art optional diaphragm leak detection system senses the early
stages or diaphragm failure, The. system consists (iF a soli -state:
electro optic sense)r that mounts to the liquid end and a 1.P 65
control box. This box, which can be inounted at the pt.rmp, nr
up to 30 metres, can monitor twa liquid ends, LE1�'s and a relay
provide both local and remote indication of t'ailure.
Plerbn-nptir sensor

1
ENCORE@ 700 DIAPHRAGM METERING PLUMP
MANUAL AND AUTOMATIC Automatic Stroke Length Control
STROKE LENGTH CONTROL
Tile Encore+}'100 metering primp can be
controlled by varying the stroke length or
stroke frequency, The following control
schemes are available:
- Nijanual or 1Zemote Nlanual Control
Start -Stop Control where the motor is
wired into the circuit of a transfer pump.
switch, timer or controller
- Flow Proportional Control from a single
process variable.
- Residual, Compound Loop or Setpoinl
Control using one or two prixess
variables
Manual Stroke Length Control
A ICi turn micrometer gives continuous
read rate adjusunenl over a 10:1 range. A
percent scale and vernier Indicate stroke
litrrgth srttir'rg to 1 part in 400. F,ach
revoiutinn of the knob changes feed rate by
10%n. Stroke length is infinitely adjustable
from 0 to 100%.
For automatic capacity control via stroke
Iength, our new IP 65 actuator is used in
conjunction with either of two new process
variable controllers. The compact, fieLd-
retrofittable actuator easily installs on the
pump and features local manual override
and a window for clear indication of stroke
length. Two new microprocessor -based
controllers are available:
SCU, Signal Conditioning Unit
The economical SCU gives automatir
process control in
response to one
process variable,
typically flow
rate. Housed in a
IP 65 enclosure,
the SCU features
an 8-character
alphanumeric l..,CD display with 6-button
keypad and rrie'ntl-driven open tar prompts
for simple operation, setup and calibration.
Input flow scaling; and output dosage
adjustment. allow independent scaling; from
10 to 4009/6. Svc publication `.t 140.100GE
cure snore details.
Variable Speed Control
For precise and accurate feed rate control
via stroking speed, an SCR Drive Unit
varies the speed of a DC pump motor.
Stroke rrequency earl be. regulated manually
by potentiometer setting. or automatically.
via a 4-20 mA process variable input signal
(optional). Closed -loop speed regrrlatfnn
provides feed rate control accutafo to 1°fo of
full scale. With conLhtuoUs adjustment over
a 20:1 range, total operating turndown
with water -like solutions is 200:1 on direct
drive units, 800:1 on pulley drives.
Dosing or scaling of a process variable cats
be accomplished liy means of an SCU,
Signal Conditioning Unit used in
conjunctiorl with an SCR drive. For more
complex control, a PCU, Process Control
Unit can be used to provide setpoint
control in response to two process variables,
such as plant flow and chlorine residual.
PCU, Process Control Unit
The PCU is a full feature setpoint
controller. It provides automatic process
control in response to Lwo process inputs,
typically flow rate and chlorine residual.
The PCU can operate in any of four
different control modes Including residual
Feedback, compound loop, dual signal feed
forward (for duchlorination) and flow
.r:.:.: .._ proportionaL. In
-i addition, the
PCU Can be
i configured for
"center zcrci
operation in
�:'..compound loop
mode when a
DEOX/20001' Dechlorination AnalyLcr is
used. Housed in a 11' 65 enclosure, Lhe
PCU features a large alphanumeric display,
an LED bargraph to indicate flow input or
actuator position in S% tncrernents, a 6-
button keypad and menu driven operator
prompts for shnple operation, setup and
calibration,
I of more information request publication
'17140.200GE.

TECHNICAL INFORMATION
CAPACITIES AND DISCHARGI,,,RESSU
Sh.SURES
$D I -fa 1460 RPM
(t",)----1is
C."ueLllnncUiapluagn,
snake
C'apaci,y'
pulley
IM
list'aois
S�ruvl}
I'li,bingll1,n)
.55 ia7S):ill
IAI
3.r.3
t
12-
35
60
'2.1
79
I
12R!�;(`A�Ifix120
4.2
15.9
1
1'l.4y'
l7p}44
5.0
18.9
1
12
5.0
22.1
I
l-
50
60
10.0
44.2
1
12 - -
[;KM.
120
20.0
89.0
1
12. - -
7 oi..))
_
144
24
106.0
i
12 -
an
9.4
355
1
11) - -
75
60
18.R
71
IN
31:5
141.9
!44
45.0
170.3
1
- 10
30
16.0
60.7
1
9
I01)
60
32.1
121 A
1
- fl -
R'q
120
64.2
2421
1
- - 9
[44
77.0
291.4
1
9
30
37.5
141 �
1
5 '
125
60
75.0
28M)
1
- 5 -
Rl
IN
150.11
567.A
I
- - 5
1.14
1A0.0
681.3
30
6G0
M0.0
1
3
165
IiU
13'2.0
a20.6
1
- :i
RI Y,
121
11f4.0
1041.0
1
- .. 3
1-14
317.0
t25DA)
a
'Re4ecn simplex 1spat0y, doubla•s!ntplex arrangemears must be co01gured with same stroke.frequent' on both liquid wi&.
`°Fcv pulley art,,, :vra,gun,enis, n,paci0es Ihlcd ;vc fur pulley ste}r L. Capacities For steps2, 3. and 4 are'75`;;:, $0% nixl'2594,
respc'0vrly.
Accuracy
Repeatable metering accuracy is t 2% of
roll scale, at constant hydraulic conditions,
over a 10:1 operating range.
Stroke length
Liquid End .S17r 3.5 and 50nu77: 4.8rrv77
(0.1.881.
Llr. wd Fnds ,97r. 7.5, 100, 125 and
t 65rrun.' 9.6mnt (0.3751,
Feed Rate Adjustment
Feed rats is infinitely adjustable from
0 through 100%, A percent. stale and
vernier indicate stroke length seitiiig in
0.25`%, increments. Tach revolution of the
kriob changes stroke length by 10°yr,.
Operating Range
Dirrer Drive Aj-rvnyrnh 171:'
Stroke length is adjustable over a
10: l range; stroke frequency is adjustable
over a 20:1 range (using an optional
variahle speed drive). "l'otal combined
tykaximum operating torridown ciin be as
high as 200:1. Above 100:1 continuous
turritlown, total available operating range
should be evaluated against specific
chemicals being metered.
pfdley Drive lirraagrr77ent.'
Stroke length is adjustable over a
10:1 range; stroke Frequency is acliustable
over an 80:1 range (using an optional
variable speed drive..). Till cnttibined
maximum operating tut-ndown can be as
high as 800:1. Above 100:1 continuous
turndown, total available operating range
should be evaluated against specific
chemicals being metered.
Speed of Response
Automatic stroke length control response
time is L00 seconds from 0 to 100%.
Valiable speed control response tirne is
under 3 seconds Froin 0 to 1009/b.
Suction Lift
The plinip will self prime with 3 metres of
water suction lift (wetted valves, zero back
pressure, full stroke and speed, waterlike
solutions), Once primed, tide pump will
operate with 3 metres of water suction lift_
Flooded suction is recorrunended.
Weight and Shipping Weight
Singlr,rLnplr..r 50 kg, fi0 kg; double shnplex
73 kg; 88 kg. For arrangements with
automatic stroke length control add
5.5 kg; 7.3kg.
Temperature Limits
With l'1JG liquid cull' atnbirnf terrlperatl.u'es
from 2-52'C:•, process fluid temperatures
LIP to 5?,' .
141io 1(ynarlkrrrld liod'process fil.lid
temperatures up to 62`C.
(.[ethnical Inibrtrialion continued on next
1."p-)
leflan, Hypslor, sod VO.on arc reyisrenaE trader;arks or
El. Dupont. Cdl.

I
Electrical Requirments
Standard induction motor arraugrnent is
1450 rpm, 115/230 Volts, 50Hz, single
phase, TUC. Motors with other electrical
characteristics are available as an option.
Diaphragm leak detector requires It 5/230
VoILs, Relay rating 5 Anifs @ 250 Volts, 30
VDC. 1.P 65 enclosure. Variable speccd drive
control unit requires 11.5/230 Volts, 50/60
Hz, Single phase., 200 mA (l'1.5V, 1.00 mA
(230V). Automatic stroke length actuator-
( atarnr contact's (high, low, actuator
disengaged) N.O., rates! 5 Amps @ 250
Volts.
Materials of Construction
C e ar box and liquid rnd adapPCr; epoxy
painted, cast iron
Stroke positioner enclosure: epoxy Painted,
cast. aluminum
Punap head' PVC or PVDF
,%lion and discharge valor, housing- clear
PVC, grey PVC or PVDF
valve bal(r; 316 stainless,'TFE, ceramic,
glass and polyurethane (for sherry service)
halve orals: Itypalon and Won
DiaphlClgl7l:'1•F.E-faced, fabric. reinforced,
elastnmer backeci, with a steel or cast irots
backing plate
M01111ting bux (apuonal).: ABS
The putrip is UV risistanl'
Due co continual product devetnprrsenr. and
in:prnveiuenL cer7ahi s1.uTc1i'icatiom May
chnngo without prior anrunmcernent.
ENCORE 700 DIAPHRAGM METERING PUMP
Polymer and Slurry Handling
Capabilities
Polyiner solutions at. viscosities LIP to 5,000
cps at. 144 sprn. Viscosities measured with a
Brookfield Viscometer with No. 2 spindle
at 3 rpm,
Hydrated lime slurries up to 0.38 kg per
litre of water, activated carbon slurries op
to 0,11 kg her Titre of water;
cliatomaceaus earth slurries up to 0,17 kg
per litre of water.
Chemical Metering Systems
Lowy cost packaged systems can be custarn
configured frorn standard stork
components including tanks, rnixers,
instrumentation and a wide range of
controls. All systems are shipped assembled,
prewired and ready to install. Ow'
comprehensive range of co-ordirnuted
accessories provide the ability to produce
the best possible irstallation.
Accessories
Choose rrorn Back Pressure Valves, Fressurc
Relief Valves, Antisyphon Valves, Whi-
Lunction Valves, Main Connections.
Strainers, Pulsation Dampeners,
Calibration Chambers, Solution'lanks,
Mixers, Liquid Level Switches. Slorr.y
FLushing Systems and nurnerous Mrnunting
Ar.;essories,,jtlst to name a lew.
PM Kits"
Preventive Maintenance kits contain
original Wallace & Tiernan replacements
ror those parts most susceptible to wear.
They facilitate .scheduled maintenance and
help maintain equipment in good working
order, eliminating equipment breakdowns
and costly downtime.
For further technical information see
publications:
Ti.440.400.GE &
Ti,440.400.2.GE,
TIEFINAN
Cltentfeed Limited
rnriary Works
'Rnib idgc Keiit `I'.N H 0QL.
Trleplione: [phone]
Fax: [phone]
Ti;1a11; trtforlrlL�tt�ai;�rrr.-trenlau7.rnn1
h1tp.��4Yt7'iV.7-Vi31%C.C-t1Y-171c111. L'O11'1
07i02

02/ 09f 2 0oe 19; 21 7658273669 TEC INC PAGE. 02
TEC. Inc.
bFMAM;A 11VN%`)
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 insta tied In the discharge air
stream to prevent damage.to positive displacement blowers
when operating pressures exceed the maximum pressure
rating. of the blower.
As the system pressure approaches the valve set 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 -stored, the valve
automatically returns to the origlnai set position.
The valve cylinder and seat are constructed of cast iron and
accurately machined to very tight tolerances for smooth
operation.
Removable weights have been carefully designed to permit
accurate pressure settings in J: PSI increments.
Adjustments In the relief setting can be made by adding or
removing weights.
D1MENSIMS
ji
c
OPEN
SIZE
A
8
C .
.0
E
Wt. (Lbs.j
1^
1.0" FPT
4.19
4.75
2.00
6.00
5
1.5" FPT
5.81
6.44
2.63
8.13
to
2-1l2"
2.5" FPT
7.63
8.88
3.63
9.88
25
PFEFO—EM_A —GE
c1 nui QnTinir _ rFArt lfiR l= P. 1d_7 PS1A1
�A
P!P£ TAP
VALVE
SIZE
-- - 'SET PRESSURE - PSIG
1
2
3
4
5
6
7
8
9
10
1"
19
40
60
80
100
120
140
160
165
206
!2"
39
80
120
160
205
245
285
330
370
410
2-112"
119
240
365
490
620
740
865
1000
1125
1260
TEC, Inc.
3594 S. CF2. 350 E.
Connersville,,IN 47331
PH: [phone] i=X: [phone] SWLI 199

