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HomeMy WebLinkAboutWQ0029945_More Information (Received)_20231109Project: Summerhouse WWTP By: DKP CK By: Goal: 112 GPM from EQ basin to screen/splitter box (YLWL (,PPWL Low Water Elev. 30.00 44 Pump Start Elev. High Point Elev 42.00 42 High Point Elev. - 2 High Point Elev. - 3 STATIC HEAD 12.00 -2 STATIC HEAD - 2 -42.00 STATIC HEAD - 3 -42.00 Pump Design Flow Rate: 500rilifi I GPD GPM Pump Design Flow Rate: 3A22 Pumn I Discharee Pipe Dia. Description [ L3l 1 6 ' EQUIV. QUAN ITI Y LENGTH 90 Elbow 30.60 45 Elbow 0.00 STD Tee (div) 31.00 Check valve I 39.00 Coupling 0.00 Gate Valve 0.00 Plug Valve i 9.00 STD Tee (->) 0.00 Butterfly 0.00 Red 1/4 0.00 Red 1/2 0.00 Red 3/4 0.00 Sud. Ent. 0.00 109.60 Le ihufRun I 12 Ift 122 TOTAL LENGTH Hazen -Williams Coeff. "C" I 110 I Pipe, Type, Class DIP( 52 f Pipe inside diameter 6.16 in Farce :Hain Manlrold to 5o11tter IMx Pipe Dia. Description (in) I 6 EQUIV. QUANTffY LENGTH 90 Elbow I 1 15.30 45 Elbow 0.00 STD Tee (div) I ] 31.00 Check valve I 0.00 Coupling I 0.00 Gate Valve I 0.00 STD Tee (->) I 0.00 Butterfly I 0.00 Red 1/4 I 0.00 Red 1 /2 I 0.00 Red 3/4 I 0.00 Sud. Enl. I 6.00 Total 52.30 Length of Run I 23.5 (TOTAL LENGTH 76 Hazen -Williams Coeff. "C" ' 110 Pipe, Type, Class DIP 33 _ Pipe inside diameter 6,16 Date: 5/10/2023 Date: '��<<illllrrrr��� CA!4'O rifr � r rS�nEAAL ' = 2il0/%.' �j \ I Project: Summerhouse WWTP By: DKP Date: 5/10/2023 CK By: Date: IPS OPERATING ONLY PUMP I OPERATING- LWL I PS I Pump I ❑ischargc Manifold - 1. mmp runnine FLOW VELOCITY HEAD VELOCITY HEAD TOTAL HEAD ill (GPM) (FT,/S) (FT.) (FT./S) (FT.) (FT.) 34.7 0.37 0.02 0.37 0.02 12.0 - - 69.4 0.75 0.08 0.75 0.08 12.2 104.2f 1.12 0.17 1.12 0.17 12.3 138.9 1.49 0.28 1.49 0-28 12.6 173.6 L86 0.43 1.86 0.43 12.9 208.3 2.24 0.60 2.24 0.60 13.2 743.1 2.61 0.79 2.61 0.79 13,6 277.8 2.99 1_01 2.98 1.01 14.0 312.5 3.36 1,26 3.36 1.26 14.5 3472 3.73 1.53 3.73 1.53 15.1 381.9 4.10 1.83 4.10 1.83 15.7 416.7 4.48 2.15 4.48 2.15 16.3 451.4 4.85 2.49 4.85 2.49 ITT 486.1 5.22 2.86 522 2.86 17.7 PS OPERATENG iDNLY PLIM P 1 0PFRAT ING- HVfL Per Pump from Split to HeadCell Pump 1 Dischar a Manifold - 1 mmp running ;FLOW VELOCITY AD VELOCITY HEAD TOTAL HEAD (GPM) (FT,) (FT./S) (FT.) (FT.) (FT,) - - - --- -'T 34.7 0.3 0.02 0.37 0.02 -2.0 69.4 0.75 0.08 0.75 