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fig,5){)?-cacc. 4 " ds, Hydraulics Summary Sheet OFC 28 2017 FIRESTOP COMPANY Designer: RD OrlIGARD 3203 NE 65TH STREET SPACE 2 atittiliNrC VANCOUVER, WA. 98663 Calc By: RD 360-718-8604 Date: 9/21/2017 Project Information Hydraulics DURHAM TPS BUILDING REMODEL Information 16060 SW 85TH AVE. Demand... TIGARD, OR. 97224 Spr Req'd Pres: 91.24 PSI ROOF PIPING Spr Req'd Row: 693.20 GPM Add'l Flows: 0.00 GPM Contract No: Hose at Srce: 100.00 GPM Building: ATTIC Total Flow: 793.20 GPM System ID: DURHAM TPS BUILDING Total Pres: 91.24 PSI Ref. Drawing No: 3 OF 3 Static Elev: 0.00 Ft Construction: PANEL Supply... Occupancy: LIGHT Water Flow Test Static: 102.00 PSI Authority: CITY OF TIGARD Residual: 78.00 PSI Qty Flowing: 1475.00 GPM System Information Elevation: 0.00 FtDate: Time: By: Hydraulics Design Criteria System Type: DRY Pump Data Rated: 0.0 PSI@ 0.0 GPM Density: .10 GPM/SqFt Remote Area: 2535 SqFt Boost Pres: (NA) PSI Sprinkler Coverage: 148MAX SqFt Discharge Pres: (NA) PSI Discharge Flow: (NA) GPM Design Standard: NFPA #13 Hazard: LIGHT Combined Figure: 112311 Curve: LIGHT Static: (NA) PSI Residual: (NA) PSI Sprinklers / Nozzles Qty Flowing: (NA) GPM Manufacturer: RELIABLE Model: KFRS6 Available... Size: 1/2" P) 94.38 PSI@ 793.20 GPM K—Factor: 5.6 F) 91.24 PSI@ 956.52 GPM Temp. Rating: 200F . Margin... Pressure: 3.14 PSI Flow: 163.32 GPM Sigma Dynamics Corporation 7700 Summary Sheet SUBMITTAL SERIAL NO:4126HY1 09-21-2017 PAGE 1 DURHAM TPS BUILDING . 10/2535 FOR UPRIGHT HEADS FLOW TEST RESULTS Water Supply STATIC 102 . 00 PSI RESIDUAL 78 . 00 PSI @ 1475 . 00 GPM CITY PRESSURE AVAILABLE AT 793 .2 GPM 94 . 38 PSI SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K-FACTOR PRESSURE --- ---- ---- 31 34 . 11 14 . 82 5. 60 37. 10 32 33 .27 14 . 82 5 . 60 35.30 33 32 . 77 14 . 82 5 . 60 34.24 34 30 . 73 14 . 82 5 . 60 30. 12 35 32 . 57 14 . 82 5 . 60 33 . 82 36 32 . 12 14 . 82 5. 60 32 . 89 37 32 . 95 14 . 82 5. 60 34 . 63 38 32 . 74 14 . 82 5. 60 34 . 19 39 32 . 65 14 . 82 5. 60 33 . 98 40 26.37 14 . 82 5 . 60 22 . 18 41 26.18 14 . 82 5 . 60 21 . 85 42 26. 11 14 . 82 5 . 60 21 . 74 43 22 .48 14 . 82 5 . 60 16. 12 44 21 . 78 14 .82 5. 60 15. 13 45 21 .42 14 . 82 5. 60 14 . 63 46 19 . 70 14 . 82 5. 60 12 .37 47 20 . 31 14 . 82 5. 60 13 . 16 48 20 . 