..., r_-Co nCn CAIr)l
-,.A., !
1--1=1%ll:MAI ntmr-KISIONS FOR STYLE 5002
1
1-5/8
=2-".
4-7/8
6-1/8
3-112
1.315
4
5
6
7
4-1/2
5-9116
1.1 /4
1-1/2
3.1 /2
4
1.660
1.900
2
2-1/4
6
.8
6-5/8
7.1/8
4
2-3/8
2-3/4
8
10
8-5/8
9-1/2
!2
5
2 7/8
3-1/4
10
12
10-3/4
11-1 /2
g
5.1/2
3 1/2
3-7/8
12
14
12-314
13-3/4
ALL DIMENSIONS IN IIVt;Htt, STANDARD MODELS &'MATERIALS
0:0
5002-AL
Aluminum
Aluminum
50
5002-SR .
Brass
Brass
150
5002-304
304 Stainless Steel
304 Stainless Steel
150
5002-316
316 Stainless Steel
316 Stainless Steel
150
5002-Class A
Steel
Aluminum
150
5002 Class D
Steel
Cadmium Plated Steel
150
Standard Elastomer: Buna-N
nP71nAIAI MATFRIAL SELECTION
MATERIAL
'TEMPERATURE RANG
• Buna-N
—60 to 225° F
+ Neoprene
—40 to 225° F
• Butyl
—65 to 325° F
• HYpalon
—20 to 300° F
•' EPOM
—40 to 350° F
• Viton
—20 to 400° F
+ Teflon
—20 to 460° F
• Silicone
—100 to 500° F
d
—40 to 225° F
'Non stock item —Available upon request. • FDA Approve
White Neoprene
,� �yy � ;,xw�,aai,�•.. '"This temperature range is for genera! guidance. The
• 304 Stainless Steel figures may vary with application.
316 Stainless Steel
Monel and Inconel springs available upon request. CONSULT RATTING
PRESSURE RANGFOR MATERIALS, SIZES AND
S NOT SHOWN.
• COMBINATION END CONFIGURATIONS ALSO AVAILABLE.

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.

ompany: Aqueonics Recirculation Pump Selection
4 ;%�� -/ �r%� e
16@0 HYDROMATIC
a e: 10/5/2008 F i�JI �7 �"`/` f ���
dump:
Size: 30MMP
Type: Self-Primer3
Synch speed: Adjustable
Curve: 30MM2000
Specific Speeds:
Dimensions:
LAO
,,_;,,Pump Limits:
Temperature: 140 °F
Pressure: 125 psi g
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% @ 180 US gpm
NOL power.
2.66 hp @ 180 US gpm
i
Search Criteria:
Flow: --- US gpm
Head: --- ft
Speed: 1200 rpm
Fluid:
Dia: 8.4062 in
Water
Temperature: 60 °F
Impeller:
Density: 62.25 Ib/f?
Vapor pressure: 0.2563 psi a
Ns: ---
Viscosity: 1.105 cP
Atm pressure: 14.7 psi a
Nss: ---
NPSHa: --- ft
Suction: --- in
Discharge: 3 in
Motor.
Standard: NEMA
--- hp
Enclosure: TEFC
Speed: ---
Power: -- hp
Frame: ---
Eye area: --- in'
Sizing criteria: Max Power on Design Curve
90
40 8.4062 in 80
30 --
d
= 20
10
0
20
40
60
80
100
120
140
160
10::
,
5
2
N
a
z
0
20
40
60
80
100
120
140
160
3:
Q. 2',
- 70
60 u
c
- 50
W
__ -- 40
30
20
10
160 0
180
s
d 0'; 20 _ 40 60 80 100 -120 140 160 180
US gpm
Performance Evaluation:
Flow Speed
Head
Efficiency
Power
r
US gpm rpm
ft
%
hp
ftNP
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
" `H2Optimize Hydromatic 8
Selected from catalog: Self -Primer Pumps 60Hz Vers: Feb 2006

Z D
MEIN
28'
no
OXIMER
IMIM
No
4'
20
IS
MIN
MEN■ME
MEN
M
IM
IN
MIMIMMIM
IM
NMI
In
IN
a
IMEMIMEM111
IN
IMIM
Ca
■IIEEII
Molina
2-
NONE
ME
NONE
1100112
ON
L40
is
ME
him,
'lag
ME
ON
som
M
L
I
N
S I
■.s■■■
L
MI
Mmb.;;
o M
—M!
---
No
■■�i■�i■�i,iii
■N�o■Om�iliv.iiii
LM
' '
MIRM
mg
OREN
oNMI
oil
il
130
4,1
now
-mom
-10
0 50 100 150 200 250 300 350 400
20 40 60 BO 14
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.
Conditions of Service: -� HYDROMATIC-
U0
GPM: TDH: rIr

�,sar32
I
Self Priming Sewage and Trash Pumps
c"
NOTE! To the installer: Please make sure you provide
this manual to the owner of the pumping equipment or to
the responsible party who maintains the system.
IrUj?0 H DROMATIC °
Pentair Pump Group

1
1
The MP / MPH self -priming
centrifugal pump has a semi -open
impeller and suction flap valve.
Pump is designed to handle raw
un-screened sewage, mild indus-
trial waste and slurries containing
entrained solids. The material of
construction is a cast iron volute
case and bearing frame, ductile
iron impeller and wear plate.
Thank you for purchasing your
Hydromatic self -priming pump.
If there are any additional
questions not covered in this manual
please contact the HYDROMATIC
representative or HYDROMATIC
Pump Co.
Before Operation:
Read the following instructions
carefully. Reasonable care and
safe methods should be practiced
for installation and operation of
pump. Check all local codes and
requirements before installation.
Attention:
This manual contains important
information for the safe use of
this product. Read this manual
completely before using this
product and refer to it often for
continued safe product use. DO
NOT THROW AWAY OR LOSE
THIS MANUAL. 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.
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.

a
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.
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
after job is finished.
Pump Installation Foundation:
Pump frame or base should be
installed on a concrete floor with
proper shims and grout. Use
hardwood tapered shims to drive
under base to level. Base should
be about 1 to 1 1/2" off the floor.
Build form around the base and
fill base inside cavity with grout.
Foundation bolts can be set in the
grout or set in the concrete floor
with expansion bolts.
Grout should be made witli 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:
Suction pipe should be same
size as pump opening. DO
NOT use larger suction pipe as
priming time will be increased
and velocity may not be
high enough to properly
carry solids.
2. Pump should be installed as
close to the liquid being
pumped as possible with a
minimum of elbows or fittings.
3. To avoid air pockets suction
pipe must be as short and
direct as possible. Suction pipe
must always slope upwards to
the pump from the source of
the liquid being pumped.
4. The suction pipe should be
installed at a distance equal to
11/2 times the diameter of the
suction pipe from the wall of
the wet well, minimum.
5. The suction pipe should be
installed at a distance equal to
one half the diameter of the
suction pipe or 3" from the
floor of the wet well, minimum.
6. If more than one suction pipe
is to be installed in the same
wet well, a distance equal to
at least 3 times the diameter
of the suction pipe should
separate them, minimum.
7. Submergence of the suction
pipe is critical to efficient pump
operations. See the following
chart for recommended minimum
submergence vs. velocity.
Submergence may be reduced
by installing a standard pipe
increaser fitting at the end
of the suction pipe. The larger
opening size will reduce the
inlet velocity and required
submergence. See Figure #1.
Vertical Suction Lift:
Vertical lift should not be more
than 15 feet. This is for starting
level only. After ` pump primes,
level can be pumped down to 18
to 20 feet if desired, but sump
level must rise up to the original
level for restart. All suction Iine
joints must be air tight as a
leak in the suction pipe can
cause pump to loose prime or
not prime at all. Always
check N.P.S.H. calculations for
available atmosphere pressure
before applying pump.
R

Hydroinatic PUMP
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PRODUCTS
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C�v �x) SiN � S- _1L AP fll-76
I - ' Mw -ff
Ejector Pump
Superior Features,
-Carbon/Ceramic type 21 mechanical seal
-Oil-filled motor with automatic reset thermal
overload for maximum protection (one phase
models)
-Upper and lower single -row ball -bearing
construction
•Piggyback plug available for easy maintenance
and switch replacement
ACCESSORIES
Download PDF Sales Sheet
Control Panels
Download PDF Nlanuai
Float Switches
Download Specification
Submittal Data
VALUE
SERVICES
Specifications:
Typical
High -capacity sornp/effluent,
Contact Us
Directions to
,Application,
Sewage
Hydromatic
Capacities:
up to 120 GPM (7.5 LPS)
Requests
Heads:
up to 28 ft. (8,5 m)
So-Nvare
115V, lo, 9.5 FLA, 6OHz-
Electrioal:
230V, lo, 4.7 FLA, 6OHz'
MADE FOR YOU
4/10 HP split phase with
lick he! - if you are a
Motor
thermal overload protection,
Hydromatic distributor
1750 RPM
or representatives.
hitermittent Liquid
140-F (60f"C)
I
Page I of 2
10/412008

Hydr("»Matic Punip
Copyright a Pentair
Pump Group All
Rights Reserved.
privney Policy
Terips and Condi tions.
Temp:
Minimum
Simplex -- 18" (457 mm)
Recommended
Duplex = 30" (762 mm)
Sump Diameter:
Automatic
Diaphragm pressure switch
Operatic, w
(manual available)
Materials of
Class 30 cast iron
Construction.
Impeller:
Thermoplastic
Discharge, Size,
TNPT (50.8 mm)
Solids Handling:
1-1/4" (31.8 mm)
Power Cord
10i, $JTW (201 optional)
Porformance.
I&S, �50AFU
Page 2 of 2
A4
0 us UPM A) 40 io 100 UO 140
Hydron.wific reserves the right. to tap Are reviAct's to Us
products and their specifications, this cata-log and relates
inforination witholat notice.
hip4O.hmnl

4
aqueonics
,,,Company:
11r,90 HYDROMATIC
Name:
t-bate: 10/5/2008
ca -F OA P
Pump:
Search Criteria:
Size: HPGF/H/X-300
Flow: 70 US gpm
Head: 23 ft
Type: GRINDER-SUBM
Speed: 1750 rpm
Fluid:
Synch speed: 1800 rpm
Dia: 7.0625 in
Water
Temperature: 60'F
Curve:
Impeller:
Density: 62.25 lb/ft'
Vapor pressure: 0.2563 psi a
Specific Speeds:
Ns: ---
Viscosity: 1.105 cP
Atm pressure: 14.7 psi a
Nss:
NPSHa: 46.4 ft
Dimensions:
Suction: --- in
Discharge: 2 in
Motor.
Pu�i$���iiYo�i iamTN to select a motor for this pump.
Pump Limits:
Temperature: 140 °F
Power: -- hp
Catalog does not contain data to verify that NPSHa is sufficient.
Pressure: --- psi g
Eye area: --- in'
Sphere size: --- in
t -- Data Point---
8 in
Flow: 70 US gpm
Head: 23 ft
50
_.
Eff: — %
Power: 3 hp
4 NPSHr: ---ft
40
-- Design Curve ---
$
Shutoff head: 34.5 ft
0
25 in
Shutoff dP: 14.9 psi
d
Min flow: 5 US gpm
Z 30'
BEP:
F.- NOL power.
3hp@5USgpm
20'
— Max Curve --
r Max power:
3 hp @ 5 US gpm
t4
10 10 20
30 40 50 60 70
80 90 100 110 120
1.5
_.
f
� 1
U) 0.5
IL
z
0 10 20
30 40 50 60 70
80 90 100 110 120
4
4
s 2
;,,--
a 0 10 20
30 40 50 60 70
80 90 100 110 120 _
US gpm
Performance Evaluation:
Flow
Speed Head
Efficiency Power
NPSHr
ft
US gpm
rpm ft
% hp
<, eR 84
1750 19.9
--- 3
---
70
1750 23
--- 3
56
1750 25.9
--- 3
---
42
1750 28.6
--- 3
---
28
1750 30.9
3
H2Optimize Hydromatic 8 Selected from catalog: Grinder Pumps 60Hz Vers: Feb 2006

=mom
DECANTING PUMP --
HYDROMATIC Model SK50
;Typical Application
[Capacities to
jHeads to
Recommended
__.... ______ ___.__ - ._...
!Sump Diameter Duplex
Automatic Operation
of Construction
u,�miYu.�er.u. ao �o sn sa too Aso
Performance Curve
18" (457mm)
" (762mm)
_..........
Wide angle float switch (manual available)
30 cast iron
;Impeller
!Class 30 cast iron non -clog
'Discharge Size
12" (50.8mm); 3" (76 2mm) optional
;Solids handling
12" (50 8mm)
;Power cord
110' , SJTW, (20' optional)
;Superior Features
Carbon/Ceramic type 21 mechanical seal
Oil filled motor w/automatic reset thermal overload
'Tor maximum protection
Upper and lower single row ball bearing
`construction
Piggy -back plug available for easy maintenance
rand replacement