0.08 -1.8 104.2 1.12 0.17 1.12 0.17 •1.7 138 9 1.49 0.28 1.49 0.28 -1.4 173.6' 1.86 0-43 1.86 0,43 -1.1 208.3 224 0.60 2.24 0.60 -0.8 243.1 2.61 0.79 2.61 0,79 -0.4 277.8 2.98 1.01 2.99 1.01 0.0 312.5 3.36 1.26 3.36 1.26 0.5 347.2 3.73 1.53 3.73 1.53 1.1 381.9 4.10 1.83 4.10 1.83 1.7 416.7 4.48 2.15 4.49 2.15 2.3 451.4 4,85 2.49 4.95 2.49 3.0 486.1 5.22 2.86 5.22 2.86 3.7 LWL Pump 1 Pump 1 2 Pumps Operetin, Flow Pump Head Pump Head (gpm) (ft) oq 34.7 12.0 12.1 69,4 12.2 12.3 104.2 12.3 12.5 138.9 12.6 12.9 173.6 12.9 13.4 209.3 13.2 13.9 243.1 13.6 14.6 277.8 14.0 15.3 312.5 14.5 16.1 347.2 15.1 17.0 <.-- 381.9 15.7 17.9 416.7 16.3 19.0 451.4 170 20.1 486.1 17.7 21.3 <..- 92.4 La�,HW C-factor of 100 Project: Summerhouse WWTP By: DKP CK By: Date: 5/10/2023 Date: HWL Pump 1 Pump 1 2 Pumps ❑peraliac Flow Pump Head Pump Head %�pPm] `34.7 (it) {Ft -2.0 69.4 -1.8 -1.7 104.2 -1-7 -1.5 138.9 -1.4 -1.1 s-- ADF 173.6 -1.1 -0.6 208.3 -0.8 -0 1 243.1 -0.4 0.6 277.8 0.0 1.3 312.5 0.5 2.1 347.2 1.1 3.0 PDF 381.9 1.7 3.9 416-7 2.3 5.0 451.4 3.0 6.1 496.1 3.7 7.3 Summerhouse WWTP EQ Pump System Curve 35.0 950 RPM Family of Pump I i Curves Based on I 300 850 RPM - 250 _ € _ Y _ Low Water Level 750 RPM - - _ 200 yr 650 RPM ~ ` ~ �='14u�IOw1y'17uJ'•1 A1. S I .0 .. 1550R -_ =�. _ - ` yE ' ` _ �� pump l i Onc \d81 PumP- - N.,pl Only-HWL I.� �� r __� Pum I + p Onc AdA'I Pump 100 -- - r - -- -- - -�--�^-�� n wL - SP-1776 - 350 RPM 450 RPM "y SP-1776 -450 RPM 50 SP-1776- 5511 RPM 350 RPM L High Water Level -SP-1776-65BRPn+ fern Curve T1.4-134 750 RIM 00 4 T44-B4956RPM - T4A-B4 95R RPN -5.0 - 0.0 100.0 200.0 300-0 400-0 500.0 600.0 Flow per pwnp (gpw) 0 12 Pumps Operating-LWL One Purim "1 Dischar Manifold - 2 rumps TEO TOTAL HEAD TO FLOW VELOCITY F3EAD VELOCITY ft$Ai7 SPLIT II GPM) (Fr -IS) (FT-1 (FT./S) (FT.) (FT-) E 347 0.37 0.02 0.75 0.05 12.1 69A 0.75 0,08 1,39 0-19 12.3 4 104-2. 1.12 0.17 2.24 0.37 12.i I 118.9 1.49 0:28 . ' 98 6-10 12-9 173.46. 1,86 0.43 3.73 0.96 13.4 2093 2.24 0.60 4-48 1.34 13.9 2431 2-61 0.79 5.22 1.78 14,6 27748 2.98 1.01 5.97 2.28 15.3 31 J 3.36 1.26 6.71 2.83 16.1 I 347..2 3.7i 1-SR 7.46 3.44 17.0 - S& S 4.10 1.83 8.20 4,11 17.9 -1fIS7 4.48 2.15 8.95 4.83 19.0 _ Sfax, 4.85 2.49 9.70 5,60 20.1 '40_ 5.22 2.86 10.44 6.42 21.3 2 Primus Oncfatia¢- RWL """. Pump I D6ch Manifold - 2 tampsr�� nijj��c FLpW� VELOCITY EAD VELOCITY H1 AD TOTAL HEAD TO [GPTd� (FT./S) (FT.) (FT./S) (FT.) (FT.) 34.7 0,37 0.02 0.75 0.05 1 9 69.4 0.75 0.08 1.49 0,18 -1.7 104,2 IJ2 0,17 2.24 0.37 -1.5 13 9 l.49 0.29 '2'9R %63 -I.I ISii .