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Report (2) {x, 15= i21/Cri McKinstry Fire Protection -7` �D S 16790 NE Mason Street Suite 100 " EWE') Porland, Oregon 97230 HYDRAULIC CALCULATIONS FOR JUL2 2015 TIGARD PEDIATRICS CITYOFTIGARD 72ND AVENUE & DARTMOUTH AVENUE BUILDING DIVISION TIGARD, OR DRAWING NUMBER: FP-2 DATE: 7-1-2015 -DESIGN DATA- REMOTE AREA NUMBER: ONE REMOTE AREA LOCATION: MEDICAL OFFICE OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: .10 gpm/sq. ft. AREA OF APPLICATION: 1500 sq. ft. COVERAGE PER SPRINKLER: 225 MAX sq. ft. Calculated Standard Coy. QR Sprk.s TYPE OF SPRINKLERS CALCULATED: 5. 6k Q.R. On Flex Heads NUMBER OF SPRINKLERS CALCULATED: 10 *IN-RACK SPRINKLER DEMAND: NA gpm HOSE-STREAM DEMAND: 100 gpm TOTAL WATER REQUIRED (INCLUDING HOSE) : 332.0 gpm FLOW AND PRESSURE (AT NODE BOR, BOR) : 231.9 gpm @ 51.7 psi TYPE OF SYSTEM: Wet PIPE *VOLUME OF DRY OR PREACTION SYSTEM: N/A INSTALLING CONTRACTOR Name: McKinstry Fire Protection Address: 16790 NE Mason Street Portland, OR Phone: 503-331-0234 AUTHORITY HAVING JURISDICTION: City of Tigard, Fire Dept. NOTES: NA Calculations performed by HASS under license # 50091140 , granted by HRS SYSTEMS, INC. (Notes continue after pipe calculations results. ) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 85.5 67.5 2409.0 85.0 332.0 58. 9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 332.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 232.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 18.3 - - - - 34.2 - - - 2 19.7 - - - - 32.3 - - - 3 19.7 K= 4.66 25.7 23.6 4 19.7 K= 4. 66 25.3 23.5 5 19.7 K= 4. 66 25.3 23.5 6 19.7 K= 4 . 66 25.5 23.5 7 19.7 - - - - 27.5 - - - 8 18.3 - - - - 29.1 - - - + 9 18.3 - - - - 29.3 - - - 10 19.7 - - - - 27.1 - - - 11 19.7 K= 4. 66 23.9 22.8 12 19.7 K= 4 . 66 23.3 22.5 13 19.7 K= 4 . 66 23.3 22.5 13A 19.7 K= 4 .66 23.5 22. 6 14 19.7 K= 4.66 24.5 23.1 15 19.7 - - - - 32.0 - - - 16 18.3 - - - - 34.3 - - - 17 18.3 - - - - 34.7 - - - 18 19.7 - - - - 33.6 - - - 19 19.7 - - - - 29.7 - - - 20 19.7 K= 4 . 66 27.4 24.4 21 19.7 - - - - 29.5 - - - 22 18.3 - - - - 30.0 - - - 23 18.3 - - - - 30.6 - - - 24 19.7 - - - - 30.4 - - - 25 19.7 - - - - 34.4 - - - 26 18.3 - - - - 35.3 - - - 27 18.3 - - - - 36.2 - - - 28 19.7 - - - - 35.2 - - - 29 19.7 - - - - 30.8 - - - 30 18.3 - - - - 30. 9 - - - 31 18.3 - - - - 31.0 - - - 32 19.7 - - - - 31.0 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 33 19.7 - - - - 36.0 - - - 34 18.3 - - - - 37.2 - - - TOR 18.3 - - - - 39.5 - - - BOR 1.0 - - - - 51.7 - - - UG -3.0 - - - - 53.4 - - - BF1 3.0 - - - - 51.1 - - - BF2 3.0 - - - - 56.1 - - - SRC -3.0 SOURCE 58. 9 232.