BULLETIN C
Cut -Sheets for WWTP Blowers

/' \tea 4 Ainc�fr
3.5
!!2!"-S
2,80076
1.1
71
1.6
67
2.1
2.4
fi3
79
2.5 59
2.9 75
3.0
3.4
56
72
4.0
2LP
2LVP
0.035
3,250
3,560
91 4.3
102 1.4
86
97
1.8
2.0
82
93
2.6
78
3.2 86
3.7
83
143
4.3
6.1
5 275
162 2.0
i 9
Y 57
142
2.8
2.8
153
135
3.7
3.7
149
130
4.6 i 46
4.5 124
5.3
5.2
120
6.1
3LP
2h'"-S
0.104
1,760
2,265
149
202 2.4
194
3.5
188
4.7
182
235
5.6 177
6.8 230
6.7
8.2
172
225
7.8
9.6
3LVP
3,600.
2,770r400
2.9
3.7
247
333
4.3
5.3
240
327
5.5
7.1
321
8.9 316
10.6
3t1
12.4
1,760
3.0
243
4.5
234
5.7
227
300
7.1 220
8.8 293
8.5
10.6
213
286
9.9
12.4
4LP
3"•S
0.17D
2,190
2,620
3.7
4.4
316
389
5.3
6.3381
307
7.1
8.4
373
10.6 366
12.7
360
14.8
4LVP
3 600
5.8
556
6.7
547
11.6
539
427
14.5 533
12.4 418149
17.4
526
409
20.3
17.4
1,500
1,760
5.2
5.8
449
540
7.5
8.8
438
529
10.0
11.7
518
14.6 509
17.5
500
20.4
5LP
SLVP
4"-S
0.350
2,100
673 7.0
669
10.5
6A8
13.9
637
17.4 628
20.9
619
24.4
1,170
739
8.0
12.0
716
1,139
11.0
18.0
697
1.120
16.9
24.0
680
1,103
19.9
29.9
664
1,
23.9
35.9
650
1,
27.9
41.
6LP
6„-F
0718
1,760
1,930
1,162
1,284
13.1
1,261
19.7
1,242
26.3
1,225
32.6
Y0
1,210
39.4
96
t,196
46.0
6LVP
1,527
40.0
1,512
1,170
1,465
1,277
1,631
13.3
16.7
1,248
1,602
20.0
25.0
1,224
1.578
16.6
33.3
1,203
1,557
33.3
41.7
1,184
1,538
39.9
50.0
7LP
7LVP
8"•F
1.200
1,760
1,985
20.0
1,956
30.0
1,932
40.0
1,911
50.1
1,892
2,240..
60.1
70.0
2050
880
2,333
1,366
23.3
14.5
2,304
1,329
35.0
21.8
2,280
1,298
46.6
29.0
2 259
1,271
58.3
36.3
1,246
43.5
8LP
10"-F.
1.740
1,170
1,375
1,871
2,228
19.3
22.7
1,834
2,191
28.9
34.0
1,803
2,159
36.6
45.4
1,775
2,132
48.2
56.7
1,750
2,107
57.9
68.0
8LVP
1,800 1
2,967
29.7
2,930
44.5
2,899
59.4
2,871
74.2
2,647 1
69.1
•
2,800.
25 1.7
22 2.1
2MP 3,250
1 -S 0.017
33 1.9
2.1
30 2.5 28 2.7
35 2.7 34 3.0
4 9
2MVP 3,560
5 275
38
67 3.1
64 3.6
64 3.9 63 4.4 60
59 4.6
5.1
,
..
1,760
3MP 2"-S 0,060 2,265
2777a
95 4.6,,
12V �5.6
i , 88,, ,,, 5. 87 6.4
119 7.1 117 7.9 112
9.5
3MVP -
3,600
175 7.2
169 9.2 167 10.2 162
12.3
1,760
144
6.8
136
8.8
132
9.8
4MP
2S" S
0 117
2,190
2,620
194
245
8.5
10.2
186
236
10.9
13.1
182
233
12.1
14.5
4MVP
3,600
1,500
359
237
14.0
10.5
351
227
18.0
13.4
347
222
20.0
14.9
213
17.9
209
19.4
5MP
C-S
0.210
1,760
292
12.3
14.6
281
353
15.8
18.8
277
348
17.5
20.9
268
339
21.0
25.1
263
335
22.8
27.2
5MVP
2,100
2,850
363
521
19.9
510
25.5
506
28.4
497
34.0
25.5
493
269
36.9
27.6
283
29.7
1,170
1,760
332
558
14.9
22.4
316
542
19.1
28.8
309
535
21.2
32.0
296
522
38.3
515
41.5
509
44.7
6MP
6MVP
5„-S
0.383
1,930
622
24.5
607
31.5
600
35.0
587
42.0
580
741
45.5
55.5
574
735
49.1
59.7
_
2,350
764
29.9
768
38.4
761
42.7
748
51.2
1,170
693
28.5
671
36.6
661
40.7
7MP
6"-F
0.733
1,465
1,760
909
1,125
35.6
42.8
887
1,103
45.8
55.0
877
1,093
50.9
61.1
7MVP
2,050
1,338
49.9
1,316
64.1
1.306
71.2
880
709
30.4
681
39.0
669
43.4
8mP
8"-F
1.040
1,170
1,375
1,011
1,224
40.4
47.4
983
1,196
51.9
61.0
970
1,183
57.7
67.6
BMVP
1,800
1 1.666
62.1
1 1,638
79.9
1,625
88.7
� �y1
e
1,760
46 ' 2.6 44 13.0
41 3.4
3HP
t -S 0.045
2,265
2 770
69 3.4 66 3.9
91 4.1 69 4.7
64 4.3
87 5.3
60
83
5.3
6.5
3HVP
3,600
129 5.4 126 6.1
124 6.9
120
8.4 117 10.0
113
11.5
1,760
2,190
80
110
4.0
5.0
77
107
4.6
5.7
74
104
5-2
6.4
99
7.9
4HP
4HVP
iW-S
0.069
2,620
139
6.0
137
6.9
134
7.7
129
9.4
13.0
124
192
11.1
15.3
168
17.7
3,600
207
8.2
204
9.4
201.
10.6
196
1,500
154
7.0
151
8.0
147
783
9.
10.5
140
177
10.9
12.8
171
15.2
165
17.5
5HP
2h"-S
0.140
1,760
2,100
91
238
8.2
9.8
187
235
9.3
11.1
231
12.5
224
15.3
218
18.1
213
20.4
SHVP
2,850
343
132
340
15.1
336
17.0
329
20.8
323
24.6
318
28.4
1,170
18
8.8
182
10.
_
177
311
1.3
17.0
168
302
13.8
20.8
159
293
16.4
24.6
265
28.4
6HP
3"-S
0.227
1.760
1,930
321
360
13.3
14.5
316
355
15.1
16.6
350
18.7
340
22.6
332
27.0
324
3i.1
6HVP
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
428
18.3
22.9
308
416
22.4
28.0
297
405
26.5
33.1
287
'396
30.5
38.2
7HP
q��.S
0.367
1,465
1,760
441
549
17.8
21.4
434
542
20.4
24.5
536
27.6
524
33.7
514
'
39.8
504
45.9
7HVP
2,050
655
25.0
649
28.5
642
32.1
631
39.2
620
46.4
610
53.5
880
363
16.5
354
18.9
34G
509
21.2
28.3
329
493
26.0
34.5
31:5
479
30.7
40:8
8D1
465
35.4
47.1
SHP
4"-S
D.566
1,170
1,375
528
644
22.0
25.8
518
634
25.1
29.5
626
33.2
609
40.6
595
- 48.0
581
55.3
BHVP
1,800
884
3:
875
38.6
866
43.5
850
53.1
835
62.8
522
72.4
RPM

r9;
Proven Performance. Global Applications. Local Support.
Below are just a few examples of the industries that, 50% Less The sound data shown,compares
over the decades, have depended upon the Sutorbilt° Operating Noise the Legend and a comparably sized
Legend'"` to deliver clean, oil -free air to a wide range blower operating at 3,275 rpm and
�.®� SUtOeFR,tECc9 ...x� Lg4fgt�atFLLH�
of global applications.
Industry Application so
�
Aquaculture Aeration is
-
Cement and Lime Fluidization and Conveying
Chemical Vacuum Processing and Conveying A
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.
p
Coal Bed/Landfill
Methane Gas Recovery
Superior Local Sales and
p
Dairy
Automated Milking
Dry Bulk Hauling
Trailer Unloading and Aeration
Service
Environmental Services
Sewer Cleaning and
""` Our extensive network of authorized
Portable Restroom Services
4. '' ' Sutorbilt distributors offers the most
Industrial
Material Vacuuming
convenient local sales and service sup -
Milling and Baking
Blending and Conveying
= - port of anyone in the industry today.
Oil and Gas
Gas Collection and Sparging
These factory trained professionals
Power Generation
Fly Ash Conveying and Aeration
are experts in blower/vacuum pump
Process Gas
Gas Boosting
technology providing system installation guidance, troubleshooting and
Pulp and Paper
Chip Conveying and
optimization recommendations of your new or existing applications.
Process Vacuum
Resin and Plastic
Processing and Conveying
Even a Legendary Warranty
Soil Remediation
Vacuum Extraction and Sparging
Every Sutorbilt Legend Series blower/ vacuum pump is covered by
Vacuum Excavation
Potholing and Slurry Recovery
an uncontested warranty for 24 months from the date of shipment
Wastewater
Aeration and Backwashing
or 18 months from the date of installation on all blower materials
and workmanship. Replacement or repair costs will be at no charge
__J._J_.__ _..,....., r_:—t— 7 nral .Cntnrhilt

LAW
Small Compact Filter Silencers
w/ Standard Filter Design
TS" Series 1/2" - 3" MPT
• Industrial & Severe Duty + Engines •Waste Water Aeration
r:J + Piston Compressors + Construction\Contractor Industry • Nailers and Staplers
+ Screw Compressors + Workshop + Vacuum Vent Breathers
+ Blowers - Side Channel & P.D. • Medical\Dental Industry
+ Hydraulic Breathers — fine filtration + Pneumatic Conveying
lFEATURES & SPECIFICATIONS��
• 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
F:F + Fully drawn weatherhood - no welds to rust or vibrate apart (safety factor)
• Tubular silencing design - tube is positioned to maximize • Temp (continuous): min -15°F (-26'C ) max 220'F (104°C )
attenuation and air flow while minimizing pressure drop • Filter change out differential: 10"-15" H2O 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
�A + Pressure Drop Indicator + Epoxy coated housings • Special connections, BSPT
%7111 s �i i-
OUTLET
Dimension tolerance + 114"
■ 1= Industriat duty S = Severe Duty *'
TYPICAL NOISE ATTENUATION — FS SERIES
za
a
v 15
I
Z
0 10
5
4LET 63 125 250 SW 1000 2000 4000 5000
OCTAVE BAND CENTER FRECUENCIES - Hz
Noise attenuation may vary due to the wide range of
applications and machines
with
Polyester
Element
,with
Paper
Element
MPT
Outlet
DIMENSIONS - inches
A B C
Rated Flow SGFM
crew.
lower, Element
Piston Fan Rating
No. of
Silencing
Tubes
Approx.
Wt.lbs
I
FS-15-050
FS-14-050
112"
4
1 1/2
6
10
10
35
1
2
I
FS-15-075
FS-14-075
3/4"
4
11/2
6
20
25
35
2
2
I
FS 15 100
F5 14 100
11.
-a.T,pJ
4
�`.".
1 1/2
fr4
OF
6
25
35
35
3
2
. .+.w.
I
FS-19P-150
FS-18P-150
1 1/2"
6 5/8
1 5/8
6
70
85
100
5
4
I
FS-31P-200
FS-30P-200
2"
7114
21/4
10
85
135
195
5
$
S
FS 231P-200
FS 230P 200
2'
12 1/4
2 1/4
10
-g'�kmwa­
135
135
300
-5
14
�
4 � ,u.
'i �:'�
k�
. �
`��i�
F
,�
t+
ei�'e�;n3,2u�
Note: Model offerings and design parameters may change without notice. 1151 Ardmore Ave, + Itasca, IL 60143 USA
Sales/Service: 630,773.1363 + Fax: [phone]
Solberg — Discover the Possibilities E-mail: [e-mail] + Web Site: www.solbergmfg.com
FS25-406 pg. 3
i._