85 14 . 82 5 . 60 13 . 86 49 20 . 64 14 . 82 5. 60 13 .59 50 19 . 60 14 . 82 5. 60 12 .25 51 20 . 97 14 . 82 5 . 60 14 . 03 52 19. 12 14 . 82 5 . 60 11 . 66 53 17 . 98 14 . 82 5 . 60 10.31 54 17.22 14 . 82 5 . 60 9.46 55 16. 66 14 . 82 5 . 60 8 . 86 56 16. 07 14 . 82 5. 60 8 .24 57 15 . 89 14 . 82 5. 60 8 . 05 58 15 . 10 14 . 82 5 . 60 7 .27 SUBMITTAL SERIAL NO:4126HY1 DURHAM TPS BUILDING 09-21-2017 PAGE 2 . 10/2535 FOR UPRIGHT HEADS SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K-FACTOR PRESSURE 59 14 . 82 14 . 82 5 .60 7. 00 TOTAL WATER REQUIRED FOR SYSTEM 693 .20 GPM OUTSIDE HOSE STREAMS AT 0 100. 00 GPM TOTAL WATER REQUIREMENT 793 .20 GPM PRESSURE REQUIRED AT 0 91 .24 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0 . 00 PSI MAXIMUM VELOCITY FROM 1 TO 2 17.47 FPS SUBMITTAL SERIAL NO:4126HY1 09-21-2017 PAGE 3 DURHAM TPS BUILDING . 10/2535 FOR UPRIGHT HEADS Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length Loss Summary From To GPM IN Devices Ft PSI/Ft PSI 75 59 1 . 049 L 3 . 00 C=100 PT 7 . 00 ( 59) Q 14 . 82 F=T,E F 5 . 00 PE 0 .22 AOl T 8 . 00 0. 1047 PF 0 . 84 PT 8 . 06 ( 75) 74 58 1. 049 L 3 . 00 C=100 PT 7.27 ( 58) Q 15 . 10 F=T,E F 5. 00 PE 0 .22 AOl T 8 . 00 0 . 1084 PF, E03 :N ( 74) 75 57 2 .157 L 1 . 70 C=100 PT 8 . 05 ( 57) Q 15 . 89 F=0 F 0 . 00 PE 0 . 00 BN7 T 1 . 70 0 . 0036 PF 0 . 01 56 75DQ 14 . 82 2 . 157 L 11.30 C=100 PT 8 . 06 ( 75) Q 30 . 71 F=0 F 0 . 00 PE 0 . 04 BN7 T 11 .30 0 . 0120 PF 0 . 14 74 56DQ 16. 07 2 . 157 L 4 .30 C=100 PT 8 .24 ( 56) Q 46. 78 F=0 F 0 . 00 PE 0 . 00 BN7 T 4 .30 0 . 0262 PF 0 . 11 55 74DQ 15. 10 2 . 157 L 8 . 70 C=100 PT 8 .35 ( 74) Q 61 . 88 F=EE F 1. 80 PE 0. 04 BN7 T 10 . 50 0 . 0440 PF 0 .46 54 55DQ 16 . 66 2 . 157 L 8 .20 C=100 PT 8 . 85 ( 55) Q 78 .54 F=0 F 0. 00 PE 0 . 04 BN7 T 8 .20 0. 0684 PF 0 . 56 53 54DQ 17.22 2 .157 L 8 .20 C=100 PT 9.45 ( 54) Q 95. 77 F=0 F 0 . 00 PE 0 . 04 BN7 T 8 .20 0. 0988 PF 0. 81 17 53DQ 17. 98 2 . 157 L 5 . 00 C=100 PT 10 . 30 ( 53) Q 113 . 75 F=T F 12 .30 PE 0 . 00 BN7 T 17 .30 0 . 1358 PF 2 .35 PT 12 . 65 ( 17) 26 51 2 . 157 L 12 .40 C=100 PT 14 . 03 ( 51) Q 20 . 97 F=E F 3 . 70 PE 0 . 00 BN8 T 16.10 0 . 0059 PF 0 . 09 _ 16 26 2 . 157 L 1 .40 C=100 PT 14 . 12 ( 26) Q 20 .97 F=T F 12 .30 PE 0 . 61 NR1 T 13 . 70 0 . 0059 PF 0. 08 PT 14 . 81 ( 16) SUBMITTAL SERIAL NO:4126HY1 09-21-2017 PAGE 4 DURHAM TPS BUILDING . 