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 53.6 1.536 PL 1.33 PF 1.3 1 18.3 0.0 34.2 0.0 9.3 120 FTG ET PE -0. 6 2 19.7 0.0 32.3 0.0 0.126 TL 10.33 PV Pipe: 2 53.6 1.536 PL 52.50 PF 6. 6 2 19.7 0.0 32.3 0.0 9.3 120 FTG ---- PE 0.0 3 19.7 4.7 25.7 23.6 0.126 TL 52.50 PV Pipe: 3 29.9 1.536 PL 8.83 PF 0.4 3 19.7 4.7 25.7 23.6 5.2 120 FTG ---- PE 0.0 4 19.7 4 .7 25.3 23.5 0.043 TL 8.83 PV Pipe: 4 6.5 1.536 PL 9.25 PF 0.0 4 19.7 4.7 25.3 23.5 1.1 120 FTG ---- PE 0.0 5 19.7 4.7 25.3 23.5 0.003 TL 9.25 PV Pipe: 5 -17.0 1.536 PL 10.00 PF 0.2 5 19.7 4.7 25.3 23.5 2.9 120 FTG ---- PE 0.0 6 19.7 4.7 25.5 23.5 0.015 TL 10.00 PV Pipe: 6 -40.5 1.536 PL 27.67 PF 2.1 6 19.7 4.7 25.5 23.5 7.0 120 FTG ---- PE 0.0 7 19.7 0.0 27 .5 0.0 0.075 TL 27.67 PV Pipe: 7 -40.5 1.536 PL 1.33 PF 1.0 7 19.7 0.0 27.5 0.0 7.0 120 FTG 2T PE 0.6 8 18.3 0.0 29.1 0.0 0.075 TL 13.33 PV Pipe: 8 -40.5 2.203 PL 10.67 PF 0.1 8 18.3 0.0 29.1 0.0 3.4 120 FTG ---- PE 0.0 9 18.3 0.0 29.3 0.0 0.013 TL 10.67 PV Pipe: 9 52.3 1.536 PL 1.33 PF 1. 6 9 18.3 0.0 29.3 0.0 9.0 120 FTG 2T PE -0. 6 10 19.7 0.0 27.1 0.0 0.120 TL 13.33 PV Pipe: 10 52.3 1.536 PL 26.33 PF 3.2 10 19.7 0.0 27.1 0.0 9.0 120 FTG ---- PE 0.0 11 19.7 4.7 23. 9 22 .8 0.120 TL 26.33 PV Pipe: 11 29.5 1.536 PL 14 .00 PF 0. 6 11 19.7 4.7 23.9 22.8 5.1 120 FTG --- PE 0.0 12 19.7 4.7 23.3 22.5 0.042 TL 14 .00 PV Pipe: 12 7.0 1.536 PL 10.00 PF 0.0 12 19.7 4.7 23.3 22.5 1.2 120 FTG ---- PE 0.0 13 19.7 4.7 23.3 22.5 0.003 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 -15.5 1.536 PL 9.00 PF 0.2 13 19.7 4.7 23.3 22 .5 2 .7 120 FTG 2E PE 0.0 13A 19.7 4.7 23.5 22 . 6 0.013 TL 15.00 PV Pipe: 14 -38.1 1.536 PL 9.08 PF 1.0 13A 19.7 4.7 23.5 22. 6 6. 6 120 FTG 2E PE 0.0 14 19.7 4 .7 24.5 23.1 0.067 TL 15.08 PV Pipe: 15 -61.2 1.536 PL 46.83 PF 7.5 14 19.7 4.7 24.5 23.1 10. 6 120 FTG ---- PE 0.0 15 19.7 0.0 32.0 0.0 0.161 TL 46.83 PV Pipe: 16 -61.2 1.536 PL 1.33 PF 1 .7 15 19.7 0.0 32.0 0.0 10. 6 120 FTG ET PE 0. 6 16 18.3 0.0 34.3 0.0 0.161 TL 10.33 PV Pipe: 17 -53. 6 2.703 PL 10. 67 PF 0.1 1 18.3 0.0 34.2 0.0 3.0 120 FTG ---- PE 0.0 16 18.3 0.0 34.3 0.0 0.008 TL 10.67 PV Pipe: 18 -114 .8 2.703 PL 12.00 PF 0.4 16 18.3 0.0 34.3 0.0 6.4 120 FTG ---- PE 0.0 17 18.3 0.0 34.7 0.0 0.033 TL 12.00 PV Pipe: 19 33.3 1.536 PL 1.33 PF 0.5 17 18.3 0.0 34.7 0.0 5.8 120 FTG ET PE -0. 6 18 19.7 0.0 33.6 0.0 0.052 TL 10.33 PV Pipe: 20 33.3 1.536 PL 68.83 PF 3. 9 18 19.7 0.0 33. 6 0.0 5.8 120 FTG 2E PE 0.0 19 19.7 0.0 29.7 0.0 0.052 TL 74.83 PV Pipe: 21 -24.4 1.080 PL 5.83 PF 2.3 20 19.7 4.7 27.4 24.4 8.5 120 FTG ET PE 0.0 19 19.7 0.0 29.7 0.0 0.163 TL 13. 90 PV Pipe: 22 8. 