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

: TPA 9
■■
so
u

12:21pm wwS1 7702766535 #439 Page 11/12
tjU
Co
PUMPS_
LC - 20953 Configured Curve
By., TGJ
Date; 1019/2008
Rev.
�Project: Waste Water Systems
-Tag
9 P-I P-2
P.O.
Location;
Model: 20953
Oust Ref#
,1Contractor:
Cfty; 2
EgenURep. SPE
jEngineer:
Service:
Dar, #
La 60
asp 40
20
...... ....
........ ........... .. ..... ..... . .... ....
- -------- .... . ................ .
FEE.
............. .... . . ..... ....
......... . .........
. ..........
0 so 100 150 200 260 300 350 400 450 Soo 550 600 650 700
Capacity - Us9pril
9.60 in Max
Ratedl-
. .....
. ............... ... . .. . ......
. ......... ..... ... ...
.... ......
....... ....... --------
- F954 In
. . . . .............
. ..... . .......
Effidency
.... . ... ...
7.00 in
fain
i
... ........
. ........
. .... . ...... .......
. . .......... ............ .
-4
..
.......
100
-90
80
,70
-60
50
.40
30
20
0 so 100 150 200 250 500 350 400 450 Soo SSO 600 650 700
Capacity - Usgpm
20-
n.
ir i
T.. ........... . .........
............. . ..... -
0 so 100 ISO 200 250 300 3S0 400 450 500 550 $00 650 700
Capacity - usgpm
6,w ..7
Flow: 200 USqpm
Fluid: Wetter
Suct. Press: 0-00 psi.a
?H: 350 ft
Temp: 68.00 deg F
Dis. Press:
�Pqutoff Head; 363 ft
S.C.: 0.998
Diff. Press:
NPSHr, 7.04 ft
isc.; 1.00 ap
BHP: 30.3 hp
Dig-- 9-54 In
Pump Eff., 58.16
fa*4 Of Stages., 1
ISEP- 426 Usgpm,
Motor Data,
40
Voltage: 208-2301460
Eff;
r' inal RPM, 3500
Phase: Three phase
S.F.; 1.15
Actual RPM., 3500
Hz, Go
End.: ODP
•

SELECTICtN
CC3'[ DITKYNS
Flow:
200.0 GPM
Priming Type:
Standard,
Total Dynamic Head:
140.0 feet
M-ot-or Loading:
Standard
PUMP DESCRIPTION
Pump Model:
82TPMS
Priming Type:
Standard
Impeller Diameter:
6,Iaa in.
Irrrp•el•ler Material:
Iron
Suction:
2Vz"NPT
Discharge:
2"NPT
Shaft Seal:
Mechanical'
PUMP PERFGRIrEANEE
Flow:
200-0 GPM
Pa.Wer:
3..7 3N.P
Total Dynamic Head;
140-6 feet
Efficiency:
73-.4 7
Nominal Speed:
3600 RPM
NPSHR:
°I4..2 feet
Shut —Off Head:
154.3 feet
Max Power:
T'T.0 ETH.R
Beat Eff; 73.7 (9� 21.4.E 0P'M
MOTOR
Size:
10 HP
Enclosure:
TEFL
VoItoYe: Consult Catalog/Factory
HZ/171-hose:
FR10E/ORDER
INFORMATION
CatOing No.:
Factory
WaighL;
200 Ibs_

BULLETIN E
Cut -Sheets for Flushing Return Pumps and Tanks

`QV,4L/TY PVMPS �NCE ����/ 'tUA
Product information presented
here reflects conditions at time
of publication. Consult fac-
u tory regarding discrepancies or
inconsistencies.
Ar
MAIL TO: P0. BOX 16347 • Louisville, KY 40256-0347
SHIP TO: 3649 Cane Run Road • Louisville, KY 40211-1961
[phone]. 1(800) 928-PUMP • FAX [phone]
SECTION: 3.20.022
FM2091
0207
Supersedes
0506
visit our web site:
www.zoeller.com
80E1.66R ON -SITE WASTEWATER PRODUCTS
Multi-Sta Effluent Turbine Submersible Pumps
Effluent turbine pumps are used in on -site applications that
demand more head than a traditional single stage centrifugal
submersible pump. Zoeller Pump Company is able to meet this
need by offering a complete line of submersible effluent turbine
pumps. These pumps have been proven in field applications and
have many years of development behind them. Typical appli-
cations include mound systems, drip systems, and recirculating
media filters. All units include cool running submersible motors
that do not require external water flow to prevent overheating.
An outer pump sleeve is not required. Pumps can be installed
directly in a dose tank as long as an effluent filter is used on the
septic tank outlet. These pumps can also be used in conjunction
with the Zoeller Effluent Turbine Filtered STEP system.
FEATURES:
• Corrosion resistant.
• 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).
Heavy wall stainless steel pump shell.
• Franklin Electric submersible motors.
• Stainless steel hex drive pump shaft.
High Efficiency floating stack.
Glass -filled Noryl discharge and mounting ring
(10, 19, and 27 GPM models).
Stainless steel discharge and mounting ring
(35, 55 and 85 GPM models).
No external capacitors or relays required for starting
('/,A % 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'/z HP units
only). Consult Factory for longer lengths.
• Timed dosing panels available.
5 year extended warranties available. (Consult Factory
for details.)
U Gopyrlgnl Lu t LOeller l.O. Mu l lyi as load Vc

75
70
65
60
55
0
50
4
= 45
v_
¢ 40
35
F 30
25
20
15
10
5
C
Models65 GPM
PERFORMANCEPUMP
55 GPM
2" NPT A-
MEN
W�
�1■■■■■.
ME
77
F77
ME
314 HP-2 STAGE
10 20 30 40 50 60 70 80 90 10
LITERS 0 40 80 120 160 200 240 280 320 360
FLOW PER HOURIMINUTE 015649
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5034-0005
1 /2
115
1
12.0
1
18-5/ 16,
5034-0006
112
230
1
6.0
1
18-5116"
5034-0007
314
230
1
8.0
2
21-9116"
6034-0008
1
230
1
9.8
3
24-3/4'
5034-0009
1-1/2
230
1
13.1
4
30-3/16"
5034-0010*
2
230
1
13.2
5
32-5/16°
5034.0011*
3
1 230
1 1
14.5
7
1 40-7/16"
*Includes starter box and 25' long flat wire cable assembly.
W PUMP PERFORMANCE CURVE
85 GPM
2" NPT DISCHARGE
60
200
3 HP-6 STAGE
55
175
50
¢w 45
x
150
U
40
2 HP-4
STAGE
a
125
}
0 35
1.5HP
0 30
100
_
3 STAGE
25
75
20
1 HP-2 STAGE
15
50
314 HP-1
STAGE
10
25
5-
0
20 40 60 80 100 120 140
GALLONS
LITERS 0 80 160 240 320 400 480
FLOW PER HOUR/MINUTE 015845
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5035-0005
314
230
1
8.0
1
20-1/8"
5035-0006
1
230
1
9.8
2
24"
5035-0007
1-1/2
230
1
13.1
3
30-1/8'
5035-0008*
2
230
1
13.2
4
32-7/8"
5035.0009*
3
230
1
14.5
6
42-318"
*Includes starter box and 29long flat wire cable assembly.
Accessories
Filtered STEP System
Zoeller Pressure Effluent Filter
This Zoeller Filtered STEP
The Zoeller Pressure Filter will help
System is designed as an
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 resi dental 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 as a
the Filtered STEP System
prefilter for dosed treatment devices
is the answer without the
such as recirculating media filters.
extra cost of a pumping
chamber.
For use with pumps up to
55 GPM. Contact Factory
for 85 GPM applications.
See FM2244 for more information.
See FM2090 for more information.
© Copyright 2007 Zoeller Co. All rights reserved.

All brass spring loaded check valves are designed to
screw directly into the pump discharge. Check valves
are assembled with components suitable for a septic
environment. Check valves should be used at the pump
in a pressure sewer system. A redundant PVC check
valve and isolator (ball) valve should also be used at
the sewer connection in pressure sewers.
Part
Number
Piping
Size
Pressure
Rating
Weight
30-0187
1-1/4"
400 psi
2lbs.
30-0189
2"
400 psi
3 lbs.
H
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
V
125 psi
11b.
30-0209
1-1/2"
125 si
11b.
30-0210
2"
125 si1
3lbs.
Rail systems are used for easy pump removal from an efflu-
ent pit. Service personnel will not need to enter a hazardous
environment. Pump sits on floor and engages piping system
via a sliding disconnect fitting. All parts are stainless steel or
brass and suitable for a septic environment.
Part
Number
Piping Size
Weight
39-0098
1-1/4" Female pipe thread
10 lbs.
39-0099
1-1/2" Female pipe thread
11 lbs.
39-0100
2" Female pipe thread
12 lbs.
Disconnects Onlv
Part
Number
Pipe
Size
Weight
39-0053
1-1/4"
2lbs.
39-0001
1-1/2"
2lbs.
39-0002
1 2"
1 2.5lbs
Stainless Steel Pull Rods
3/8"-16 UNC
umber
Length
0691'
N
006
2%0007
3%2
39-0008
4'/2
39-0009
5%
39-0018
7'
39-0010
8'
ALL ZOELLER ON -SITE WASTEWATER PRODUCTS MUST BE INSTALLED IN ACCORDANCE WITH LOCAL AND/OR STATE PLUMB-
ING AND/OR HEALTH DEPARTMENT CODES.
© Copyright 2007 Zoeller Co. All rights reserved.

10 GPM Models
1
w PUMP PERFORMANCE CURVE
LL 10 GPM
1 1/4" NPT DISCHARGE
"1
314 HP-12 STAGE
360
104
96
320
ss
p 80
2so
112 HR 8 STAGE
L
i 72
U
240
g
z 64
0 56
zoo
112 HP-
6 STAGE
'�
<
0 49
160
40
120
32
2q
80
I" A
16
40
8
LA
IN
o
2
4
6
8 10
12 14
FLOW PER MINUTE
015413
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5030-0005
1/2
115
1
12.0
6
22-3/8'
5030-0006
112
230
1
6.0
6
22-318"
5030-0007
112
115
1
12.0
8
24-118'
5030- 0008
112
230
1
6.0
8
24-1/8'
5030-0009
3/4
230
1
8.0
12
28-7/8'
7 GPM Models
PUMP PERFORMANCE CURVE„'.z
27 GPM
1 1/4" NPT DISCHARGE..
326
399
11t2 HP-10
STAGE
v i t � ' "".
\I
IN
Hij
cA 1oNs l
❑TERG 29 a0 s ea Tao 126 1c0
FLUNPERMINUTE 015045
Part Number]HPVoltage
Phase
Amps
Stages
Height
5032-0005
115
112.0
4
21-1/8'
5032-0006
230
1
6.0
4
21-118'
5032-0007
230
1
8.0
6
24-5116'5032-0008
230
1
9.8
7
26-7116'
-0009
230
1
13.1
10
31-718'
19 GPM Models
E
LL
PUMP PERFORMANCE CURVE
19 GPM
1"/4" NPT DISCHARGE
80
280
1 HP -.9
STAGE
72
240
314 HP
7 STAGE
64
200
56
48
160
U
< 40
� 32
120
1/2 HP
5 STAGE
0 24
H
80
16
40
8
D
I I I I
5 10 15 20 25
GALLONS
LITERS '—'I
0 20 40 60 80 100
FLOW PER MINUTE
015414
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5031-0005
1/2
115
1
12.0
5
21-16116'
5031- 0006
1/2
230
1
6.0
5
21-15116"
5031-0007
3/4
230
1
8.0
7
25-1/16"
5031.0008
1
230
1
9.8
9
28-1/8'
35 GPM Models
PUMP PERFORMANCE CURVE
35 GPM
2" NPT DISCHARGE
56
180
1-1/2 HP- 5 STA
48
160
140
1 HP- 4 STAGE
40
120
32
314 HP-3STAG
100
r
0
0 24
BO
1/2HP-25TAG
F-
8
j
0
10 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
19-7/16'
5033-0007
3/4
230
1
8.0
3
22-3/16'
6033-0008
1
230
1
9.8
4
24-15/16'
5033-0009
1-1/2
230
1
13.1
5
29-15/16'
© Copyright 2007 Zoeller Co. All rights reserved.

