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HomeMy WebLinkAboutWQ0018992_Application (FTSE)_20230512 (8)East Coast Engineering, P.C. E N G IN E E RS- PLAN NERS-CO N SU LTANTS Croft Pointe Subdivision Sewer Design Report April 2023 SEAL 35054 4-11-2023 ............ 5vs-r/AN \`t:0 /011111110\\ Digitallysigned 1\ toy byJohn Christian Russell AL 35054 i Date: 2023.04.14 '09:45:15 -05'00 4918 Main Street Post Office Box 2469 Shallotfe, North Carolina 28459 Tel.: 910-754-8029 * Fax: 910-754-8049 Firm License Number: C-4785 fu1P-1 : 2. IPMP-2 : 2.71 ` Pump-2 Pump-3 NIP-3:3. loop DO J,. lIftmp-4 R- I * * * * * * * * * * * * K Y P I P E * * * Pipe Network Modeling Software * CopyRighted by KYPIPE LLC (www.kypipe.com) * Version: 10.009 10/01/2019 * Serial #: 8-10080653 * Interface: Classic * Licensed for Pipe2000 * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * Date & Time: Tue Apr 11 17:10:10 2023 Master File : c:\users\chris russell\desktop\22-0331-ece_documents\_la projects\23-0404- croft_pointe_sewer.KYP\23-0404-croft_pointe_sewer.P2K ************************************************ S U M M A R Y O F O R I G I N A L D A T A ************************************************ U N I T S S P E C I F I E D FLOWRATE ............ = gallons/minute HEAD (HGL) .......... = feet PRESSURE ............ = psig P I P E L I N E D A T A STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NAMES LENGTH DIAMETER ROUGHNESS MINOR N A M E #1 #2 (ft) (in) COEFF. LOSS COEFF. ------------------------------------------------------------------------------- P-1 J-1 J-2 138.80 2.00 130.0000 0.00 P-2 J-2 J-3 107.08 2.00 130.0000 0.00 P-3 J-3 J-4 203.91 2.00 130.0000 0.00 P-4 J-4 R-1 467.22 2.00 130.0000 0.00 PMP-1 O-Pump-1 J-1 28.00 1.50 140.0000 0.00 PMP-2 O-Pump-2 J-1 69.70 1.50 130.0000 0.00 PMP-3 O-Pump-3 J-3 100.40 1.50 130.0000 0.00 PMP-4 0-Pump-4 J-4 119.20 1.50 130.0000 0.00 P U M P/L 0 S S E L E M E N THERE IS A DEVICE AT NODE HEAD FLOWRATE (ft) (gpm) 104.00 0.00 90.00 10.00 80.00 16.00 70.00 22.00 60.00 30.00 50.00 36.00 40.00 41.00 30.00 44.00 THERE IS A DEVICE AT NODE THERE IS A DEVICE AT NODE THERE IS A DEVICE AT NODE N 0 D E D A T A D A T A Pump-1 DESCRIBED BY THE FOLLOWING DATA: (ID= 1) EFFICIENCY 75.00 (Default) 75.00 (Default) 75.00 (Default) 75.00 (Default) 75.00 (Default) 75.00 (Default) 75.00 (Default) 75.00 (Default) Pump-2...............................> (ID= 1) Pump-3...............................> (ID= 1) Pump-4...............................> (ID= 1) NODE NODE EXTERNAL JUNCTION EXTERNAL NAME TITLE DEMAND ELEVATION GRADE -------------------------------------------------------------- (gpm) (ft) (ft) J-1 0.00 10.00 J-2 0.00 0.00 J-3 0.00 0.00 J-4 0.00 11.00 0-Pump-2 ---- 6.00 8.00 0-Pump-3 ---- 6.00 8.00 0-Pump-4 ---- 3.00 5.00 R-1 ---- 18.00 20.00 O-Pump-1 ---- 4.00 6.00 O U T P U T O P T I O N D A T A OUTPUT SELECTION: ALL RESULTS ARE INCLUDED IN THE TABULATED OUTPUT MAXIMUM AND MINIMUM PRESSURES = 3 MAXIMUM AND MINIMUM VELOCITIES = 5 MAXIMUM AND MINIMUM HEAD LOSS/1000 = 5 S Y S T E M C O N F I G U R A T I O N NUMBER OF PIPES ...................