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F2020-0234 - Calcs
RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 1ST FLOOR 2 HD LIVING ROOM CALC FILE NUMBER: 13526 DATE: MAY 18, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 392.0 sq. ft. COVERAGE PER SPRINKLER: 196.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 20.0 gpm TOTAL WATER REQUIRED (including hose): 25.1 gpm FLOW AND PRESSURE (@ BOR): 20.0 gpm @ 34.7 psi REQUIRED PRESSURE (@ SRC): 50.0 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. oqaNd4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/18/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD PROOF.SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SRC 71.0 20.0 1500.0 AGGREGATE FLOW ANALYSIS: AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 71.0 25.1 50.0 TOTAL FLOW AT SOURCE 25.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 12.0 - - - 2 30.0 - - - - 12.0 - - - 3 30.0 - - - - 12.0 - - - 4 30.0 - - - - 12.0 - - - 5 30.0 - - - - 12.0 - - - 6 15.0 - - - - 18.5 - - - 7 15.0 - - - - 18.5 - - - 7A 15.0 _ _ _ _ 18.4 - _ _ 7B 15.0 _ _ _ _ 18.4 _ _ _ 7C 15.0 _ _ - _ 18.4 _ _ _ 7D 15.0 _ _ _ _ 18.4 _ _ _ 8 15.0 - - - - 17.9 - - - 9 15.0 - - - - 16.6 - - - 10 15.0 -.- - - 18.3 - - - 11 15.0 - - - - 18.3 - - 12 30.0 - - - _ 13 30.0 - - _ _ 8.0 - - - 14 30.0 - - _ _ 8.2 - - - 15 30.0 - - _ _ 8.2 - - - 16 30.0 - - - _ 17 20.0 _ _ _ _ 11.8 18 20.0 - - - - 11.1 - - - 19 20.0 _ _ _ _ 7.8 - - - 20 20.0 K= 3.70 7.3 10.0 21 20.0 K= 3.70 7.4 10.0 22 20.0 _ _ _ _ 11.7 _ _ _ 23 15.0 - - - - 19.6 _ _ _ 24 15.0 - - - - 19.7 - - _ 25 15.0 _ _ _ _ 19.0 _ _ _ 25A 15.0 - - - - 18.8 - - - 25B 15.0 - - - - 18.8 - - - 25C 15.0 - - - - 18.7 - - - 25D 15.0 - - - - 18.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 5/18/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD PROOF.SDF3 JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - 26 - - - 0.0 18.7 _ _ _ _ _ _ - 26.5 _ _ TR 0.0 _ _ _ _ 27.2 - _ _ FS -5.0 _ - _ _ 29.5 - _ _ FS1 -5.0 _ _ _ _ 32.5 - - - BR -8.0 - - - - 34.7 U1 -8.0 HOSE STREAM 35.3 5.0 U2 2.0 _ _ _ - 32.9 U3 -13.0 _ _ _ _ 40.1 U4 -13.0 - _ - - 99.1 - SRC -15.0 SOURCE 50.0 25.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/18/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD PROOF.SDF JOB TITLE: 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 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 12.0 0.0 0.0 150 FTG 2E PE 0.0 2 30.0 0.0 12.0 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 12.0 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 12.0 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 12.0 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 12.0 0.0 0.000 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 12.0 0.0 0.0 150 FTG E2R PE 0.0 5 30.0 0.0 12.0 0.0 0.000 TL 22.58 PV Pipe: 5 0.0 1.101 PL 15.00 PF 0.0 4 30.0 0.0 12.0 0.0 0.0 150 FTG T PE 6.5 6 15.0 0.0 18.5 0.0 0.000 TL 20.00 PV Pipe: 6 0.0 1.101 PL 10.42 PF 0.0 6 15.0 0.0 18.5 0.0 0.0 150 FTG ET PE 0.0 7 15.0 0.0 18.5 0.0 0.000 TL 22.42 PV Pipe: 7 6.1 1.101 PL 5.33 PF 0.1 7 15.0 0.0 18.5 0.0 2.1 150 FTG T PE 0.0 7A 15.0 0.0 18.4 0.0 0.008 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 18.4 