10 GPM Models
PUMP PERFORMANCE CURVE
10 GPM
1 1/4" NPT DISCHARGE
1zo qoo � I
t12 314 HR 12 STAB
360
t04
96 320
88 280
o so 112 HP-8 STAGE
i 72 240
U
z 64
200
56 112 HP- 6 STAGE
0 48 160
40
120
32
2q SO -
Is
40-
8
0
2 4
GALLONS
FLOW PER MINUTE 015413
Part Number
HP
Voltage
Phase
Amps
Stages
Height
5 330-0005
1/2
115
1
12.0
6
22-318"
5030.0006
1l2
230
1
6.0
6
22-3/8'
5036-0007
1l2
155
1
120
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"
19,
27 GPM Models ?,,% l
PUMP PERFORMANCE CURVE ¢
.._..,,27 GPM
f
320 NPT DISCHARGE �.
1 HP-7 STAGE
220
84 31
200 5fAGEHP _
i 5fi 160
� ae ts0
W.
LO 12 HP-4 STAGE
LITERS
FLOW PER MI NUTE
IL
015045
Part Number
H P
Voltage
Phase
Amps
Stages
Height
5032-0005
72
115
1
12.0
4
21-1/8'
5032-0006
112
230
1
6.0
4
21-1/8'
5032-0007
3l4
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"
19 GPM Models
LL
PUMP PERFORMANCE CURVE
19 GPM
1'/4" NPT DISCHARGE
280
1 HP - 9 STAGE
80
72
240
3/4 HP
7 STAGE
64
200
0 56
4g
160
U
a 40-120
1/2HP
32
5 STAGE
O 24
80
16
40-
8
0
5 10 15 20 25 30
GALLONS _
LITERS 0 20 40 60 80 100
FLOW PER MINUTE
015414
Part Number
H P
Vdtage
Phase
Amps
Stages
Height
5031-0005
112
115
1
12.0
5
21-15116"
5031-0006
112
230
1
6.0
5
21-15116'
5031-0 007
3l4
230
1
8.0
7
25-1116'
5031-0008
1
230
1
9.8
9
28-118"
35 GPM Models
PUMP PERFORMANCE CURVE
LL 35 GPM
2" NPT DISCHARGE
56 180
:1HP
HP-5STAGE
48 160
140 4STAGE
40
120
2
9 32 314HP-3 STAGE
100
r
0
0 24 80 1/2HP-2STAGE
6U
16
40-
8
20
10 20 30 40 50 60
GALLONS I
LITERS 110 40 80 120 160 200
FLOW PER MINUTE 015044
HP
Voltage
Phase
Amps
Stages
Height
112
115
1
12.0
2
19-7/16'
112
230
1
6.0
2
19-7/16'
P5033-0008
314
230
1
8.0
3
22-3116'
1
230
1
9.8
4
24-15/16'
1-1/2
230
1
13.1
5
29-15116"
O Copyright 2007 Zoeller Co. All rights reserved.

FM2218
..
`4KIWITY jazImPs 9116CE 11939 0206
Supersedes
® L" 1204
Product information presented %
here reflects conditions at time L .
of publication. Consult faG
Wry regarding discrepancies or VISIt our Web Site:
inconsistencle!s. MAIL TO: PO. BOX 16347 • Louisville, KY 40256-0347
SHIP TO: 3649 Cane Run Road • Louisville, KY 40211-1961 www.zoeller.com
[phone]. 1 (800) 928-PUMP • FAX [phone]
EFFLUENT TURBINE PUMP INFORMATION
Cable Guide: SJOW: Junior hard service, same construction as type'juuv out only 14Lea poi 0w V U-1
*Dry run capable for up to 24 hours without damage.
`"Minimum Liquid Level (measured from bottom of pump).
© Copyright 2006 Zoeller Co. All rights reserved.

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BULLETIN F
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BULLETIN G
WSI PC Controller Electrical Schematics

k
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pM
PUMP A & B 120 VAC
➢ISCONNECTS DISCONNECTS
CONTACTOR A
G
CE15+NSTR
TI T2 T3
A 6
e e
OVERLOAD A
CONTACTOR B
1 FM
�� L
[&jgi r - Na��e
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® Deb
6 6
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120V POWER
DISTRIBUTION
BLOCKS
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IIo11:�]OOfi�ll
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MM
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24 VAC CONTROL
TRANSFORMER
qM
24 VAC ISOLATION
TRANSFORMER
;7,-
TGo241-,E ._ 0 0
TG ee ❑❑ RACK i
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❑ ao mm,mmmmmm'm°mmmmmm""m19mmmmmmmmmmmmm
,.
N
120VAC CPU
POWER
me
1A AM
TO L A
SCP30 S 5-DN
+12 VDC POWER
m, r SUPPLY
C E. 9J
IN IN
• •
6 m
m e
SS ❑ L
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+5 VDC POWER
' SUPPLY
Irt� Sv- , 6M
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IN 1N
• •
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. .. .....uuc.c.c.c.c.c.c.c.c.c.c.c
.........ca..e.e.a.ess..e...cs......e.e
DISTRIBUTION
BLOCKS1
CONTROLLER
RACK 2
�Q� O
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❑
I�C�9C OBC� aCaCCCC�CC al.-�.-1 L_�.-1 L-�.-1Cal- 1��a i �I I:a I_I I-1 L->I �� L_I I-1 I-1 L-11�-1 L-1 I_I I-1 I_I I -•.I I_I
PC PANEL LAYOUT
1 of 1
REV-0
4 Rose Hill
"PercdRito" DATE: 09/22/07
FIELD ISOLATION RELAYS r4 - r20
Waste Water Systems, Inc.
P.O. BOX 1023 [phone]
F1 i IJAY (A n.54n Fry (7nF)

PUMP A
POWER
A B C
PUMP B
POWER
A B C
G
G
G
G
G
G
➢30
WMS3D30
415V —
10000
D30
WMS3D30
415V —
10000
A B
A B B
S 261
D4
—230/40
7R7-
Nt
40 A
S 261
➢4
—230/40C
Nt
40 A
❑N
ON
LEIN
ON
LEIN
LoNj
GGGGGGG
G
PUMP A & B
DISC❑NNECTS
120 VAC
DISCONNECTS
0000�aoop�p
=0000000�m
120V 20 A
from panel
120V
from UPS
(by wwsi)
fsiiii';2� �1lfltii[itiaa[[til?[19
11 � 11
11
�..._ E'961=, ��AIgPIRIFIIAIAIAAIgIpIFPIPP�giq;q'.
INCOMING POWER CONNECTIONS
1 of 1
Waste
Water
Systems, Inc.
4
REV-0
Rose Hill
P.O. BOX
1023
[phone]
DATE: 09/22/07
n "Perc�Rite'� � _
ELLIJAY.
GA. 30540
Fax i706i 276-6535

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REV_0
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DATE: 09/22/07
"Perc`Rite"• ELLIJAY, GA. 30540 Fax [phone]

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1 of 1 Waste Water Systems, Inc.
REV-0
d Rose Hill P.O. BOX 1023 [phone]
DATE: 09/212/07
„_ "PerclRite'® FLI_I, AY. GA. 3054(1 Fnx (706) 976—A.5.-�.5

COMMUNICATIN WIRING
-- 1 of 1 Waste Water Systems, Inc.
REV_0
IWZ� Rose Hill P.O. BOX 1023 [phone]
"Perc`Rite" DATE: 09/22/07 FI I IJAY (A 3n54n Fnv f7nFl

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1 of 1 Waste Water Systems, Inc.
REV_0
Rose Hill P.O. BOX 1023 [phone]
DATE:
"PeYc09/22/07 ,`Rite"• _ _ EI_I.I,IAY. GA .30.54(1 Fnx (7(1F1

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® 1 of 1 Waste Water Systems, Inc.
REV-0
4 Rose Hill P.O. BOX 1023 [phone]
"Perc`Rite" DATE: 09/22/07 FI 1 I.IAY (A .-�n�an Fnv MR)

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

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FIELD VALVE CONNECTIONS
1 of 1 Waste Water Systems, Inc.
REV-0
Rose Hill P.O. BOX 1023 [phone]
" Perc! Rite' DATE: 09/22/07
„� _ _ .. ELLIJAY. GA. 30540 Fax (70e) 97Fi-R5.35

BULLETIN H
Cut -Sheets for Drip System Valving

Diaphragm Actuated Valve
44;
Piston Actuated Valve
IBM= __ id L-11ME
The actuator assembly is unitized and is removable from the body as
an integral unit. It consists of both an upper and a lower control -chamber.
Each basic valve can easily be configured, on -site, either as a
single -chamber 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. 'The 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

L
B6RMAD WatEPWOrks
70 Srri E S E _-
Avaiar:,"'a —Sizes & Patte'rns
F-1 0 1 /Y- 20" (40 - 500 mm} (.�,And Angle
a 24' - 32" (600 - 800 mm) - Globe
Cownectioii Standard
Flanged, ISO ISO 7005-2 (ANSI B- 16.42),
reacted;
9 1 rWded;NPTorBSP40,50,65&80mm
e� J Water Temp('nature
a Up to 800C (1 800F)
VVork�nq pre-,ssure
psi
v ISO PN 16: 16 bar tClass 150': 250 p,,
41
'1"�s 00, 0.
w ISO PN 25, 25 bar w Class 4#30& psi
Standard materials
Main valve body and cover
Ductile iron EN 1563 (ASTM A-536)
Main valve internals
Stainless steel and bronze
Control Trim
Brass components/accessories
Forged brass fittings & copper tubing
Elastomers
NBR (Bona-N)
Coating
Fusion Bonded Epoxy, RAL 5005 (Blue)
i LNSF 61 and WRAS approved
or Electrostatic Polyester Powder, RAL 6017 (Green)
1-11 WRAS approved
Main valve body/internals
Carbon steel (ASTM A-216-WCB)
Stainless steel 316 CF8M (316)
Aluminum
Nickel Aluminum Bronze
Titanium
Alloy 20
Duplex
Hastalloy
Marine Bronze
254 SM0
Control Trim
Stainless steel 316
Hastalloy C-276
Elastorners
EPDM
Viton
Hydraulic C;OMPOI VaIVES
700 & 800 5 ries
o ins
Available Sizes Patterns
11/2" -� 20" (40-1- 500 mm) - Y pattern
11/9" - 18" (40450 mm) - Angle
n Star dard
x Flange : ISO 16-1 (ANSI B16.5),
Water lei iperah lre
a Up to IC (1 80'F)
Working ressur�
* ISO PNI 16: 16 bar K Class 4 150: 250 psi
* ISO PNj25: 25 ar a Class #300: 400 psi
* ISO PN�40: 40 ar s Class #400-. 600 psi
Stardard ilfttena
I
j Main alve y
Gar on bl
on steel TM A-216-WCB)
DucJile iron EJ 1563 (ASTM A-536)
Valvelcover (p' ton cylinder)
Brorize or stai less steel
-j Main valve int malls
StAless steel and bronze
Control Trim
,)mponpnts/acce-ssorjes
brass fAtings & copper tubing
NSF�l and W1
or E16otrostatic
WRA'approvE
i
optiom , aterials
Main valve bod
StainlIss steel
Nickel Alt.
Titaniu I in
Alloy 20
Duplex
Hastalloy
Marine B?
254 SIVId
-j Control Tr
Stainless
Hastalloy
-3 Flastarnei
EPDM
Viton
-poxy, RAL 5005 (Blue)
�S approved
lolvester Powder, RAL. 6017 (Green)
6 CF8M (316)
Bronzee

BERMAD Watepworks
Flow Chart
i C�
Valvc- Flow COOPOEnt
Y-Pattern
Flat Disc
Y-PaMern U_Plug
Angle
Flat Disc
Angie
"'J
Control VaIVES
M-6 & 800 seric-s
�-777 7 77 4,
$T IN
Inch
1.5"
3"
4"
6%p
87'
10" 12"
14" 16v$ 18"
ir
:,1
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 12,035
2,189 3,641 3,773
NAI
Cv
53
64
70
146
250
580
1,040
1,590 2,350
2,530 4,210 4,360
NA
Kv
39
47
51
108
187
430
762
1,169 1,730
1,861 3,095 3,207
NA
CV
45
54
59
124
220
500
880
1,350 2,000
2,150 3,580 3,710
NA
inch 24'' 28 30" 32"
G-Pattern rE
Kv 7,350 7,500 7,500 7,500
Flat Disc
Cv 8,490 8,670 8,670:8,670
FG-f
Valve flow coefficient, Kv or Cv Kv(Cv)=Q dP
Where:
R
Kv = Valve flow coefficient (flow in m3/h at 1 bar Diff. . Press.)
Cv = Valve flow coefficient (flow in gprn at Diff. . Press. 1 psi)
Q = Flow rate (rn',I/h ; gpm)
AP = Differential pressure (bar; psi)
Gf = Liquid specific gravity (Water = 1.0)
J

0 Series
METAL BODY
cONT.:
TECHNICAL DATA
Specifications
• Valve Configuration:
Y-pattern and angle
• Sizes:
Y - Y-pattern; 11/2", 2" & 3"
A —Angle. 2"
• End Connections.
—11/2" & 2": threaded NPT, BSP
— 3": female threaded NPT/BS or
flanged to ANSI/ISO/BS-D
• Operating Pressure Range:
10-150 psi (0.7-10 bar)
• Temperature Range:
Water up to 1 B0°F (80°C)
• Materials:
Body: (11/2" & 2") Brass,
(3") Polyester -coated Cast Iron
Actuator: Plastic, Brass and
Stainless Steel
Diaphragm: Nylon -fabric,
Reinforced Natural Rubber
Seals: BNR and NR
77
and��nf�r �lcceasc�ries,
'ref�rt�r�serie, page$
Flow Chart
6
Model 300
Hydraulic Control Valve
Model 300 is a hydraulically operated
control valve, requiring a pressure
command to close.
e w 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.