(i 1.86 0,43 3.73 0.96 46 2083 2.24 0.60 4-48 1.34 -0.1 143.1 ' 2.61 0.79 5.22 1.78 0.6 277.8 2.98 3.01 5.97 2.28 1.3 312.S 3.36 1.26 6.71 2.83 2.1 3+7.2 373 L53 3,44 3.0 381.9 4.10 1.83 8.20 4,11 3.9 416.7 4-48 2.15 8.95 4.83 5.0 451.4 4.85 2.49 9.70 5.60 6.1 I 486.1 5.22 2.86 10.44 6.42 7.3 Project: Summerhouse WWTP Improvements By: DKP Date: 10/5/2023 CK By: Date: Feed Forward Pumps (from MBR Tanks to Treatment Tanks) - Tank 2 Pump Stop Elev. 33.751 Pump Start Elev. 33.71 Discharge Elev. +(,.{ifi STATIC HEAD 2.25 Treatment Train Flows GPD GPM ADF 100000 69A PDF (Q) 250000 173.6 Feed Forward (5Q) 1250000 868.1 PAS (4Q) 1000000 694.4 Permeate (Q) 250000 173.6 Pump Pipe Dia. Pipe Dia. Discription (i n) 0n) 6 EQUIV_ 4 EQUIV. QUANTITY LENGTH QUANTITY LENGTH 90 Elbow f 76.50 0 0.00 45 Elbow 1 7.10 0 0.00 STD Tee (div) 2 62.00 0 0.00 Check valve 1 1 39.00 0 0.00 Coupling 0 0.00 0 0.00 Gate Valve j 3 9.60 0 0.00 STD Tee (->) 0 0.00 0 0.00 Red 1/4 0 0.00 0 0.00 Red 1/2 _' 12.00 2 7.50 Red 3/4 0 0.00 0 0.00 Sud. Enl. j. =2 i 26.00 f 0 0.00 Total 232.20 7.50 Length Of Run 85 it 4 Ift TOTAL EQUIVALENT LENGTH 317 12 Hazen -Williams Coeff. "C" Pipe, Type ,Class Pipe inside diameter FLOW (GPM) 100 500 750 869.1 1000 1150 SYSTEM CURVE Flow (gpm) 100 250 500 750 868.1 1000 1150 I DIPI System Losses - 6" VELOCITY (FT./S) 1.05 2.63 5.27 7.90 9.14 10.53 12.11 120 250 6.22 HEAD (FT.) 0.32 1.77 6.37 13.50 17.69 22.98 29.76 System Head Pump Head (ft) (ft) 2.66 4.47 10.26 19.21 24.48 31.13 39.65 f DIP I in System Losses - 4" VELOCITY (FT./S) 2.35 5.89 11.77 17.66 20.44 23.55 27.08 120 250 4.16 HEAD (FT.) 0.08 0.45 1.64 3.46 4.54 5.90 7.64 in .,tiiilllll1111 \\A G A f? :R SEAL ' 1 ' a.;:..9 29430�V -1� E �'I/rrr111i►���� t�;9liS TOTAL HEAD (FT.) 2.66 4.47 10.26 19.21 24.48 31.13 39.65 1 Project: Summerhouse WWTP Improvements By: DKP Date: 10/5/2023 CK By: Date: Feed Forward Pumps (from MBR Tanks to Treatment Tanks) - Tank 2 Pump System Curve Manufacture Model Size 45.00 40.00 Design Point 35.00 I J 30.00 Pump efficiency 2500 — SyAcm Head (ft) 9 a v 20.00 { - Pump Head (ft) 60 /o Motor HP at duty point 15.00 8.94 10.00 - f 