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 18.4 0.0 0.000 TL 14.42 PV Pipe: 7B 6.1 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 18.4 0.0 2.1 150 FTG R PE 0.0 7C 15.0 0.0 18.4 0.0 0.008 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 18.4 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 18.4 0.0 0.000 TL 30.17 PV Pipe: 7D 6.1 1.101 PL 46.08 PF 0.4 7C 15.0 0.0 18.4 0.0 2.1 150 FIG T6R PE 0.0 8 15.0 0.0 17.9 0.0 0.008 TL 57.08 PV Pipe: 8 20.0 1.101 PL 8.08 PF 1.4 8 15.0 0.0 17.9 0.0 6.8 150 FTG ET PE 0.0 9 15.0 0.0 16.6 0.0 0.068 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/18/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD PROOF.SDF JOB TITLE: 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: 9 -13.9 1.101 PL 9.33 PF 0.4 8 15.0 0.0 17.9 0.0 4.7 150 FTG 2R PE 0.0 10 15.0 0.0 18.3 0.0 0.035 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 18.3 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 18.3 0.0 0.000 TL 20.75 PV Pipe: 11 20.0 1.101 PL 15.00 PF 1.5 9 15.0 0.0 16.6 0.0 6.8 150 FTG E PE -6.5 12 30.0 0.0 8.6 0.0 0.068 TL 22.00 PV Pipe: 12 11.0 1.101 PL 6.08 PF 0.6 12 30.0 0.0 8.6 0.0 3.7 150 FTG 2ETR PE 0.0 13 30.0 0.0 8.0 0.0 0.023 TL 26.08 PV Pipe: 13 9.0 1.101 PL 12.75 PF 0.4 12 30.0 0.0 8.6 0.0 3.0 150 FIG 2TR PE 0.0 14 30.0 0.0 8.2 0.0 0.016 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 8.2 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 8.2 0.0 0.000 TL 5.50 PV Pipe: 15 9.0 1.101 PL 9.08 PF 0.4 14 30.0 0.0 8.2 0.0 3.0 150 FTG 3T PE 0.0 16 30.0 0.0 7.8 0.0 0.016 TL 24.08 PV Pipe: 16 11.0 1.101 PL 10.00 PF 0.5 13 30.0 0.0 8.0 0.0 3.7 150 FTG 2E PE 4.3 17 20.0 0.0 11.8 0.0 0.023 TL 24.00 PV Pipe: 17 11.0 1.101 PL 18.33 PF 0.7 17 20.0 0.0 11.8 0.0 3.7 150 FTG ETR PE 0.0 18 20.0 6.0 11.1 0.0 0.023 TL 31.33 PV Pipe: 18 20.0 1.101 PL 14.17 PF 3.2 18 20.0 0.0 11.1 0.0 6.8 150 FTG 4ET PE 0.0 19 20.0 0.0 7.8 0.0 0.068 TL 47.17 PV Pipe: 19 10.0 1.101 PL 9.83 PF 0.5 19 20.0 0.0 7.8 0.0 3.4 150 FTG 2ET PE 0.0 20 20.0 3.7 7.3 10.0 0.019 TL 28.83 PV Pipe: 20 10.0 1.101 PL 7.08 PF 0.5 19 20.0 0.0 7.8 0.0 3.4 150 FTG 2ET PE 0.0 21 20.0 3.7 7.4 10.0 0.019 TL 26.08 PV Pipe: 21 -9.0 1.101 PL 14.17 PF 0.6 18 20.0 0.0 11.1 0.0 3.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 11.7 0.0 0.016 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/1e/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FIR - 2HD PROOF.SDF JOB TITLE: 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: 22 -9.0 1.101 PL 10.00 PF 0.5 22 20.0 0.0 11.7 0.0 3.0 150 FTG 3E PE -4.3 16 30.0 0.0 7.8 0.0 0.016 TL 31.00 PV Pipe: 23 -13.9 1.101 PL 27.08 PF 1.3 10 15.0 0.0 18.3 0.0 4.7 150 FTG E2R PE 0.0 23 15.0 0.0 19.6 0.0 0.035 TL 36.08 PV Pipe: 24 -20.0 1.598 PL 2.25 PF 0.1 23 15.0 0.0 19.6 0.0 3.2 150 FTG T PE 0.0 24 15.0 0.0 19.7 0.0 0.011 TL 10.25 PV Pipe: 25 6.1 1.101 PL 61.17 PF 0.6 23 15.0 0.0 19.6 0.0 2.1 150 FTG ETSR PE 0.0 25 15.0 0.0 19.0 0.0 0.008 TL 78.17 PV Pipe: 26 6.1 1.101 PL 16.00 PF 0.2 25 15.0 0.0 19.0 0.0 2.1 150 FTG ETR PE 0.0 25A 15.0 0.0 18.8 0.0 0.008 TL 29.00 PV Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 18.8 0.0 0.0 150 FTG ET PE 0.0 25B 15.0 0.0 18.8 0.0 0.000 TL 17.50 PV Pipe: 26B 6.1 1.101 PL 7.58 