Simple Design Delivem
Years of Trouble -Free Operatil
3/4' LOW4LOW PRESSURE REGULATOR
OUTLET PRESSURE VS. INLET tRtSSUM AT 1.3 GPM
0 28 56 84 112
Inlet Pressure (psi)
)v
40
30
20
10
0
140
Product Advantages
• Instant response to variations in pressure assures that outlet pressure will remain constant
regardless of inlet pressure.
• Pressure Regulators are preset with flows from 3.5 to 175 GPM.
• Manufactured from non -corrosive, high quality plastic and Bross, to withstand all fertilizers
and chemicals In cammoin use.
• Regulating unit has a stainless steel spring and screw.
• The EDPM rubber diaphragm creates a tight seal eliminating leakage.
• The rise versus the decline in outlet pressure has significantly decreased ensuring better
hydraulic perfornance.
• 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 Flow
Pre_-,� RegWator
• Improved in -line unit.
• Female threaded 3/4" X 3/4" connections.
• One-piece sealed unit regulates accurately
at low flows.
• Silicon diaphragm and stainless steel
spring — no leakage.
310 F6W
Appikafims
For use in drip and sprinkler irrigation
systems.
Speciffitcadons * Available in the following pre-set pressures:
9, 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

t
Flow Rate (CWjW)
EXAMPLE:
• Given Flow Role = 63 GPM, Nominal
required pressure = 20 psi:
• Using Pressure Regulator Model 2" x 6
(6 regulating units) will result in 10, 5 GPM
per regulating unit.
• 10, 5 GPM Per regulating Unit Will 16SUlt in On
output pressure of 18 psi. (See Regulated
Pressure vs. Flow Rote graph).
• Head loss of Pressure Regulator 2" x 6 at
63 GPM is 5 psi, (See Heed Loss vs. flow
Rate graph).
• Design pressure of inlet of Pressure Rft§Ul0tOT
should be 18 + 5 = 23 psi.
3.5 8 12 16 17.5
Flow Raic (per r-egulating unit)

L i
A
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. r1% 9 a
Standard Features (see diagram)
A. Self -Cleaning Filter
B. Needle Valve
C. Ball Valves
D. Quick Response Pilot (66-300)
E. Quick Response Relay 2" (for 6" and larger valves)
The 2" QR valve(bronze) is available in a globe or angle pattern. A
pilot (68-200) with a built-in needle valve ensures slow closure.
The QR valve is installed on a tee -junction in a pipeline and releases
excess pressure to protect the pipe network from dangerous surges.
The slow closing of the valve, adjustable with a needle valve,
prevents secondary surges,
Design Considerations
0 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.
ir +k I
0 A discharge pipe attached TO the downstream side ki e v 1-4 V
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
spring is standard for the 66-300
pilot,
FBI
68-200 66-300
For detailed information, material specifications and
dimensions, see the Dorot Basic Valve brochure.
C
Pilot Specs
68-200
66-300
Spring
Yellow
8-30 PSI
8-30 PSI
Green
14-140 PSI
14-100 PSI
Red *
115-360 PSI
30-190 PSI
Black
N/A
100-360
Dimensions
Port Size
V",
Height
6 V
9"
Width
2"
3 Y2`
Max, Press.
350 PSI
350 PSI
Materials
Body/borinet
Bross
Brass
Plunger
St. Steel
St. Steel
Diaphragm Not. Rubber Not. Rubber
0-rings Nitrile Nitrile
__,NETAF1M-..,_
\Quality Works
NETAFIM IRRIGATION, INC.
- ..... . .. .............
WEST COAST: 3025 E, Hamlion - Fresno. CA 93721
[phone] - FAX (209) 442-Sl 10
FAST COAST: 548 N. Douglas Ave. - Altamonte Springs, FL 32714
[phone] - FAX [phone]

BULLETIN I
Cut -Sheets for Flow Meter

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,F a
r,
g
pp ff
5,.st'St.F„S fi� G two
so I
i{ {
c

'�'� ,e t^Afnrc:b �nnv ww
i
f
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
'LOWVELOCITY
CONSTRUCTION
MIN. - MAX.
FLOW RANGES,GPM
STANDARD HIGHVELOGITY
CONSTRUCTION CONSTRUCTION
MIN. - MAX. - INT. MIN. - MAX.
DIMENSIONS
SHIPPING'
WEIGHT
POUNDS
A I
B1
132
C
D
E
F
G
H
K
3
40-250
45-250-350
NIA
18
81/4
5
11/8
7
65/8
8
3/4
53/16
9
85
4
50-500
55-500-700
200-700
18
10
63/16
11/8
7
7718
8
3/4
53/16
9
122
6
90-1200
120-1200-1500
300-1500
22
12112
81/2
13/8
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
718
71/4
9
237
10
125-2000
180-2000-3000
500-3500
26
171/2
12314
15/8
10
151/4
16
1
81/2
11
310
12
150-2800
200-3000-3500
800-5000
28
201/2
15
113/16
10
173/4
16
11J8
9112
11
400
14
250-3750
300-4000-4500
1000-6000
42
23
161/4
115/16
12
201/4
20
11/8
101/2
131/2
600
16
350-4750
400-5000-6000
1200-7500
48
251/2
18112
21116
12
221/2
20
11/4
111/2
131/2
800
18
450-5625
700-6000-7500
1500-9000
54
28
21
23/16
15
243/4
24
11/4
121/2
131/2
1080
20
550-6875
850-8000-9000
2000-12000
60
301/2
23
27116
15
27
24
11/4
131/2
131/2
1260
24
800-10000
100010000-13500
3000-15000
72
36
271/4
211/16
'18
32
24
11/2
173/4
23
2040
30
1200-15000
1800-15000-21000
4000-25000
84
43
35
215/16
18
391/4128
13/4
203/4
23
3220
36
1500-20000
2000-20000-30000
5000-35000
96
50
42
33/16
20
46
32
2
233/4
23
4550
42
2000-28000
3000-30000-40000
6000-50000
108
57
507/16
37/16
24
523/4
36
2
1 28
36
5900
48
2500 35000
5500-35000-50000
7000-60000
120
65
587/16
39/16
24
603/4
40
2
31
36
7200
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 flows refer to Model
» TM-01 turbine meters.
x,:w^,rt.as.-,,
10 A
� t�)A'Z" FA Z1 r" _r 40114r 1,° f6l
�,�� �`�: k S x F �,, ' k ` ,-
1 f t Sr

BULLETIN J
Cut -Sheets for Disc Filtration System

?4
i juil[vA r®mA-
Fully Automatic Disc Filters
For 50-800 GPM Flow Ranges
4
2
w
1.0
0.4
0.2
2n & V DISC-KLEEN FILTERS
Headloss
40 100 200 400 1000 2000
Flow Pate (GPM)
uct AchmnWges
• Quick Installation — factory assembled and tested, arriving on a pallet ready for hook-up
and immediate operation.
• Less Maintenance — molded spine, chemically resistant and performs reliable backflush.
Manual cleaning is practically eliminated.
• Filtration Grade Versatility — filtration discs can be changed quickly and easily from
40 mesh up to 200 mesh.
• Optimizes Irrigation — less backflush time means more uniform application of water in the
field.
• System Flexibility — each Disc-Kleen Battery is capable of handling a wide operational flow
range.
• Lasts Longer — manufactured from engineered synthetics to resist rust and corrosion from
chemicals and weather.
• Standard with installed polypropylene drain manifold.
F111ratIon Process
As dirty water travels through a
Disc-Kleen Filter, debris is captured
along the walls and in the grooves of
the channels in the filter element.
During the backflush cycle, the valve
changes position, the pressure in the
outlet manifold loosens the discs
automatically. A specially designed
nozzle system inside the filter stack
then sprays pressurized water against
the loosened discs, spinning them
clean quickly and efficiently. After
backflushing, the stack of discs
automatically compress to resume
filtration.
No of Nladfold !
Part ;Number Size :: Ei[ters, " :,Size
3" Disc-ICleen
Filter Battery
lllica$ons
• 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.
Specificatilons
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-Rings and Seals: EPDM

;tea
Mmuii"ALAbIaLaL
IMPORTANT NOTE: We have categorized water quality as a guideline for filtration requirements. Be aware all water qualify categories shown above are general. Your water quality may vary. If your water
contains more ihan two path per million of sand, a sand separator is recommended. If in doubt, consult an authorized Netafim USA dealer.
a

BULLETIN K
Cut -Sheet for Rainbird Rain Gauge

A?AlAr�*BIRD(@ TECH SPECS
Rainfall and Wind Speed Sensors
Rain Bird Rainfall Gauge
The Rain Bird Rainfall Gauge customizes the
weather data gathering features of
Maxicomz by providing site -specific rainfall
measurements. The central controller
retrieves this information daily, adjusting
station runtimes using the site -specific
weather data. The Rainfall Gauge may be
used to automatically interrupt Maxicomz
during an irrigation cycle if it starts to rain.
If enough rainfall occurs, further irrigation
will be cancelled. If only a small amount of
rainfall occurs, irrigation will resume,
adjusting runtimes for the amount of
rainfall that occurred.
Features
• Identifies localized rainfall and adjusts
system operation accordingly
• Watering cycle can be interrupted or
cancelled when rainfall commences
• Provides site specific rainfall
measurements in increments of 0.01"
(.025 cm)
• Heavy-duty construction, with a gold
anodized aluminum collector funnel and
white baked enamel coated aluminum
sensor housing
• Filter screen for capturing debris
• Integrates into the Maxicomz system
using the Rain Bird pulse decoder for
two -wire CCU systems, or directly to the
sensor input on ESP -Site and IvIAXILink
satellite controllers
Specifications
• Resolution: 0.01" (.025 cm)
• Accuracy. 1.0% at 1 " (2.5 cm) /hour or less
• Average switch closure time: 135 ms
• Maximum bounce settling time:.75 ms
• Maximum switch rating: 30 VDC @ 2 A,
115 VAC @ IA
• Temperature limits: +32° F to +125° F
(0° C to +52' C)
• Humidity limits: 0 —100%
• Height: 4.5" (11,4 cm)
• Weight: 1.5 pounds (0,68 Kg)
• Receiving orifice diameter: 3.80" (9,7 cm)
• Cable: 60 feet (18 meters)
Model
• RAINGAUGE
Rain Bird Anemometer
(Wind Speed Meter)
The Rain Bird Anemometer provides
additional customization to the Maxicomz
Central Control system by providing site -
specific windfall measurements. Local wind
speed is captured by the Wind Speed Meter
and input to the Cluster Control Unit (CCU).
The CCU can interrupt irrigation when wind
velocity reaches a programmed set point.
Interrupting a watering cycle during windy
conditions saves water, avoids property
damage, and improves sprinkler distribution
uniformity.
Features
• Precision three -cup anemometer for
measuring wind velocity
• Balanced rotor and low friction bearings
detect wind speeds from 4 MPH to
80MPH (6,5 to 128 km/h)
• Electronics supplied with a weather tight
enclosure exceeding NEMA 4 and 6
specifications
• Mounting bracket and 20 feet (6 meters)
of cable
• Identifies localized wind speed and
adjusts system operation accordingly
• Watering cycle can be interrupted during
windy conditions
• Integrates into the Maxicom- system
using the Rain Bird pulse decoder for
two -wire CCU systems, or directly to the
sensor input on ESP -Site and MAXILink
satellite controllers
Specifications
• Power supply: 5 to 24 VDC
• Current draw: 3 to 7 mA
• Output signal: K = 1.6965, offset of +0.059
• Cable: 20 feet (6 meters)
• Weight: 1.3 Lbs (0,6 Kg)
• Dimensions: 22"L x 8"W x 8"H (56 cmL x
20cmW x 20cmH)
Model
• ANEMOMETER (Wind Speed Meter)
Rainfall Gauge
Anemometer
HOW t6 Speccfy
RAINGAUG
ANEMOMETER