9 1.536 PL 43.58 PF 0.2 19 19.7 0.0 29.7 0.0 1.5 120 FTG ---- PE 0.0 21 19.7 0.0 29.5 0.0 0.005 TL 43.58 PV Pipe: 23 8. 9 1 .536 PL 1 .33 PF 0.1 21 19.7 0.0 29.5 0.0 1 .5 120 FTG 2T PE 0. 6 22 18.3 0.0 30.0 0.0 0.005 TL 13.33 PV Pipe: 24 -92.8 2 .203 PL 12.00 PF 0.7 9 18.3 0.0 29.3 0.0 7 .8 120 FTG ---- PE 0.0 22 18.3 0.0 30.0 0.0 0.060 TL 12.00 PV Pipe: 25 -83. 9 2 .203 PL 11.50 PF 0. 6 22 18.3 0.0 30.0 0.0 7.1 120 FTG ---- PE 0.0 23 18.3 0.0 30.6 0.0 0.050 TL 11 .50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) _ Pipe: 26 -25.7 1.536 PL 1 .33 PF 0.4 23 18.3 0.0 30. 6 0.0 4.4 120 FTG 2T PE -0. 6 24 19.7 0.0 30.4 0.0 0.032 TL 13.33 PV Pipe: 27 -25.7 1.536 PL 111.17 PF 4.0 24 19.7 0.0 30.4 0.0 4.4 120 FTG 4E PE 0.0 25 19.7 0.0 34.4 0.0 0.032 TL 123.17 PV Pipe: 28 -25.7 1.536 PL 1.33 PF 0.3 25 19.7 0.0 34 .4 0.0 4.4 120 FTG ET PE 0. 6 26 18.3 0.0 35.3 0.0 0.032 TL 10.33 PV Pipe: 29 -148.1 2.703 PL 11.50 PF 0. 6 17 18.3 0.0 34.7 0.0 8.3 120 FTG ---- PE 0.0 26 18.3 0.0 35.3 0.0 0.053 TL 11.50 PV Pipe: 30 -173.7 2.703 PL 12 .50 PF 0.9 26 18.3 0.0 35.3 0.0 9.7 120 FTG ---- PE 0.0 27 18.3 0.0 36.2 0.0 0.071 TL 12 .50 PV. Pipe: 31 27.1 1.536 PL 1.33 PF 0.4 27 18.3 0.0 36.2 0.0 4.7 120 FTG ET PE -0. 6 28 19.7 0.0 35.2 0.0 0.036 TL 10.33 PV Pipe: 32 27.1 1.536 PL 113.17 PF 4 .5 28 19.7 0.0 35.2 0.0 4.7 120 FTG 4E PE 0.0 29 19.7 0.0 30.8 0.0 0.036 TL 125.17 PV Pipe: 33 27.1 1.536 PL 1 .33 PF 0.5 29 19.7 0.0 30.8 0.0 4.7 120 FTG 2T PE 0.6 30 18.3 0.0 30. 9 0.0 0.036 TL 13.33 PV Pipe: 34 -58.2 2.203 PL 12.50 PF 0.3 23 18.3 0.0 30. 6 0.0 4.9 120 FTG ---- PE 0.0 30 18.3 0.0 30. 9 0.0 0.025 TL 12.50 PV Pipe: 35 -31.1 2.203 PL 11 .25 PF 0.1 30 18.3 0.0 30.9 0.0 2.6 120 FTG ---- PE 0.0 31 18.3 0.0 31.0 0.0 0.008 TL 11 .25 PV Pipe: 36 -31.1 1.536 PL 1.33 PF 0. 6 31 18.3 0.0 31.0 0.0 5.4 120 FTG 2T PE -0. 6 32 19.7 0.0 31.0 0.0 0.046 TL 13.33 PV Pipe: 37 -31.1 1.536 PL 109.17 PF 5.0 32 19.7 0.0 31.0 0.0 5.4 120 FTG ---- PE 0.0 33 19.7 0.0 36.0 0.0 0.046 TL 109.17 PV Pipe: 38 -31.1 1.536 PL 1.33 PF 0. 6 33 19.7 0.0 36.0 0.0 5.4 120 FTG 2T PE 0. 6 34 18.3 0.0 37.2 0.0 0.046 TL 13.33 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -200.8 2.703 PL 11.25 PF 1.0 27 18.3 0.0 36.2 0.0 11 .2 120 FTG ---- PE 0.0 34 18.3 0.0 37.2 0.0 0.092 TL 11.25 PV Pipe: 40 -231. 9 2.703 PL 7.33 PF 2.3 34 18.3 0.0 37 .2 0.0 13.0 120 FTG 2E PE 0.0 TOR 18.3 0.0 39.5 0.0 0.121 TL 19.33 PV Pipe: 41 -231. 9 2.703 PL 17.33 PF 4 . 6 TOR 18.3 0.0 39.5 0.0 13.0 120 FTG CB PE 7 .5 BOR 1.0 0.0 51.7 0.0 0.121 TL 38.33 PV Pipe: 42 -231.9 6.270 PL 4 .00 PF 0.0 BOR 1.0 0.0 51.7 0.0 2.4 140 FTG L PE 1.7 UG -3.0 0.0 53.4 0.0 0.002 TL 18.07 PV Pipe: 43 -231. 9 6.270 PL 120.00 PF 0.3 UG -3.0 0.0 53.4 0.0 2.4 140 FTG 4L PE -2 . 