PF 0.1 25A 15.0 0.0 18.8 0.0 2.1 150 FTG T2R PE 0.0 25C 15.0 0.0 18.7 0.0 0.008 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 18.7 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 18.7 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 18.7 0.0 0.0 150 FTG 2E2R PE 0.0 25E 15.0 0.0 18.7 0.0 0.000 TL 24.42 PV Pipe: 26F 6.1 1.101 PL 15.33 PF 0.2 25C 15.0 0.0 18.7 0.0 2.1 150 FTG 2T2R PE 0.0 7 15.0 0.0 18.5 0.0 0.008 TL 27.33 PV Pipe: 27 -20.0 1.598 PL 15.00 PF 0.3 24 15.0 0.0 19.7 0.0 3.2 150 FIG E PE 6.5 26 0.0 0.0 26.5 0.0 0.011 TL 24.00 PV Pipe: 28 -20.0 1.598 PL 25.00 PF 0.7 26 0.0 0.0 26.5 0.0 3.2 150 FTG 4ER PE 0.0 TR 0.0 0.0 27.2 0.0 0.011 TL 62.00 PV Pipe: 100 -20.0 1.598 PL 5.00 PF 0.2 TR 0.0 0.0 27.2 0.0 3.2 150 FTG E PE 2.2 FS -5.0 0.0 29.5 0.0 0.011 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/18/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2RD PROOF.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 32.5 0.0 3.0 psi, 20.0 gpm FS -5.0 0.0 29.5 0.0 Pipe: 102 -20.0 1.101 PL 3.00 PF 0.9 FS1 -5.0 0.0 32.5 0.0 6.8 150 FTG 2RC PE 1.3 BR -8.0 0.0 34.7 0.0 0.068 TL 13.00 PV Pipe: 103 -20.0 1.055 PL 2.00 PF 0.7 BR -8.0 0.0 34.7 0.0 7.4 150 FTG 2E PE 0.0 Ul -8.0 H.S. 35.3 5.0 0.084 TL 8.00 PV Pipe: 104 -25.0 1.025 PL 10.00 PF 1.9 U1 -8.0 H.S. 35.3 5.0 9.7 150 FIG E PE -4.3 U2 2.0 0.0 32.9 0.0 0.146 TL 13.00 PV Pipe: 105 -25.0 2.003 PL 70.00 PF 0.7 U2 2.0 0.0 32.9 0.0 2.5 150 FTG 5E PE 6.5 U3 -13.0 0.0 40.1 0.0 0.006 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 44.1 0.0 4.0 psi, 25.0 gpm U3 -13.0 0.0 40.1 0.0 Pipe: 107 -25.1 0.995 PL 10.00 PF 5.1 U4 -13.0 0.0 44.1 0.0 10.3 150 FTG TX PE 0.9 SRC -15.0 SRCE 50.0 (N/A) 0.169 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 computer program in accordance with NFPA13 (2016) under license no. 38061304 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 0.005 gpm and a maximum imbalance at any node of 0.197 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 10.3 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/18/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD PROOF.SDF JOB TITLE: 70.96 psi with a flow of 32.32 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 5/18/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR — 2HD PROOF.SDF JOB TITLE: E a D' Ln 0 O H '-I S O .A Ga .a N a O 0 0 N .d to W UI a N w a H O ul O N z r � U a .J a 4J ro a o N w V' a w E+ .c 0 0 w 0 0 0 0 0 0 o r 0 o c o d 0 0 0 0 r �o in sr M N .•� o .I 04DOW wawwwpaw aro•+ E] ° U 4 0 O N tl Ul !-4 4 0 i N 10 w ro a C to O W 4J E U 0 7 0 ro D v 4 D W N ro N U1 41 7 4 ro N in U1 D G1 0 41 rd ri C a ° ro v 4 GI l� co x ro N A 4J 4 ro CO U ro w C 4 •ri C N w N N GI C 4 •� a a w ro +J m •) x w W ro C a o H N UI 0 O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 5/18/2020EACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD PROOF.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I \ I 66+ \ I I \ I \ 60+ \ I \\ I \ 54+ \ I \ x \ P 48+ \ R I \ E I \\ S I \ S 42+ \ U I \ R I \ E I \ 36+ \ ( I \ P I \\ S I \ 1 30+ \ I \ I \ I \ 24+ \ I \ I \ * <-20.0 18+ Psi @ 1500 gpm Flow Test Point I I 12+ LEGEND I I X = Required Water Supply ^ I 50.05 psi @ 25.1 gpm 6+ „ I 0 = Available Water Supply TT I 70.97 psi @ 25.1 gpm 11 ItT 0++-+---+----+-----+------+--------+------- 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 1ST FLOOR 2 HD GARAGE CALL FILE NUMBER: 13526 DATE: MAY 18, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 512.0 sq. ft. COVERAGE PER SPRINKLER: 256.