J
E - RAIW�kBIRDS
Specifications
_ Model: RAINGAUGE
eA 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
4 increments of 0.01" (.025 cm). The rainfall
gauge shall have three mounting feet for use
,° =} on flat surfaces as well as a side bracket for
mast mounting. The rainfall gauge shall
operate in temperatures ranging from +32' F
to +125° F (0° C to +52° Q. 60 feet (18
meters) of 2-conductor cable shall be
included. This rainfall sensor shall be Rain
Bird Model RAINGAUGE.
Model• ANEMOMETER
The wind speed meter shall be a three -cup
anemometer providing wind speed
measurements from 4 — 80 miles per hour
(65 to 128 km/h). The wind speed meter
electronics shall be housed in a weather -tight
enclosure exceeding NEMA 4 and 6
specifications. The wind speed meter shall
include a mounting bracket and 20 feet (6
meters) of cable. This wind speed meter shall
be Rain Bird Model ANEMOMETER.
Rain Bird Corporation
Contractor Division
970 West Sierra Madre Avenue, Azusa, CA 91702
Phone: [phone] Fax: [phone]
Rain Bird Corporation
Commercial Division
6991 East Southpoint Road, Tucson, AZ 85706
Phone: [phone] Fax: [phone]
Rain Bird International, Inc.
145 North Grand Avenue, Glendora, CA 91741
Phone: [phone] Fax: [phone]
Rain Bird Technical Service
[phone] (U.S. only)
www.rainbirdcom
CentralContro►@rainbirdcom
k4' Rain Bird. Conserving More Than Water.
® Registered trademark of Rain Bird Corporation.
O 2002 Rain Bird Corporation 9102
i
D37238A

BULLETIN L
Drip Line Cut Sheets

NEWIMUSA
The Most Successful Pressure Compensating
Diripper in the History of Irrigation
Industry`s Widest Flaw Path ... -- Self -Adjusting
Wider cross-section allows large Diaphragm
particles through short flow path Continuously adjusts
s' to varing water
: * prassares - crushing,
mini'rizing and
�� , flushing debris.
Large Filter Inlets,
Secondary Filtration
Reduces clogging and
maintains the essential
supply of water to the
dripper for constant
delivery of water flow.
Pressure
Compensating
Bath and Outlet
Delivers precise water
applications anywhere
in the field.
I, y
_. Increased Flow Path Velocity
Commonly used turbulent drippers have overlapping tooth patterns,
easily catching debris.
Turbonet Technology improves dripper'perfarmonce by widening
the tooth pattern, maximizing flow, path velocity, allowing
contaminants to pass easily through the dripper, virtually eliminating
plugging.
Product Advantages
• Wide pressure range (7 to 60 psi) produce uniform dripper flow rates• longer runs and steep
topographies are irrigated with high uniformity.
• Mechanical barrier prevents root intrusion - ideal for sub -surface irrigation (SDI).
• lowest coefficient of manufacturing variability (Cv) in the industry.
•Seamless, one-piece construction prevents damage to drippers during installation and retrieval.
• Design flexibility and performance with various dripper flows and spacings allow for specific
application rates and controlling of wetting pattern in different soil types.
* Pressure compensating feature delivers precise water applications anywhere in the field.
Applications
• For sub -surface or surface applications.
• For tree, vine, row crops, €;.reenhouse and
nursery.
• Multi -seasonal use,
• For undulating fields.
Specificadons
Nominal flow rates (GPH)c .32, .42, .53,
.62, .92
Common spacings: 24", 30" 36", 42.25" 48"
Recommended filtration: 120 mesh
Inside diameter:.540 - 16mm (45 roil)
.570 - 17mm (45 mill)
.620 - I8mm (45 mil)
.690 - 20mm (48 nail)
.820 - (35, 45'niil}
,.. VineLlne
t Vineyard solutions
Pre -Installed Adjustable Dtipperline Ring
See back for details.
PRECISION IRRIGATI'ONTB"

E
® i
Flows (GPH):
- .32, •42, .53, .62, ,92
Wall thickness (mil): 45
RAM 57
Flows (GPH):
± .32, A2, .53, .62> .92
Wall thickness Wit: 45
!RAM
620
Flows (GPH):
.32, .42, .53, .62, .92
Wall thickness (mil), 45
V
RAM 690
Flours (GPH):
_ .32, .42, .5 i, 62, 92
Well thickness (Wit): 48
i
RAM $20
Flows (GPH)-
.32:.42, .5 i> 62, .92
Wall thickness (mil). 45
ti
0 ?Oil 41)0 b60 800 4, 1200 1491 00
D. NO WfJ 101
kr�t Len�rh'CfY j�
25
I`
'0
7
800 WOO
1?00
5

Ram Technical Infonnation
6
.4
.2
RAM Flow Rare vs. Pressure '
0 10 20 30 40 50 60
Pressmn, j),i)
DRIPPER FLOW PATH DIMENSIONS
OH JS"
0.42 GPH 75"
.037" 04
0.53 OPH .75",
0.62,GPH TSa,
-0.044"
0.92 OPH
.0477., Caw
PACKAGING DATA
340
45.-J
0Q
5
6,90.,,
'48
3 000!",:,
47,$
20 coils per pallet.
ViiineLlne Vineyard Solutions
Pre -installed Adjustable Dripper line Ring
- Easily adjustable — moves from one,end of the dripperline to the other preventing wale; migration
& Ecoflomicol — saves labor costs
* Flexible options — available with Rain of Triton Hen/wall Nipperlines
e Available for 540, 620, and 690 sizes.
, Pre -installed at Netafirn USA
Netafim USA — Delivering Total Growing Solutions
Dripperlines ® Filters e Valves a Air Vents - Sprinklers * Automation a Flow Meters
For Agriculture, Greenhouse & Nursery and Landscape
Description of Ram's
Advanced Pressure
Compensatimrso 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 elastomers to
withstand chemicals and. fertilizers. The Ram
dripper contains a diaphragm that
continuously adjusts to vaiyiti,-,, water
pressure to ensure a constant flow rate. The
diaphragm allows particles to pass through
the dripper, promoting reliable performance
and a longer system life.
This continuous flushing feature and wide
flow path keep drippers flowing at optimal
rates without clogging or interrupting
operation.
Parlicles that may
sMi accumulate at the
dripper outlet can
cause a reduction of
flow.
Dripper resumes 7
normal operation. koW?"
4
.7,
PRECISION IRRIGATION'"
For more information call your Authorized
Netahm USA Dealer or call Netalim USA
Customer Service at (888; 638-2346.
Aow 3"'07

BULLETIN M
Pole Blower Curve and Cut -Sheet

Daytone PSC and
Shaded Pole Blowers
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 8" Lead Length.
NOTE: Not suitable for use with speed -controlled devices.
Dimensions
in. (mm)
13.109
(332.98)
1 i
0 0
0 0
078013
00).a
60HZ
(inwg) (MMAq)
1 25.4
0.8 20.3
0.6 15.2
OA 10.2
0.2 5.1
0 0
(CMM)
0 4.53 9.06 13.6 18.12 22.65
iIiiiiiiiIir!.ii_iiii-(CFM)
0 160 320 480 640 800
610 570 — — 115230 2.75 @115V
1.45 @230V
(261.00)
Features
• PSC motor
• Baked enamel Gray finish
• Heavy gauge steel housing
• All position Mounting
• Maximum Ambient Temperature
104°F
• Suitable for 50Hz operation
Additional Benefits
• Permanently Lubricated Ball -Bearings
• Extruded Aluminum Blower Frame
for Increased Rigidity
• Auto -Thermal Protection
60
®
Motor Component Recognition C US E47479

BULLETIN N
Back -Up Generator Cut -Sheets

Descilption Features
Cummins Power Generation commercial generator sets
are fully integrated power generation systems providing
optimum performance, reliability and versatility for
stationary and prime power applications.
This generator set is designed in faclittles
certified to IS09001 and manufactured in
facilities certified to ISS69001 or iS0900 .
The Prototype Test Support (PTS) program
verifies the performance integrity of the
generator set design. Cummins Power
Generation products bearing the PTS symbol
meet the prototype test requirements of NFPA
110 for level 1 systems.
All low voltage models are CSA certified to
cal,
product class 4 15-01.
The generator set is available Listed to
U12200, Stationary Engine Generator
Assemblies.
Engine certified to U.S. EPA lslonroad Source
Emissions standards, 40 CFH 89, Tier 3.
Cu rise 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 with low reactance /S pitch
windings, low waveform distortion with non -linear heads
and fault clearing short-circuit capability.
Control system -"The PowerCornmando 1.1 electronic
control is standard equipment and provides total genset
system integration including automatiG 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 compliance. The optional PowerCommand
2.2 control is UL 508 Listed and provides Am $entry'
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.
Warmnty and service - Backed by a comprehensive
warranty and worldwide distributor network.
Standby rating
Prime rating
Continuous rating
Data sheets
Made]
60 RZ
SD NZ
so Fix
60 14M
60 NZ
60 Ha
60 1IZ
'so NZ
DSGAA
i llti 125
113}
D-3349
DSGAS
125156
113141
b-335fi
DSDA►D
15f) 13&
135 169
D-3351
•L)2008 I Cummins Potter Generation Inc. I Aff rights reserved i Specifications subject to change without rw&e I Cummins Power Generation
and Cummins are registered trademarks at Cummins Inc. PowerCommand, InPower and 'Our energy working for you." are trademarks of
Cummins Power Generation. other company, product or service flames may be trademarks or service marks of others.
S-1540 (4108)

Governor regulation cuss
180 8528 Part 1 Mass G3
Voltage regulation, no load to full load
z 1$0
Random voltage variation
+ 0.5
Frequency regulation
Random frequency variation
lsochronous
0.25%
Radio frequency emissions compliance
Meets requirements of most industrial and commercial applications.
Engine specifications
Design
4 cycle, turbocharged and charge air aftercooted
Bore
107 mm (4,21 ink
Stroke
124,0 mim (4,88 in)
Displacement
&69 L (408 in)
Cylinder block
Cast Iron, in -line; 6 cylinder
Battery capacity
1100 amps minimum at ambient temperature of -flit °C to 0 °C
°F to 32 a
Battery charging alternator
100 amps
Starting voltage
12 volt, negative ground
Fuel system
Direct in;ection. number 2 diesel fuel
Fuel fitter
Single element,10 micron filtration, spin -on fuel #iiterwith water
se tar
Air caner type
Dry replaceable element
Lube oil filter typed
One spin -on, full flow filter
Standard cooling system
High ambient radiator
Alternator i
r
t
Design
Brushless, 4 pole, revolving field
Stator
213 pitch
Rotor
Single haring, flexible disc
Insulation system
Standard temperature rise
Class H
150 -C Standby @ 40.0 ambient
Exciter type
Torque match (shunt) standard, PG optional
Phase rotation
A N}, 8 M, C (t }
Alternator cooling
Direct drive centrifugal blower fan
AC waveform total harmonic distortion
c 5% no load to full lineal' load, { 3% for any single harmonic
Telephone Influence factor (TIF)
c 50 per NEMA MG1-22.43
Telephone harmonic factor (THF)
< 3
Available It
vl
60 Nz Three titre- a flfine-flue
eO Hz Single phase fine-neutral#line-line
- 110/190 . 115/230 Delta o 127/220 •240/416
•110/220 - 1151230
• 1201240
- 110/220 .',1201208 - 1391240 - 2551440
- 115/200 o 120/240 Delta • 2201380 • 27i/480
t...
- 230/400 - 347/600
* Note: Consult factory for other voltages.
Generator set options and accessories
Engine Atterrtator
Exhaust system
0
Power0ommand Network
0 120 V, 150 W lube oil heater 0 105 °C rise alternator
13 Heavy duty exhaust elbow
Communications Module
51 1201240 V, 1500 W coolant 9 125 IC rise alternator
0 Slip on exhaust connection
(NCM)
hater Q 120 V,100 W anti -condensation
aeiiei"a$4s:i" set
0
Remote annunciator panel
4
Fuel System heater
0 PMG excitation
Satiety
0
13
Spring isolators
UL2200listed
24 hour dual wall iota -base 0 Single phase
charger
�
2 year prime over warrant
Y R P y
tank
EndoBattery
Enclosure: aluminum, steel,
0
2 year standby power
weather protective car sound
warranty
attenuated
5 year basic power warranty
N Main fine circuit breaker
` Note: Some options may not be available on all models - consult factory for availability.
Our eneMy worlding for you.rlf
z a .rq=T I ,i qs V_fLoxlm
C,2008 1 Cummins Power Generation tnc. I Xt tights reserved l Specificationssubject to change wbout notice I Cummins Power Generation
uitwer
and Cummins are registered t edernaft of Cummins Inc. PoweaComman4. InPower end "Our emrgy wprking far you." are trademarks of
Generation "
Ce
Cummins Power Ge om Otner compani. P Suci cr scarce names may he trae9emarhs
or service marks esf others
S-9544f (4/08)