5.00 — — - 0.00 100 250 500 750 868.1 1000 Flow (gpm) 1, Project: Summcrhouse WWTP Improvements By: DKP Date: 10/5/2023 CK By: Date: Feed Forward Pumps (from MBR Tanks to Treatment Tanks) - Tank 3 r» Pump Stop Elev. 33.75 Pump Start Elev. I 3375 Discharge Elev. 36.00 STATIC HEAD 2.25 Treatment Train Flows GPD GPM ADF 100000 69.4 PDF (Q) 250000 173.6 Feed Forward (5Q) 1250000 868.1 PAS (4Q) 1000000 694.4 Permeate (Q) 250000 173.6 Pump Pipe Dia. Pipe Dia. Discription (in) (in) 6 EQUIv. 4 EQUIV. QUANTITY LENGTH QUANTITY LENGTH 90 Elbow 11 168.30 0 0.00 45 Elbow 1 7.10 0 I 0.00 STD Tee (div) 2 62.00 0 l 0.00 Check valve 1 39.00 0 + 0.00 Coupling j 0 0.00 0 0.00 Gate Valve 3 9.60 1) 0.00 STD Tee (->) 0 0.00 0.00 Red 1 /4 0 0.00 i i 0.00 Red 1/2 2 12.00 _ 7.50 Red 3/4 U 0.00 b 0.00 Sud. Enl. 2 26.00 0 0.00 Total 324.00 7.50 Length Of Run 70 ft 4 ] ft TOTAL EQUIVALENT LENGTH 631 12 Hazen -Williams Coeff. "C" Pipe, Type ,Class Pipe inside diameter FLOW (GPM) i00 250 500. 750 868.1 1000 IISA SYSTEM CURVE Flow (pm) ]00 250 500 750 868.1 1000 1150 1 120. DIPS 250 6.22 System Losses - 6" VELOCITY HEAD (FT./S) (FT.) 1.05 0.65 2.63 3.52 5.27 12.68 7.90 26.85 9.14 35.19 10.53 45.71 12.11 59.20 System Head Pump Head (ft) (ft) 2.98 6.22 16.57 32.56 41.98 53.86 69.09 1 � DIP I in :System Losses - 4" VELOCITY (FT./S) 2.35 5.89 11.77 17.66 20.44 23.55 27.08 120 2a0 4.16 HEAD (FT.) 0.08 0.45 1.64 3.46 4.54 5.90 7.64 in ,�`�11111!l111/ �•`'�'t� CAR OC10 oC' .'FrSSlp'' ' Q-� �9;r y SEAL 29430�. GIN '!I � �C►�r Ki yp�ieL�i 1 9 1 t� TOTAL HEAD (FT.) 2.98 6.22 16.57 32.56 41.98 53.86 69.09 1 Project: Summerhouse WWTP improvements By: DKP Date: 10/5/2023 CK By: Date: Feed Forward Pumps (from MBR Tanks to Treatment Tanks) - Tank 3 Pump System Curve Manufacture Model Size 80.00 70.00 Design Point 60.00 50.00 Pump efficiency 40.00 • I —system Head (a) 60% 1S - Pump Head (fl) 30.00 Motor HP at duty point 15.34 zo.00 I _ 10.00 0.00 ._ . 100 250 500 750 868.1 1000 Flow (gpm) Project: Summerhouse WWTP Improvements By: DKP Date: 10/6/2023 CK By: Date: Permeate Pumps (from MBR Tanks to UV) Pump Stop Elev. }, 5 Pump Start Elev. j Discharge Elev. STATIC HEAD Treatment Train Flows GPD GPM ADF 100000 69.4 PDF (Q) 250000 173.6 Feed Forward (5Q) 1250000 868.1 RAS (4Q) 1000000 694.4 Permeate (Q) 250000 173.6 Permeate pipe with 1 pump discharge Pump Pipe Dia. Pipe Dia. Discription (in) (in) 6 I EQUIV. 