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Report (64) f -ff9-0-0ay i 60'00 5 tv 6PC,17 V 0 ! 9 ..,..„ ... Hydraulics Summary Sheet FIRESTOP COMPANY 3203 NE 65TH STREET SPACE 2 Designer: RD GREEN VANCOUVER, WA. 98663 Cala By: RD GREEN 360-718-8604 Date: 9/21/2017 Project Information Hydraulics DURHAM TPS BUILDING REMODEL Information ilt:1 ;r7-1\1:2 ' 16060 SW 85TH AVE. DFC 7 ?Or Demand... TIGARD, OR. 97224 Spr Req'd Pres: 91.24 PSI ROOF PIPING Uri' 1 * k,;;{, : : Spr Recfd Flow: 693.20 GPM Add', 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 N.,..o. -320F -3- 0/ Cr _Et Static/ Supply... AElev: 0.00 Ft IM eift* Constructi PANEL ,Or\\G 1 ' ' #'0* Occupancy: LIGHT ,- Water Flow Test C' 77506 PE -1Static: 102.00 PSI Authority: CITY OF TIGARD 10-2-2017 Residual: 78.00 PSI \ OREGON co Qty Flowing: 1475.00 GPM `'<<• 1 0 ri- li'' EleVation: 0.00 System Information if' /PY 0, Date: Time: Ft Hydraulics Design Criteria By: EXPIRATION DATE:12/31/18 Pump Data System Type: DRY Rated: 0.0 PSI@ 0.0 GPM Density: .10 GPM/SaFt Boost Pres: (NA) PSI Remote Area: 2535 SoFt Discharge Pres: <NA) PSI Sprinkler Coverage: 148MAX SqFt 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: KFR5G 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 N 4 r 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 09-21-2017 PAGE 2 DURHAM TPS BUILDING .10/2535 FOR UPRIGHT HEADS SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW -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 -QUIRED 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 A01 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 A01 T 8 .00 0 . 1084 PF 0 . 87 PT 8 .36 ( 74) 75 57 2 . 157 L 1. 70 C=100 PT 8 . 05 ( 57) Q 15 . 89 F=0 F 0 . 00 FE 0.00 BN7 T 1 .70 0 . 0036 PF 0 . 01 56 7SDQ 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 7.4DQ 15 . 10 2 . 157 L 8 . 70 C=100 PT 8 .35 ( 74) Q 61 . 88 F=EE F 1 . 80 FE 0. 04 BN7 T 10 . 50 0 . 0440 PF 0.46 54 55D4 16 . 66 2 . 157 L 8 .20 C=100 PT 8 . 85 ( 55) Q 78 . 54 F=0 F 0 . 00 FE 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 5313Q 17 . 98 2 . 157 L 5 . 00 C=100 PT 10 .30 ( 53) Q 113 .75 F=T F 12 .30 PB 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 FE 0. 00 BNB T 16. 10 0 . 0059 PF 0 . 09 16 26 2 .157 L 1 .40 C=100 PT 14 . 12 ( 26) 4 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 FE 0 . 00 A01 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 A01 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 Flow Pipe Fittings Equiv Friction Pressure in Size & Length Loss Summary From To 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 . 08 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 NC1 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 33D0 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 32DQ 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 SDQ 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=I00 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=T,GV F 29 .40 PE 0 . 00 UN1 T 37 .40 0 . 0852 PF 3 . 19 PT 91 .24 ( 0) DURHAM IPS BUILDING Sigma Dynamics Corporation 7700 Supply/ Demand Graph 250 0 111111111111111 11111.1111 111111111111 1111M11111111111maummillII.M111111111111111111111111 . 240 111111111111111 11111111111. 11111111.11111 IIIMMENNIII IIIIIIIIIMIIIIII Mar in 23 IIIIIIIIIIIII 1111 220 MR IIIMIIIIIIIIIIIIIIIIIIIIIIIII Pressure 3.14 PSI II 11111111111111111 mu. inimmummilim Flow 163.3LtLii 210 1111111111111 NI 1111 1111111111111111111111111. 11111111111111 2°°111111111111 IIIIIIIIIINIMIIIIMIIIMIIIIIIII IIIIIIIIIMIIIIIIIINIIIIIIIIIIIIII '115°50 111111111111111111111111111.11111111111111 11111111111111111111111111111111111111111 .1111111 11111111111111111 1111 11111111111111111111111111111=1111111111111•1•1111111 170 111111111111111 NM. 111111111111111.1=1111111111111111111111111111 1:0 1101111111111111111111111 IIIIIIIIIIIIIIIIIII 1 0 1 .11111111111111111111111111 IIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIINIIIIIIIMIIIM E 1450 111111111111111111111111 11111 11111111111111111111111111111111111111111111111111111.11111111111111111111 § 130 111111111111111 111111 1111111‘1111111111111111111111111111111111111111111111111111.11111 120 11111111111111111111 1111111111111111 NIIIIIIIIIIIIHIIIIIIIIIIIIIIIIIIIIIIIIIIII 1101041111 1111111111111111111111 IIIIMIIIIIIIIIIIIIIIIIIIMIIIIIIIIIIIMMIIIIIIIIIIIIIIIIIIIIIII miIiim 1 -as 8,....IIIIIIIII1111MmIIIIIIIIIIIIIIIMIIIIIIIIIIIIIIIIIIIINIMIIIIIIIII No imii • ....— , 90 mom iE80 M=MIMIIIIINIIIIIIIIIIIIIIII MIN 7°mow ..1111111111 miioW'J'oIIIIIIIMIIIIIINIIIIIIIIIII 50 illuril7AilrA411111111111.111111.11111111111.111 INN 1.11111110111. 60 1111111111111111111.111111111111111111.111111111111111111111111111Th 0 11111 '"4A11111111.11111111111111111 111111 1111111111111111111111111111111111111111111111111111111111111 4°11 A111111•11111111111111 1111111111111111111111 30 wommommEnim amaisimm. immimmammmmmmmmim 2°Ibill1111111111111 111111111111•111111•111111111111111111111111111111111111 1°C11111111111 111111111111 11111111111111111111 INIIIIIIIIIIIUIIMIRI 200 400 600 800 1000 1200 1400 1600 1800 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