wControl 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).
Control - Provides battery monitoring and testing
features and smart -starting control system-.
In erT - PC -based service tool available for detailed
diagnostics.
- Network interface (standard) to
devices such as remote annunciator for NFPA 110
applications,
Control boards s - Potted for environmental protection.
High ambient a tion - Suitable for operation in
ambient temperatures from -47 °C to +lit °C and
altitudes to 13,000 feet (5000 meters).
Pfttatype to - UL, GSA and CIE compliant.
AC protection
• Over current warning, and shutdown
:,
• Over and under voltage shutdown
• Over and under frequency shutdown
L :a
• Over excitation (loss of sensing) fault
Field overload
Engine protection
• Overspeed shutdown
a Low tail pressure warning and shutdown
a High coolant temperature warring and shutdown
Low coolant level warning or shutdown
• Low coolant temperature warning
e High, low and weak battery voltage warning
-,
• Fail to start (overcrank) shutdown
• Fail to crank shutdown
• Redundant start disconnect
• Cranking lockout
o Sensor failure indication
• Low fuel level warding or shutdown
Fuel -in -rupture -basin warning or shutdown
Operator/display panel
* Manual off switch
t
• Alpha -numeric display with pushbutton access for
viewing engine and alternator data and providing setup,
controls and adjustments (English or international
symbols)
.y_
• LIT lamps indicating genset running, not in auto,
common warning, common shutdown, manual run
mode and remote start
+ Suitable for operation in ambient temperatures from
-20 °C to +70 $G
Aftemator data
• Line -to -neutral AC volts
¢ Lure -to -line AC volts
• 3-phase AC current
• Frequency
• Total WA
Our energy working r your
?t;
Standard control fun terry
Engine data
• OC voltage
• Lube oil pressure
o Coolant temperature
Other daft
• Genset model data
• Start attempts, starts, running hours
• Fault history
• R5485 Modbue interface
• Data logging and fault simulation (requires InPower
service tool)
Dilgiltal governing (optional)
• Integrated digital electronic isochronous governor
• Temperature dynamic governing
Digital voltage regulation
• Integrated digital electronic voltage regulator
• 2-please line -to -line sensing
• Configurable torque matching
Control functions
• Time delay start and cooldown
• Glow plug control (some models)
• Cycle cranking
• PCCNet interface
• (2) Configurable inputs
• (2) Configurable outputs
• Remote emergency stop
Options
n Auxiliary output relays (2)
1] 120/240 V, 100 W anti -condensation heater
❑ Rewrote annunciator with (3) configurable inputs and (4)
configurable outputs
a PMG alternator excitation
tj PowerCommand for Windowe remote monitoring
software (direct connect)
❑ Auxiliary, configurable signal inputs (8) and
configurable relay outputs (8)
C AC output analogue meters
C3 PowerCommand 2.2 control with AmpSentry
protection
Standard Po erCarnmand
1.1 control operator/display
panel'
n2008 I Cummins Power Generation Inc. I All rights reserved I Specifiicatrons subject to change without notice I Cummins Power Generation
and Cummins are registered trademarks of Cummins inc. PowerCommand, inPower and 'Our energy working for you.' are trademarks of
Cummins Power Generaion. Other company, product or service names may be trademwilz or service marks of others.
S-1544f j4108)
Optional AC output
analog meters
Pores e
Generation

This outline drawing is for reference only. See respective model
data sheet for specific model outline drawing number.
Model
Dim 0A`1
mm (in.)
Dim "S"
mm (in.)
Dim "C"
mm (in.)
set Weight*
dry kg (Ibs)
Set Weight*
wet kq )ilbs)
AA
2656(104.6)
1100(43.3)
1549(61)
1180(2602)
DSGAS
2656(104.6)
110D(413)
1549(61)
1225(2700)
DSGAC
2656(104.6)
1100(43.3)
1549(61)
1263(2784)
* Note. Weights represent a set with standard features. $ee outline drawings for weights of other configurations.
Cummins Power Generation
1400 73� Avenue N.E.
Minneapolis, MN 55432 USA
Telephone: [phone]
Fax: [phone]
Important. Back feed to a utility system can cause electrocution and/or property damage. Do not connect to any btfilding's electrical system
except through an approved device or after building main switch is open.
Our enerlding for Vou.—
vmmm,
02008 1 Cummins Power Generation Inc. I Aft tights reserved I Spectlications wbject to charge withoto notice f Curnrrons Power (3arwatlon Power
and Curravins we registered tradernaft of Curna;Ins Im PowarCorrimand, InPower and 'Our energy woWng for you.' are traderriaft of -leneration
Cummins Power Generation. Other company, product or service names may be tradernaft or service niaft of oftm-
S-1544f (4108)

BULLETIN O
Turbidity Meter

experience + accuracy + simplicity

EXPERIENCE
The Model 1720E Low Range Turbidimeter reflects an astound
years of Hach leadership in turbidity measurement science. Metrol
water treatment systems, rural water utilities, wastewater trey
' plants large and small, and industrial processes of every kind - a
relied on Hach turbidimeters for nearly five decades. In fact, Ha
the largest turbidimeter installation base in the world.
Operators and engineers alike know they can count on the
formance of Hach turbidimeters and calibration standards as wl
the experienced Hach personnel designing, manufacturing, se
installing, and supporting these systems. Additionally, Hach of
;. 2-year warranty on the 1720E, compared to the 1-year wart
offered with many other turbidimeters on the market. Hach is
` only the world's turbidity leader, but also your partner in turb
measurement, filtration management, and treatment pro
optimization solutions.
ACCURACY
Now, the 1720E Turbidimeter combines Hach's proven design, demonstrat
accuracy and reliability, plus innovative elements that add more powe
and utility to your low-level turbidity monitoring program:
> Built-in bubble removal system - eliminates falsely high readings
at low levels
> Sensitivity -'fast response to fine changes in low-level turbidity
> Repeatability -not effected by sample flow and pressure
SIMPLICITY
> Simplified two -module design -sensor and controller interface
with simple plug & play connection
> Reduced instrumentation - controller accepts two sensors;
adding a second 1720E sensor unit gives you two complete turbidir
> Easy calibration and verification - with no interruption in sample flow
.. _i
THE BEST TOOL FOR EFFLUENT
MONITORING' IREQUIREMEN

PRINCIPLE OF OPE ON
NPHLOETIC EAS.EET
Incandescent light directed from the sensor head asse91
l.�`down into the turbidimeter body is
scattered by suspended particles in the sample. Thespnsor's submerged photocell detects light
scattered at 90° from the incident beam.
SAMPLE FLOW P TH
Sample enters the center column of the turbidimeter, rises into the measuring chamber and
spills over the weir into the drain port. This configuration results in an optically flat surface
free of turbulence:
SIMPLIFIED CALIDATIO1
One -point calibration with preparStablCal'�' Stabilized Formazi "Solution eliminates the
errors USEPsof cee tedlme suspension dilution, takes less than two minut per sensor, and is a
p
Lng
�,j
P

POWERFUL DATA MANAGEMENT
AND COMMUNICATIONS
t...,J
COLLECTIONDATA L
The 1720E Turbidimeter sc100 Controller receives data from one or two sensors. Its built-in
data logger collects turbidity measurements at user selectable intervals (1-15 minutes),
along with calibration and verification points, alarm history, and instrument setup changes
for 6 months. Local display, recall, graphing, and trending in CSV format make chart
recorders redundant:
DIRECT DIGITAL COMMUNICATION
a This revolutionary smart controller is a new standard for Hach instruments. Not only will it
accept a rapidly increasing number of Hach analytical tools; but it will reduce your operator
training load as a wide variety of instruments will share the same interface and control method.
The sc100 Controller also offers optional Digital Direct solutions for direct

Range
Accuracy"
Displayed Resolution
Repeatability"
Response Time
Signal Average Time
Sample Flow Required
Storage Temperature
Operating Temperature
Operating Humidity
Sample Temperature
Recorder Outputs
Alarms
Power Requirements
Sample Inlet Fitting
Drain Fitting
Enclosures
Digital Communications
Wireless Communication
Compliance
Certification
Safety:
Immunity:
Emissions
Class A:
Dimensions
Mounting
Shipping Weight
*Subject to change without notice.
"" Defined according to ISO 15E39.
a
0.001-100 Nephelometric Turbidity Units (NTU)
± 2% ofreading or±0.015 NTU (whichever is greater) from 0 to 10 NTU;
± 50/o of reading froln 10 to 40 NTU; ± 100/b of reading from 40 to 100 NTU
0.0001 NTU from 0 to 9.9999 NTU; 0.001 NTU from 10.000 to 99.999 NTU
Better than ± 1.0% of reading or ±0.002 NTU, whichever is greater
For a full-scale step change, initial response in 1 minute, 15 seconds
User Selectable ranging from 6, 30, 60, 90 seconds; user default
30 seconds
200 to 750 mL/minute (3.1 to 11.9 galthour)
-20 to +60' C (-4 to 140' F)
0 to 50o C (32 to 122° F) for single sensor system,
0 to 40' C (32 to 104' F) for two sensor system
5 to 95% non -condensing
0 to 50' C (32 to 122' F)
Two selectable for 0-20 mA or 4-20 mA. Output span programmable
over any portion of the 0-100 NTU range; built into the sc100
Controller
Three set -point alarms, each equipped with an SPDT relay with
unpowered contacts rated SA resistive load at 230 VAC; built into the
sc100 Controller
100-230 VAC, 50/60 Hz, auto selecting; 40 VA
1/4" NPT female, 1/4" compression fitting (provided)
1/2" NPT female, 1/2" hose barb (provided)
NEMA-4XIIP66 Controller
Network card compatible; MODBUSIRS485, MODBUSIRS232,
Lon Works° protocol (optional)
IR Port on the sc100 Controller to download into a handheld Personal
Digital Assistant (PDA) or laptop computer via MODBUS
Standard Methods 2130B, USEPA 180.1, Hach Method 8195
Listed by ETL to UL 61010A-1: Certified by FTL to CSA C22.2
No. 1010.1: CE certified by Hach Company to EN C1010-1
CE certified by Hach Company to EN61326 (industrial levels)
EN 61326, CISPR 11, FCC Part 15, Canadian Interference -Causing
Equipment Regulation ICES-003
Turbidimeter Body and Cap: 10 x 12 x 16 inches (25.4x 30.5 x 40.6 cm)
sc100 Controller: 5.67 x 5.67 x 5.91 inches (14.4 X 14A X 15.0 cm)
Turbidimeter Bodyand Head Assembly: wall and floor stand
sc100 Controller: wall, pole, panel, and floor stand
1720E Turbidimeter and sc100 Controller: 13.5 lbs. (6.12 kg)
1720E Turbidimeter: 10 lbs. (4.54 kg)

HOW TO ORDER
60101-00 1720E Turbidimeter with sc100 Controller
60101-01 1120E Turbidimeter, Sensor Only
r7lsq 1720E with DigitaiDirect communications
60101-02
1720E/sclo0 with MODBUS/RS485 output
IL,4
60101-03
1720E/sc1o0 with MODBUS/RS232 output
60101-04
1720E/5c100 with LonWorks output
60101-05
1720E/sc100 with PROFIBUS output
r'
CABLES*
57960-00
25 ft (7.7 M) Extension Cable
46306-00
Power Cord with Strain Relief (125 VAC)
46308-00
Power Cord with Strain Relief (230 VAC), European Style Plug
"Note: Power cables must be ordered separately.
OPTIONAL
ACCESSORIES
ICE-PIC
Verification Module/1720E:
52250-00
20 NTU
52215-00
1 NTU
STABLCAL COMPARATIVE CALIBRATION STANDARDS (far 1720E, 1720D,
and 1720C Turbid!meters)***
26601-53 20.0 NTU, 1 L each
— Note: Calibration Cylinder must be ordered separately.
STABLCAL VERIFICATION STANDARDS
26598-53 1.0 NTU, 1 L each
27463-53 40.0 NTU, 1 L each
26979-53 0.3 NTU, 1 L each
26980-53 0.5 NTU, 1 Leach
27233-53 0.1 NTU, 1 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 #44156-00
44153-000 Calibration Cylinder, 1L
57432-00 Floor Stand
MODEL SC100TM CONTROLLER
The Model sc100 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.
MODEL SCIOOOTM CONTROLLER
Get the same great features as the sc100 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
sc1000 Controller is also expandable and upgradeable to
easily adapt to you needs.
Lit. No. 2446
155 Printed in U.S.A.
0 Hach Company, 2005. All rights reserved.

ATTACHMENT M
Pole Blowe Curve and Cut -Sheet

ATTACHMENT N
Back -Up Generator Cut -Sheets
,w
:,j
�,_J

ATTACHMENT 0
Turbidity Meter
71
I=