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 26.4 gpm TOTAL WATER REQUIRED (including hose): 31.4 gpm FLOW AND PRESSURE (@ BOB): 26.4 gpm @ 28.5 psi REQUIRED PRESSURE (@ SRC): 48.3 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. 0°I t8wz+t4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD GARAGE.SDF JOB TITLE: i4h,VY0l W-1049woON0.1 SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 71.0 20.0 1500.0 71.0 31.4 48.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 31.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 1.7 - - - 2 30.0 - - -- 1.7 - - - 3 30.0 - - - - 1.7 - - - 4 30.0 - - - - 1.7 - - - 5 30.0 - - - - 1.7 - - - 6 15.0 - - - - 8.2 - - - 7 15.0 - - - - 8.2 - - - 7A 15.0 - - - - 8.0 - - - 7B 15.0 K= 4.90 7.5 13.4 7C 15.0 - - - - 8.0 - - - 7D 15.0 K= 4.90 7.0 13.0 8 15.0 - - - - 10.2 - - - 9 15.0 - - - - 10.2 - - - 10 15.0 - - - - 10.6 - - - 11 15.0 - - - - 10.6 - - - 12 30.0 - - - - 3.7 - - - 13 30.0 - - - - 3.7 - - - 14 30.0 - - - - 3.7 - - - 15 30.0 - - - - 3.7 - - - 16 30.0 - - - - 3.7 - - - 17 20.0 - - - - 8.0 - - - 16 20.0 - - - - 8.0 - - - 19 20.0 - - - - 8.0 - - - 20 20.0 - - - - 8.0 - - - 21 20.0 - - - - 8.0 - - - 22 20.0 - - - - 8.0 - - - 23 15.0 - - - - 12.0 - - - 24 15.0 - - - - 12.2 - - - 25 15.0 - - - - 10.0 - - - 25A 15.0 - - - - 9.3 - - - 25B 15.0 - - - - 9.3 - - - 25C 15.0 - - - - 8.9 - - - 25D 15.0 - - - - 8.9 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FIR - 2HD GARAGE.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - 8.9 - - - 26 0.0 - - - - 19.1 - - - TR 0.0 - - - - 20.3 - - - FS -5.0 - - - - 22.7 - - - FS1 -5.0 - - - - 25.7 - - - BR -8.0 - - - - 28.5 - - - U1 -8.0 HOSE STREAM 29.6 5.0 U2 2.0 - - - - 28.2 - - - U3 -13.0 - - - - 35.7 - - - U4 -13.0 - - - - 39.7 - - - SRC -15.0 SOURCE 48.3 31.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD GARAGE.SDF JOB TITLE: 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 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 1.7 0.0 0.0 150 FIG 2E PE 0.0 2 30.0 0.0 1.7 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 1.7 0.0 0.0 150 FIG ET PE 0.0 3 30.0 0.0 1.7 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 1.7 0.0 0.0 150 FIG ET2R PE 0.0 4 30.0 0.0 1.7 0.0 0.000 TL 39.67 FV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 1.7 0.0 0.0 150 FIG E2R PE 0.0 5 30.0 0.0 1.7 0.0 0.000 TL 22.58 FV Pipe: 5 0.0 1.101 PL 15.00 PF 0.0 4 30.0 0.0 1.7 0.0 0.0 150 FTG T PE 6.5 6 15.0 0.0 8.2 0.0 0.000 TL 20.00 PV Pipe: 6 0.0 1.101 PL 10.42 PF 0.0 6 15.0 0.0 8.2 0.0 0.0 150 FIG ET PE 0.0 7 15.0 0.0 8.2 0.0 0.000 TL 22.42 PV Pipe: 7 11.7 1.101 PL 5.33 PF 0.3 7 15.0 0.0 8.2 0.0 3.9 150 FIG T PE 0.0 7A 15.0 0.0 8.0 0.0 0.025 TL 10.33 PV Pipe: 7A 13.4 1.101 PL 2.42 PF 0.5 7A 15.0 0.0 8.0 0.0 4.5 150 FIG ET PE 0.0 7B 15.0 4.9 7.5 13.4 0.032 TL 14.42 PV Pipe: 7B -1.7 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 8.0 0.0 0.6 150 FIG R PE 0.0 7C 15.0 0.0 8.0 0.0 