3 EQUIV. QUANTITY LENGTH QUANTITY LENGTH 90 Elbow 0.00 I ? 15.40 45 Elbow I 0.00 l 3.60 STD Tee (div) I 0.00 ti 124.00 Check valve I 0.00 0.00 Coupling I 0.00 I 0.00 Gate Valve I 0.00 I 3 4.80 STD Tee (->) I 0.00 I 0.00 Red 1/4 0.00 I 0.00 Red 1 /2 I 0.00 0.00 Red 3/4 0.00 I 0.00 Sud. Enl. 0.00 0.00 Total 0.00 147.80 Length Of Run kft 59.75 ,ft TOTAL EQUIVALENT LENGTH 0 198 •��H CAR0 SSjp�!�l•� SEAL 9� 29430 ' - k, Hazen -Williams Coeff. "C" 1 120 1 1 120 Pipe, Type ,Class PVC) 8Q I PVC1 to, .' Pipe inside diameter 5.76 in 3.04 in System Losses - 6" System Losses - 3" TOTAL SEGMENT FLOW (GPM) VELOCITY HEAD VELOCITY HEAD HEAD (FT./S) (FT.) (FT./S) (FT.) (FT.) 30.. 0.37 0.00 1.32 0.71 0.71 0.74 0.00 2.64 2.55 2.55 1.11 0.00 3.96 5.40 5.40 ¢ 1.47 0.00 5.28 9.20 9.20 1.84 0.00 6.61 13.89 13.89 I;t(9'. ` , 2.21 0.00 7.93 19.47 19.47 2J;U' 2.58 0.00 9.25 25.89 25.89 1 Project: Summerhouse WWTP ImproveMCntS By: DKP Date: 10/6/2023 CK By: Date: Permeate Pumps (from MBR Tanks to UV) Permeate pipe with 2 pumps discharge 2 Pump Pipe Dia. Pipe Dia. Discription (in) (in) 6 EQUIV. j _ -3 j EQUIV. QUANTITY LENGTH QUANTITY LENGTH 90 Elbow 2 30.60 0.00 45 Elbow 2 14.20 0.00 STD Tee (div) 0.00 0.00 Check valve 0.00 0.00 Coupling 0.00 0.00 Gate Valve 6.40 0.00 STD Tee (->) 2 20.40 0.00 Red 1/4 0.00 I 0.00 Red 1/2 0.00 0.00 Red 3/4 0.00 0.00 Sud. Ent. 0.00 0.00 Total 71.60 0.00 Length Of Run J 65 J ft I I ft TOTAL EQUIVALENT LENGTH 137 0 Hazen -Williams Coeff. "C" 120 120 Pipe, Type Class PVC1 80 4 PVC1 80 Pipe inside diameter 5.76 in 3.04 in System Losses - 6" Svstem Losses - 3" TOTAL SEGMENT FLOW (GPM) VELOCITY HEAD VELOCITY HEAD HEAD (FT./S) (FT.) (FT./S) (FT.) (FT.) 60 0.74 0.08 2.64 0.00 0.08 170 1.47 0.28 5.28 0.00 0.28 f 180 2.21 0.60 7.93 0.00 0.60 24fi 2.95 1.03 10.57 0.00 1.03 I`I 31in 3.68 1.55 13.21 0.00 1.55 360 4.42 2.17 15.85 0.00 2.17 4-10 5.16 2.89 18.50 0.00 2.89 Permeate pipe with 4 pump discharge 4 Pump Pipe Dia. Pipe Dia. Discription ( ill) (in) f 6 EQUIV. ] 3 EQUIV. QU1 \N 1 1-1-Y LENGTH QUANTITY LENGTH 90 Elbow 0.00 0.00 45 Elbow 1 7.10 0.00 STD Tee (div) 2 62.00 0.00 Check valve 0.00 0.00 Coupling 0.00 0.00 Gate Valve 1 3.20 0.00 STD Tee (->) 0.00 0.00 Red 1 /4 i 0.00 0.00 Red 1 /2 0.00 0.00 Red 3/4 0.00 0.00 Sud. Enl. I 1 13.00 0.00 Total 85.30 