10/2535 FOR UPRIGHT HEADS . Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length Loss Summary From To GPM IN Devices Ft PSI/Ft PSI 17 52 1 . 049 L 2 . 00 C=100 PT 11 . 66 ( 52) Q 19. 12 F=T F 4 . 00 PE 0 . 00 AOl T 6 . 00 0. 1677 PF 1 . 01 16 17DQ 113 . 75 3 .260 L 4 . 70 C=100 PT 12 . 67 ( 17) Q 132 . 87 F=0 F 0 . 00 PE 2 . 04 NC1 T 4 . 70 0 . 0242 PF 0 . 11 15 16DQ 20 . 97 3 .260 L 2 . 00 C=100 PT 14 . 82 ( 16) Q 153 . 85 F=0 F 0 . 00 PE 0 . 87 NC1 T 2 . 00 0. 0318 PF 0 . 06 PT 15 . 75 ( 15) 77 50 1 . 049 L 1 . 70 C=100 PT 12 .25 ( 50) Q 19. 60 F=T F 4 . 00 PE 0 . 17 A01 T 5. 70 0 . 1757 PF 1 . 00 49 77 2 . 157 L 20 . 00 C=100 PT 13 .42 ( 77) Q 19 . 60 F=EE F 1 .80 PE 0 . 04 BN6 T 21 . 80 0 . 0052 PF 0 . 11 48 49DQ 20 . 64 2 . 157 L 11 .40 C=100 PT 13 . 57 ( 49) Q 40 .25 F=0 F 0. 00 PE 0 . 04 BN6 T 11 .40 0 . 0199 PF 0 .23 25 48DQ 20 . 85 2 . 157 L 5 . 70 C=100 PT 13 . 84 ( 48) Q 61 . 09 F=E F 3 . 70 PE 0 . 00 BN6 T 9.40 0 . 0430 PF 0 .40 15 25 2 . 157 L 2 . 00 C=100 PT 14 .24 ( 25) Q 61. 09 F=T F 12 .30 PE 0 . 87 NR1 T 14 .30 0 . 0430 PF 0 . 61 14 15DQ 153 . 85 3 .260 L 1 .30 C=100 PT 15. 72 ( 15) Q 214 . 94 F=0 F 0 . 00 PE 0. 56 NC1 T 1.30 0 . 0590 PF 0 . 08 PT 16.36 ( 14) 14 47 1 . 049 L 4 . 80 C=100 PT 13 . 16 ( 47) Q 20 .31 F=T,E F 5. 00 PE 1 .39 AOl T 9. 80 0 . 1876 PF 1 . 84 13 14DQ 214 . 94 3 .260 L 6.30 C=100 PT 16.39 ( 14) Q 235 .25 F=0 F 0 . 00 PE 2 . 73 NC1 T 6.30 0 . 0697 PF 0 .44 PT 19. 56 ( 13) SUBMITTAL SERIAL NO:4126HY1 09-21-2017 PAGE 5 DURHAM TPS BUILDING . 10/2535 FOR UPRIGHT HEADS Location From To Flow Pipe Fittings Equiv Friction Pressure in Size & Length Loss Summary GPM IN Devices Ft PSI/Ft PSI 76 45 2 . 157 L 13 .30 C=100 PT 14 . 63 ( 45) Q 21 .42 F=0 F 0 . 00 PE 0 . 04 BN5 T 13 .30 0 . 0062 PF 0 . 08 PT 14 . 75 ( 76) 76 46 1 . 049 L 4 . 80 C=100 PT 12 .37 ( 46) Q 19. 70 F=T F 4 . 00 PE 0 . 82 A01 T 8 . 80 0 . 1773 PF 1 . 56 44 76DQ 21 .42 2 . 157 L 14 . 00 C=100 PT 14 . 75 ( 76) Q 41 . 12 F=EE F 1 . 80 PE 0 . 04 BN5 T 15. 80 0 . 0207 PF 0 .33 23 44DQ 21 . 78 2 . 157 L 10. 60 C=100 PT 15. 12 ( 44) Q 62 . 90 F=T F 12 .30 PE 0. 04 BN5 T 22 . 90 0 . 0454 PF 1 . 04 PT 16.20 ( 23) 23 43 2 . 157 L 0 . 80 C=100 PT 16. 12 ( 43) Q 22 .48 F=T F 12 .30 PE 0 . 00 BN5 T 13 . 10 0 . 0068 PF 0 . 09 13 23DQ 62 . 90 2 . 157 L 4 . 