0.001 TL 1.50 PV Pipe: 7C 13.0 1.101 PL 11.17 PF 0.9 7C 15.0 0.0 8.0 0.0 4.4 150 FTG 2ET PE 0.0 7D 15.0 4.9 7.0 13.0 0.031 TL 30.17 PV Pipe: 7D -14.7 1.101 PL 46.08 PF 2.2 7C 15.0 0.0 8.0 0.0 5.0 150 FIG T6R PE 0.0 8 15.0 0.0 10.2 0.0 0.039 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 10.2 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 10.2 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FIR - 2HD GARAGE.SDF JOB TITLE: 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: 9 -14.7 1.101 PL 9.33 PF 0.4 8 15.0 0.0 10.2 0.0 5.0 150 FTG 2R PE 0.0 10 15.0 0.0 10.6 0.0 0.039 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 10.6 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 10.6 0.0 0.000 TL 20.75 PV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 10.2 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 3.7 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 3.7 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 3.7 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 3.7 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 3.7 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 3.7 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 3.7 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 3.7 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 3.7 0.0 0.000 TL 24.08 Pv Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 3.7 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 8.0 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 8.0 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 8.0 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 8.0 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 8.0 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 9.83 PF 0.0 19 20.0 0.0 8.0 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 8.0 0.0 0.000 TL 28.83 PV Pipe: 20 0.0 1.101 PL 7.08 PF 0.0 19 20.0 0.0 8.0 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 8.0 0.0 0.000 TL 26.08 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 8.0 0.0 0.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 8.0 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD GARAGE.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 8.0 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 3.7 0.0 0.000 TL 31.00 PV Pipe: 23 -14.7 1.101 PL 27.08 PF 1.4 10 15.0 0.0 10.6 0.0 5.0 150 FTG E2R PE 0.0 23 15.0 0.0 12.0 0.0 0.039 TL 36.08 PV Pipe: 24 -26.4 1.598 PL 2.25 PF 0.2 23 15.0 0.0 12.0 0.0 4.2 150 FTG T PE 0.0 24 15.0 0.0 12.2 0.0 0.019 TL 10.25 PV Pipe: 25 11.7 1.101 PL 61.17 PF 2.0 23 15.0 0.0 12.0 0.0 3.9 150 FTG ETSR PE 0.0 25 15.0 0.0 10.0 0.0 0.025 TL 78.17 PV Pipe: 26 11.7 1.101 PL 16.00 PF 0.7 25 15.0 0.0 10.0 0.0 3.9 150 FTG ETR PE 0.0 25A 15.0 0.0 9.3 0.0 0.025 TL 29.00 PV Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 9.3 0.0 0.0 150 FTG ET PE 0.0 25B 15.0 0.0 9.3 0.0 0.000 TL 17.50 PV Pipe: 26B 11.7 1.101 PL 7.58 PF 0.4 25A 15.0 0.0 9.3 0.0 3.9 150 FIG T2R PE 0.0 25C 15.0 0.0 8.9 0.0 0.025 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 8.9 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 8.9 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 8.9 0.0 0.0 150 FTG 2E2R PE 0.0 25E 15.0 0.0 8.9 0.0 