0.00 Length Of Run f 150. in !ft TOTAL EQUIVALENT LENGTH 235 0 1 Project: Summerhouse WWTP lmprovemews By: DKP Date: 10/6/2023 CK By: Date: Permeate Pumps (from MBR Tanks to LTV) Hazen -Williams Coeff. "C" 1_ w v?Oz� I L M Pipe, Type ,Class PVCI1 ' _ '' PVC1 80 Pipe inside diameter 5.76 in 3.04 in Permeate Pumps (from MBR Tanks to UV) System Losses - 6" FLOW (GPM) VELOCITY (FT./S) 120 1.47 240 2.95 360 4.42 480 5.89 600 7.37 720 8.84 840 10.31 SYSTEM CURVE Flow per pump System Head ($pm) (ft) 30 -6.83 60 -3.51 90 1.63 120 8.48 150 16.95 180. 1701 210 38.60 Pump Manufacture Model Size Design Point Pump efficiency 60% Motor HP at duty point 2.05 Project: Summerhouse WWTP lmprnVcmcniti By: DKP Date: CK By: Date: System Losses - 3" TOTAL SEGMENT HEAD VELOCITY HEAD HEAD (FT.) (FT./S) (FT.) (FT.) 0.49 5.28 0.00 0.49 1.77 10.57 0.00 1.77 3.74 15.85 0.00 3.74 6.37 21.14 0.00 6.37 9.62 26.42 0.00 9.62 13.48 31.71 0.00 13.48 17.93 36.99 0.00 17.93 Pump Head (ft) System Curve 4500 4000 3500 / 3000 �! _ 2500 2000 f 1500 MOO 500 �r 000 -5.00 -10.00 Flow (gpm) 10/6/2023 -SyM- Hoad (R) - Pump Heed (ft) 1 Project: Summerhouse WWTP Improvements By: DKP Date: 10/6/2023 CK By: Date: RAS Pumps (from MBR Tanks to Treatment Tanks) - Tank 2 Pump Stop Elev. 33,75 Pump Start Elev. I 33.75 Discharge Elev. I 36.00 STATIC HEAD 2.25 Treatment Train Flows GPD GPM ADF 100000 69.4 PDF (Q) 250000 173.6 Feed Forward (3Q) 750000 520.8 RAS (3Q) 750000 520.8 Permeate (Q) 250000 173.6 Pump Pipe Dia. Pipe Dia. Discription (i n) (in) 6 EQUIV. 4 EQUIV. OUAN-fITY LENGTH QUANTITY LENGTH 90 Elbow I 1 15.30 0.00 45 Elbow I 0.00 0.00 STD Tee (div) I 0.00 0.00 Check valve I 0.00 0.00 Coupling I 0.00 0.00 Gate Valve I 2 6.40 0.00 STD Tee (->) I 0.00 0.00 Red 1 /4 I 0.00 0.00 Red 1/2 I 0.00 0.00 Red 3/4 I 0.00 0.00 Sud. Enl. E 2 26.00 0.00 Total 47.70 0.00 Length Of Run I 176 j f I I ft TOTAL EQUIVALENT LENGTH 224 0 Hazen -Williams Coeff. "C" Pipe, Type ,Class Pipe inside diameter FLOW (GPM) 100 200 300 500 525 700 800 SYSTEM CURVE Flow (£pm) 100 200 300 500 700 800 I DIPI System Losses - 6" VELOCITY (FT./S) 1.05 2.11 3.16 5.27 5.53 7.37 8.43 System Head (ft) 2.48 3.08 4.00 6.75 7.17 10.63 12.98 110 250 6.22 HEAD (FT.) 0.23 0.83 1.75 4.50 4.92 8.38 10.73 Pump Head (ft) 4 I DIP: in :System Losses - 4" VELOCITY (FT./S) 2.35 4.71 7.06 11.77 12.36 16.48 