60 C=100 PT 16.21 ( 23) Q 85 .38 F=T F 12 .30 PE 1 . 99 NR1 T 16. 90 0 . 0799 PF 1 .35 12 13DQ 235 .25 3 .260 L 7. 80 C=100 PT 19 .55 ( 13) Q 320 . 63 F=2E F 13 .40 PE 3 .38 NC? T 21.20 0. 1236 PF 2 . 62 PT 25 . 55 ( 12) 41 42 2 . 157 L 7. 80 C=100 PT 21. 74 ( 42) Q 26. 11 F=0 F 0 . 00 PE 0 . 04 BN4 T 7. 80 0 . 0089 PF 0 . 07 73 41DQ 26 . 18 2 . 157 L 2 . 90 C=100 PT 21 . 85 ( 41) Q 52 .29 F=T F 12 . 30 PE 0 . 00 BN4 T 15 .20 0. 0322 PF 0 .49 PT 22 .34 ( 73) 73 40 2 . 157 L 6.20 C=100 PT 22 . 18 ( 40) Q 26.37 F=T F 12 .30 PE 0 . 00 BN4 T 18 .50 0 . 0091 PF 0 . 17 22 73DQ 52 .29 2 . 157 L 2 .20 C=100 PT 22 .35 ( 73) Q 78 . 66 F=E F 3 . 70 PE 0 . 00 BN4 T 5 . 90 0 . 0686 PF 0 .40 SUBMITTAL SERIAL NO:4126HY1 09-21-2017 PAGE 6 DURHAM TPS BUILDING . 10/2535 FOR UPRIGHT HEADS . Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length Loss Summary From To GPM IN Devices Ft PSI/Ft PSI 12 22 2 . 157 L 3 . 90 C=100 PT 22 . 75 ( 22) Q 78 . 66 F=T F 12 .30 PE 1 . 69 NR1 T 16.20 0 . 0686 PF 1 . 11 11 12DQ 320 . 63 3 .260 L 9. 00 C=100 PT 25 . 55 ( 12) Q 399 .30 F=T,2E F 33 .50 PE 3 . 90 NC1 T 42 . 50 0. 1854 PF 7. 88 PT 37.33 ( 11) 38 39 2 . 157 L 11 . 80 C=100 PT 33 . 98 ( 39) Q 32 . 65 F=0 F 0 . 00 PE 0. 04 BN3 T 11 .80 0 . 0135 PF 0 . 16 PT 34 . 18 ( 38) 71 34 1 . 049 L 4 . 90 C=100 PT 30 . 12 ( 34) Q 30 . 73 F=T,E F 5 . 00 PE 0 . 00 A01 T 9 . 90 0 .4037 PF 4 . 00 33 71DQ 32 . 57 2 . 157 L 2 . 80 C=100 PT 34 . 12 ( 71) Q 63 .30 F=0 F 0 . 00 PE 0 . 00 BN1 T 2 . 80 0 . 0459 PF 0. 13 32 33DQ 32 . 77 2 . 157 L 10 .20 C=100 PT 34 .25 ( 33) Q 96. 07 F=0 F 0. 00 PE 0 . 04 BN1 T 10 .20 0 . 0993 PF 1 . 01 31 3213Q 33 .27 2 . 157 L 10 .20 C=100 PT 35.30 ( 32) Q 129.34 F=0 F 0 . 00 PE 0 . 04 BN1 T 10 .20 0 . 1722 PF 1. 76 7 31DQ 34 . 11 2 . 157 L 0 . 50 C=100 PT 37 . 10 ( 31) Q 163 .45 F=T F 12 .30 PE 0 . 00 BN1 T 12 . 80 0 .2655 PF 3 .40 8 7 3 .260 L 6 .50 C=100 PT 40.50 ( 7) Q 163 . 45 F=0 F 0 . 00 PE -2 . 82 NC1 T 6. 50 0 . 0355 PF 0 .23 9 8DQ 32 . 12 3 .260 L 4 .20 C=100 PT 37. 91 ( 8) Q 195 .57 F=0 F 0 . 00 PE -1 . 82 NC1 T 4 .20 0 . 0495 PF 0 .21 10 9DQ 98 .34 3 .260 L 2 . 00 C=100 PT 36.30 ( 9) Q 293 . 91 F=0 F 0 . 00 PE -0 . 87 NC1 T 2 . 00 0 . 1052 PF 0 .21 PT 35 .64 ( 10) SUBMITTAL SERIAL NO:4126HY1 09-21-2017 PAGE 7 DURHAM TPS BUILDING . 10/2535 FOR UPRIGHT HEADS . Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length . Loss Summary From To GPM IN Devices Ft PSI/Ft PSI 37 38 2 . 157 L 8 .20 C=100 PT 34 . 19 ( 38) Q 65. 39 F=0 F 0 . 00 PE 0 . 04 BN2 T 8 .20 0 . 0487 PF 0 .40 9 37DQ 32 . 95 2 . 157 L 3 . 80 C=100 PT 34 . 63 ( 37) Q 98 . 34 F=T F 12 .30 PE 0 . 00 BN2 T 16. 10 0. 1037 PF 1. 67 PT 36.30 ( 9) 8 36 1 . 049 L 3 . 50 C=100 PT 32 . 89 ( 36) Q 32 . 12 F=T,E F 5. 00 PE 1 .30 A01 T 8 .50 0 .4379 PF 3 . 72 PT 37. 91 ( 8) 71 35 2 . 157 L 6. 10 C=100 PT 33 . 82 ( 35) Q 32 . 57 F=T,E F 16. 00 PE 0 . 00 BN1 T 22 . 10 0 . 0134 PF 0 .30 PT 34 . 12 ( 71) 11 10 3 .260 L 1 .30 C=100 PT 35 . 64 ( 10) Q 293 . 91 F=T F 20 . 10 PE -0 .56 NC1 T 21 .40 0 . 1052 PF 2 .25 5 11DQ 399.30 4 .260 L 71. 00 C=100 PT 37.33 ( 11) Q 693 .20 F=3E F 23 . 70 PE -0 .48 FM2 T 94 . 70 0 . 1398 PF 13 .24 4 5 4 . 026 L 7. 00 C=100 PT 50 . 09 ( 5) Q 693 .20 F=DPV F 21. 00 PE 3 . 03 FR2 T 28 . 00 0 . 1841 PF 5 . 15 3 4 4 . 026 L 3 . 00 C=120 PT 58.27 ( 4) Q 693 .20 F=BV F 12 . 00 PE 0 .43 FR1 T 15 . 00 0 .1314 PF 1 . 97 2 3 4 . 150 L 230 . 00 C=150 PT 60 . 67 ( 3) Q 693 .20 F=2EE/E F 18 . 60 PE 0 . 00 UN2 T 248 . 60 0 . 0750 PF 18 . 65 1 2 4 . 026 L 6. 00 C=120 PT 79.32 ( 2) Q 693 .20 F=DDC F 0 . 00 PE 0 . 00 FM1 T 6. 00 0 . 1314 PF 0 . 79 4" WILKINS 350DA 7. 93 COMMENT: INCLUDES SUBMITTAL SERIAL NO:4126HY1 09-21-2017 PAGE 8 DURHAM TPS BUILDING . 10/2535 FOR UPRIGHT HEADS . Location Flow Pipe Fittings Equiv Friction Pressure in Size & Length Loss Summary From To GPM IN Devices Ft PSI/Ft PSI 0 1 4 . 150 L 8. 00 C=140 PT 88 . 05 ( 1) Q 693 .20 F 29.40 PE 0 . 00 UN1 T 37 .40 0 . 0852 PF 3 . 19 PT 91 .24 ( 0) . . • DIIRHARA TPS BUILDIN7 G ,.., ... Sigma Dynamics Corp ration 7700 Supply/ Demanci°Graph 250 240 230 220 IIIIIIIIIIIIIII 111 Margin ssure 3.14 PSI 210 Fl ow 163.32 GPM 200 190 180 170 160 150 140 o- 130 I 120 a. 110 100. ------a-..' ,.os omeimi_ !!!!!! 90 Am' .....musemmo Ina 80 11111111111 70 111111111111FA 111.1111MR"."1"1"11ftwm...--"1111111111111111111 lall 60 111111111E111 Mar 011111111 III 50 III e 40 11111... 41 : 30 20 ®1, 10 0 200 400 600 800 1000 1200 1400 1600 1800 N1.2000 Water Flow(GPM) System Demand.. Water Supply.. Sprinkler Demand 91.24 PSI @ 693.20 GPM Static 102.00 PSI Additional Flows 0.00 GPM Residual 78.00 PSI @ 1475.00 GPM Hose at Source 100.00 GPM Elevation 0.00 PSI Total Demand 91.24 PSI @ 793.20 GPM