(P) = 8 NUMBER OF END NODES ...............(J) = 4 NUMBER OF PRIMARY LOOPS ...........(L) = 0 NUMBER OF SUPPLY NODES ............(F) = 5 NUMBER OF SUPPLY ZONES ............(Z) = 1 Case: 0 RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.64012E-05 S I M U L A T I O N D E S C R I P T I O N (L A B E L) P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELD. 1000 1000 gpm ft ft ft/s ft/f ft/f ----------------------------------------------------------------------------------------- P-1 J-1 J-2 29.80 3.24 0.00 3.04 23.34 23.34 P-2 J-2 J-3 29.80 2.50 0.00 3.04 23.34 23.34 P-3 J-3 J-4 47.35 11.22 0.00 4.84 55.02 55.02 P-4 J-4 R-1 68.28 50.62 0.00 6.97 108.35 108.35 PMP-1 0-Pump-1 J-1 14.68 0.62 0.00 2.66 22.25 22.25 PMP-2 0-Pump-2 J-1 15.12 1.88 0.00 2.75 26.97 26.97 PMP-3 0-Pump-3 J-3 17.55 3.57 0.00 3.19 35.54 35.54 PMP-4 0-Pump-4 J-4 20.93 5.87 0.00 3.80 49.21 49.21 P U M P/L 0 S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. gpm ft ft ft a Hp $ $ ft ------------------------------------------------------------------------------------------------------- Pump-1 14.68 2.00 84.20 82.2 75.00 0. 0.0 0.0 ** ** 35.2 Pump-2 15.12 2.00 83.46 81.5 75.00 0. 0.0 0.0 ** ** 35.2 Pump-3 17.55 2.00 79.41 77.4 75.00 0. 0.0 0.0 ** ** 35.2 Pump-4 20.93 2.00 73.49 71.5 75.00 0. 0.0 0.0 ** ** 35.2 N 0 D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE gpm ft ft ft psi ------------------------------------------------------------------------------ J-1 0.00 87.58 10.00 77.58 33.62 J-2 0.00 84.34 J-3 0.00 81.84 J-4 0.00 70.62 11.00 59.62 25.84 0-Pump-2 ---- 89.46 6.00 83.46 36.17 O-Pump-3 ---- 85.41 6.00 79.41 34.41 O-Pump-4 ---- 76.49 3.00 73.49 31.85 R-1 ---- 20.00 18.00 2.00 0.87 O-Pump-1 ---- 88.20 4.00 84.20 36.49 Case 0.0000 0.0000 0.0000 0.0000 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES --------------------- psi --------------------- psi 0-Pump-1 36.49 R-1 0.87 0-Pump-2 36.17 J-4 25.84 0-Pump-3 34.41 0-Pump-4 31.85 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (ft/s) (ft/s) --------------------- P-4 6.97 --------------------- PMP-1 2.66 P-3 4.84 PMP-2 2.75 PMP-4 3.80 P-1 3.04 PMP-3 3.19 P-2 3.04 H L+ M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 --------------------- (ft/ft) --------------------- (ft/ft) P-4 108.35 PMP-1 22.25 P-3 55.02 P-1 23.34 PMP-4 49.21 P-2 23.34 PMP-3 35.54 PMP-2 26.97 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (ft/ft) --------------------- (ft/ft) --------------------- P-4 108.35 PMP-1 22.25 P-3 55.02 P-1 23.34 PMP-4 49.21 P-2 23.34 PMP-3 35.54 PMP-2 26.97 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME -------------------------------------------- gpm TITLE Pump-1 14.68 Pump-2 15.12 Pump-3 17.55 Pump-4 20.93 R-1 -68.28 NET SYSTEM INFLOW = 68.28 NET SYSTEM OUTFLOW = -68.28 NET SYSTEM DEMAND = 0.00 ***** HYDRAULIC ANALYSIS COMPLETED ***** K 9 2 a U, 20 30 44 so jO 120 ;6u 200 140 FLOW PER W.VJW