18.84 ",, I tIIIIIIIII // Z S �o•,r:Jt 29�430'� "JVG I tAE�� •��C�: IVZE K. PEp�•`• JIIIrr1111���''tir�R �3 120 f 2,50 4.16 in HEAD TOTAL HEAD (FT.) (FT.) 0.00 2.48 0.00 3.08 0.00 4.00 0.00 6.75 0.00 7.17 0.00 10.63 0.00 12.98 1 Project: Summerhouse WWTP Improvements By: DKP Date: 10/6/2023 CK By: Date: RAS Pumps (from MBR Tanks to Treatment Tanks) - Tank 2 � I i System Curve Ji 12.00 ( 10.00 ' 8.00 / r -System Head (ft) m 6.00 / -Pump Head(ft) � x 4.00 2.00 0.00 log 0 100 200 300 400 500 600 700 800 900 Flaw (gpm) 1 Project: Summerhouse WWTP Improvements By: DKP Date: 10/5/2023 CK By: Date: RAS Pumps (from MBR Tanks to Treatment Tanks) - Tank 3 Pump Stop Elev. 26,50 Low water level for tank emptying Pump Start Elev. 26.50 Discharge Elev. 36.00 STATIC HEAD 9.50 9.5 ft on Kubota calcs for tank emptying Treatment Train Flows GPD GPM ,,��1111111►I'�, ADF PDF (Q) 100000 250000 69.4C!°!RO 173.6 ; ~ L Feed Forward 750000 520.8 ._.SSSIo.�I,� O~9 Q ' (3Q) , �'¢ 9[ f RAS (3Q) 750000 520.8 : Permeate (Q) 250000 173.6 = SEAL 29430 Pump Pipe Dia. Pipe Dia. Q' . C�` E4 �i/�f !1'Gll�frG Discription (in) (in) EQUIV. .•'�`�� 1 6 EQUIV_ 4 P��` QUANTITY LENGTH QUANTITY LENGTH 1 ► t f l 111► I� 90 Elbow 1 15.30 0.00 45 Elbow �. 0.00 0.00 STD Tee (div) 0.00 0.00 Check valve 0.00 0.00 Coupling 0.00 0.00 Gate Valve 6.40 0.00 STD Tee (->) 0.00 0.00 Red 1/4 iL 0.00 0.00 Red 1/2 0.00 0.00 Red 3/4 0.00 0.00 Sud. Enl. 2 26.00 0.00 Total 47.70 0.00 Length Of Run 272 I ❑ TOTA 1. EQUIVALENT LENGTH 320 0 Hazen -Williams Coeff. "C" 120 1 120 Pipe, Type ,Class DIPI 250 1 DIPS 250 1 Pipe inside diameter 6.22 in 4.16 in System Losses - 6" System Losses - 4" FLOW (GPM) VELOCITY HEAD VELOCITY HEAD TOTAL HEAD (FT./S) (FT.) (FT./S) (FT.) (FT.) 100 1.05 0.33 2.35 0.00 9.83 200 2.11 1.18 4.71 0.00 10.68 300 3.16 2.50 7.06 0.00 12.00 500 5.27 6.42 11.77 0.00 15.92 525 5.53 7.03 12.36 0.00 16.53 700 7.37 11.97 16.48 0.00 21.47 800 _ _ 8.43 15.33 18.84 0.00 24.83 SYSTEM CURVE Flow System Head Pump Head (epm) (ft) (ft) 100 9.83 200 10.68 300 12.00 500 15.92 525 16.53 700 21.47 800 24.83 Project: Summerhouse WWTP lmprovcmews By: DKP Date: 10/5/2023 CK By: Date: RAS Pumps (from MBR Tanks to Treatment Tanks) - Tank 3 System Curve 30.00 25.00 20.00 15.00 —System Hcad(ft) — Pump Head (ft) 10.00 5.00 0.00 0 100 200 300 400 500 600 700 800 900 Flow (gpm) E