0.000 TL 24.42 PV Pipe: 26F 11.7 1.101 PL 15.33 PF 0.7 25C 15.0 0.0 8.9 0.0 3.9 150 FTG 2T2R PE 0.0 7 15.0 0.0 8.2 0.0 0.025 TL 27.33 PV Pipe: 27 -26.4 1.598 PL 15.00 PF 0.4 24 15.0 0.0 12.2 0.0 4.2 150 FTG E PE 6.5 26 0.0 0.0 19.1 0.0 0.019 TL 24.00 PV Pipe: 28 -26.4 1.598 PL 25.00 PF 1.1 26 0.0 0.0 19.1 0.0 4.2 150 FTG 4ER PE 0.0 TR 0.0 0.0 20.3 0.0 0.019 TL 62.00 PV Pipe: 100 -26.4 1.598 PL 5.00 PF 0.3 TR 0.0 0.0 20.3 0.0 4.2 150 FTG E PE 2.2 FS -5.0 0.0 22.7 0.0 0.019 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD GARAGE.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 25.7 0.0 3.0 psi, 26.4 gpm FS -5.0 0.0 22.7 0.0 Pipe: 102 -26.4 1.101 PL 3.00 PF 1.5 FS1 -5.0 0.0 25.7 0.0 8.9 150 FTG 2RC PE 1.3 BR -8.0 0.0 28.5 0.0 0.114 TL 13.00 PV Pipe: 103 -26.4 1.055 PL 2.00 PF 1.1 BR -8.0 0.0 28.5 0.0 9.7 150 FTG 2E PE 0.0 U1 -8.0 H.S. 29.6 5.0 0.140 TL 8.00 PV Pipe: 104 -31.4 1.025 PL 10.00 PF 2.9 U1 -8.0 H.S. 29.6 5.0 12.2 150 FTG E PE -4.3 U2 2.0 0.0 28.2 0.0 0.222 TL 13.00 PV Pipe: 105 -31.4 2.003 PL 70.00 PF 1.1 U2 2.0 0.0 28.2 0.0 3.2 150 FTG 5E PE 6.5 U3 -13.0 0.0 35.7 0.0 0.009 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 39.7 0.0 4.0 psi, 31.4 gpm U3 -13.0 0.0 35.7 0.0 Pipe: 107 -31.4 0.995 PL 10.00 PF 7.7 U4 -13.0 0.0 39.7 0.0 13.0 150 FTG TX PE 0.9 SRC -15.0 SRCE 48.3 (N/A) 0.257 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 computer program in accordance with NFPA13 (2016) under license no. 38061304 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 0.002 gpm and a maximum imbalance at any node of 0.062 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 13.0 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FIR - 2HD GARAGE.SDF JOB TITLE: 70.93 psi with a flow of 41.70 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC EWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD GARAGE.SDF JOB TITLE: O '-I [y N a O 0 0 N b In al w a in N wa H O m o H � r-I Z r �H U a +'4J a a ro D " m to a W H 0 0 m 0 0 0 0 0 0 0 0 0 0 0 0 0 0 o a r w Ln d' nl N rl O 1 0 4 D D W W 9 W w 0 0 9 W a w -H C7 w U N 7 O N w w 1-1 4J r-i0 � 7 N 4j w ro a a 1J O al 4J w H 0 U 7 e a) o w H ro W N ro w w D N 1 -1 � ro a, w O m w O � ro p 0 C O O m ro J w J w x aA w w 41 N ro ro U i w 'O w q fa •'I 7 N N N w w q N a w v +1 w •.a A m w ro q a o r N w y O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 5/18/2020ACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD GARAGE.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I I \ I \ 60+ \ I \ I \ I \ 54+ \ I \ I \ I \ P 48X \ R I \ E I \\ S I \ S 42+ \ U I \ R \ E I \ 36+ \ ( I \ P I \\ S I \ I 30+ \ I \ I I \ 24+ \ I \ I \ I * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 12+ LEGEND " 1 " I X = Required Water Supply " I 48.27 psi @ 31.4 gpm " 6+ I 0 = Available Water Supply I 70.96 psi @ 31.4 gpm 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 1ST FLOOR 1 SO GUEST BATH CALC FILE NUMBER: 13526 DATE: MAY 18, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 225.0 sq. ft. COVERAGE PER SPRINKLER: 225.