6 BF1 3.0 0.0 51.1 0.0 0.002 TL 176.29 PV Pipe: 44 FIXED PRESSURE LOSS DEVICE BF2 3.0 0.0 56.1 0.0 5.0 psi, 231. 9 gpm BF1 3.0 0.0 51.1 0.0 Pipe: 45 -232.0 6.270 PL 25.00 PF 0.2 BF2 3.0 0.0 56.1 0.0 2.4 140 FTG T2LG PE 2.6 SRC -3.0 SRCE 58.9 (N/A) 0.002 TL 104.75 PV NOTES (HASS) : (1) Calculations were performed by the HASS 8.4 computer program under license no. 50091140 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 (2) The system has been calculated to provide an average imbalance at each node of 0.004 gpm and a maximum imbalance at any node of 0.143 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 13.0 ft/sec at pipe 41 . (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. (5) Available pressure at source node SRC under full flow conditions is 84 .87 psi compared to the minimum required pressure of 20.00 psi. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD (6) PIPE FITTINGS TABLE Pipe Table Name: ROADRUNNER.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVly BfyVly GatVly AlmChk DPV1v NPTee 1.080 2.30 5.76 2.30 5.76 6.91 1.15 11.52 11.52 5.76 6.270 16.46 35.27 10.58 37. 62 11.76 3.53 32.92 32.92 35.27 PAGE: D MATERIAL: DYNAFL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee LngEll ChkV1v BfyVly GatV1v AlmChk DPV1v 1.536 3.00 6.00 2.00 7.00 6.00 1.00 10.00 13.00 2.203 5.00 10.00 3.00 11.00 6.00 1.00 10.00 12.00 2.703 6.00 12.00 4.00 14 .00 7.00 1.00 10.00 12.00 • � C7 WATER SUPPLY ANALYSIS o y Static: 85 . 50 psi Resid: 67 . 50 psi Flow: 2409.0 gpm H 100 . 0 H 1 GEAD r ilable pressure 01 H 85.04 psi @ 332.0 gpm I\v H H I-- 2 Required pressure ill! �' 58.86 psi @ 332.0 gpm > G J 80 . 0 _ A. Source Supply Curve _ A B. System Demand Curve U C. Available at Source ro G H z E x .'... 01 .... P 60 . 0 �''- c _ Cf)R — .... K _ cn E 01 S S K U c R 40 . 0 r n z p k S H i 20 . 0 xcn U) rn H 0 . 0co ro 0 0, 0) cn cu C7 -14 . 7 640 9010 1100 1500 1J00 2100 2100 2100 3(f00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD WATER SUPPLY CURVE 96+ 1 88+ *0\ I \\\ I \\\ 80+ \\\ \\ I \\\ I \\\ 72+ \\\ I \\ 1 * <-67.5 psi @ 2409 gpm Flow Test Point P 64+ R I E I S IX S 56+ U I R I E 1 48+ ( 1 P I S I I 40+ 1 32+ 1 1 24+ 16+ LEGEND 1 I X = Required Water Supply 58.86 psi @ 332.0 gpm 8+ I 0 = Available Water Supply " I 85.04 psi @ 332.0 gpm 0++-+---+----+ + + + + + + 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 7/1/2015 C:\HASS DATA\15086.SDF JOB TITLE: TIGARD Utility Report: Equivalent K-Factor Calculator Node Sprinkler Pres. Dia. Pipe Ftgs. Total H-W Equivalent Name K-Factor (psi) (in) Len. (ft) Len. (ft) coef. K-factor ALL SPRK.S 5.60 18.20 1.049 40.00 T 45.00 120.00 4. 66