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 1 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 12.0 gpm TOTAL WATER REQUIRED (including hose): 17.0 gpm FLOW AND PRESSURE (@ BOR): 12.0 gpm @ 25.7 psi REQUIRED PRESSURE (@ SRC): 36.7 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 1HD.SDF JOB TITLE: 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 71.0 20.0 1500.0 71.0 17.0 36.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 17.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 12.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - -- 4.7 - - - 2 30.0 - - - - 4.7 - - - 3 30.0 - - - - 4.7 - - - 4 30.0 - - -- 4.7 - - - 5 30.0 - - -- 4.7 - - - 6 15.0 - - - - 11.2 - - - 7 15.0 - - - - 11.2 - - - 7A 15.0 - - - - 11.3 - - - 7B 15.0 - - - - 11.3 - - - 7C 15.0 - - - - 11.3 - - - 7D 15.0 - - - - 11.3 - - - 8 15.0 - - - - 11.6 - - - 9 15.0 - - - - 11.6 - - - 10 15.0 - - - - 11.7 - - - 11 15.0 - - - - 11.7 - - - 12 30.0 - - - - 5.1 - - - 13 30.0 - - - - 5.1 - - - 14 30.0 - - - - 5.1 - - - 15 30.0 - - - - 5.1 - - - 16 30.0 - - - - 5.1 - - - 17 20.0 - - - - 9.5 - - - 16 20.0 - - - - 9.5 - - - 19 20.0 - - - - 9.5 - - - 20 20.0 - - - - 9.5 - - - 21 20.0 - - - - 9.5 - - - 22 20.0 - - - - 9.5 - - - 23 15.0 - - - - 11.9 - - - 24 15.0 - - - - 12.0 - - - 25 15.0 - - - - 11.2 - - - 25A 15.0 - - - - 11.0 - - - 25B 15.0 K= 3.70 10.5 12.0 25C 15.0 - - - - 11.1 - - - 25D 15.0 - - - - 11.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 1HD.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - 11.1 - - - 26 0.0 - - - - 18.6 - - - TR 0.0 - - - - 18.8 - - - FS -5.0 - - - - 21.1 - - - FS1 -5.0 - - - - 24.1 - - - BR -8.0 - - - - 25.7 - - - U1 -8.0 HOSE STREAM 26.0 5.0 U2 2.0 - - - - 22.6 - - - U3 -13.0 - - - - 29.4 - - - U4 -13.0 - - - - 33.4 - - - SRC -15.0 SOURCE 36.7 17.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 1HD.SDF JOB TITLE: 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 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 4.7 0.0 0.0 150 FTG 2E PE 0.0 2 30.0 0.0 4.7 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 4.7 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 4.7 0.0 0.000 TL 19.08 FV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 4.7 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 4.7 0.0 0.000 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 4.7 0.0 0.0 150 FTG E2R PE 0.0 5 30.0 0.0 4.7 0.0 0.000 TL 22.58 Pv Pipe: 5 0.0 1.101 PL 15.00 PF 0.0 4 30.0 0.0 4.7 0.0 0.0 150 FTG T PE 6.5 6 15.0 0.0 11.2 0.0 0.000 TL 20.00 PV Pipe: 6 0.0 1.101 PL 10.42 PF 0.0 6 15.0 0.0 11.2 0.0 0.0 150 FTG ET PE 0.0 7 15.0 0.0 11.2 0.0 0.000 TL 22.42 PV Pipe: 7 -5.4 1.101 PL 5.33 PF 0.1 7 15.0 0.0 11.2 0.0 1.8 150 FTG T PE 0.0 7A 15.0 0.0 11.3 0.0 0.006 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 11.3 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 11.3 0.0 0.000 TL 14.42 PV Pipe: 7B -5.4 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 11.3 0.0 1.8 150 FTG R PE 0.0 7C 15.0 0.0 11.3 0.0 0.006 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 11.3 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 11.3 0.0 0.000 TL 30.17 PV Pipe: 7D -5.4 1.101 PL 46.08 PF 0.3 7C 15.0 0.0 11.3 0.0 1.8 150 FTG T6R PE 0.0 8 15.0 0.0 11.6 0.0 0.006 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 11.6 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 11.6 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 1RD.SDF JOB TITLE: 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: 9 -5.4 1.101 PL 9.33 PF 0.1 8 15.0 0.0 11.6 0.0 1.8 150 FTG 2R PE 0.0 10 15.0 0.0 11.7 0.0 0.006 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 11.7 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 11.7 0.0 0.000 TL 20.75 PV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 11.6 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 5.1 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 5.1 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 5.1 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 5.1 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 5.1 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 5.1 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 5.1 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 5.1 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 5.1 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 5.1 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 9.5 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 9.5 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 9.5 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 9.5 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 9.5 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 9.83 PF 0.0 19 20.0 0.0 9.5 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 9.5 0.0 0.000 TL 28.83 PV Pipe: 20 0.0 1.101 PL 7.08 PF 0.0 19 20.0 0.0 9.5 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 9.5 0.0 0.000 TL 26.08 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 9.5 0.0 0.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 9.5 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FIR - 1HD.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 9.5 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 5.1 0.0 0.000 TL 31.00 PV Pipe: 23 -5.4 1.101 PL 27.08 PF 0.2 10 15.0 0.0 11.7 0.0 1.8 150 FTG E2R PE 0.0 23 15.0 0.0 11.9 0.0 0.006 TL 36.08 PV Pipe: 24 -12.0 1.598 PL 2.25 PF 0.0 23 15.0 0.0 11.9 0.0 1.9 150 FTG T PE 0.0 24 15.0 0.0 12.0 0.0 0.004 TL 10.25 PV Pipe: 25 6.6 1.101 PL 61.17 PF 0.7 23 15.0 0.0 11.9 0.0 2.2 150 FTG ETSR PE 0.0 25 15.0 0.0 11.2 0.0 0.009 TL 78.17 PV Pipe: 26 6.6 1.101 PL 16.00 PF 0.3 25 15.0 0.0 11.2 0.0 2.2 150 FTG ETR PE 0.0 25A 15.0 0.0 11.0 0.0 0.009 TL 29.00 PV Pipe: 26A 12.0 1.101 PL 5.50 PF 0.5 25A 15.0 0.0 11.0 0.0 4.0 150 FTG ET PE 0.0 25B 15.0 3.7 10.5 12.0 0.026 TL 17.50 PV Pipe: 26B -5.4 1.101 PL 7.58 PF 0.1 25A 15.0 0.0 11.0 0.0 1.8 150 FTG T2R PE 0.0 25C 15.0 0.0 11.1 0.0 0.006 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 11.1 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 11.1 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 11.1 0.0 0.0 150 FIG 2E2R PE 0.0 25E 15.0 0.0 11.1 0.0 0.000 TL 24.42 PV Pipe: 26F -5.4 1.101 PL 15.33 PF 0.2 25C 15.0 0.0 11.1 0.0 1.8 150 FTG 2T2R PE 0.0 7 15.0 0.0 11.2 0.0 0.006 TL 27.33 FV Pipe: 27 -12.0 1.598 PL 15.00 PF 0.1 24 15.0 0.0 12.0 0.0 1.9 150 FTG E PE 6.5 26 0.0 0.0 18.6 0.0 0.004 TL 24.00 PV Pipe: 28 -12.0 1.598 PL 25.00 PF 0.3 26 0.0 0.0 18.6 0.0 1.9 150 FTG 4ER PE 0.0 TR 0.0 0.0 18.8 0.0 0.004 TL 62.00 PV Pipe: 100 -12.0 1.598 PL 5.00 PF 0.1 TR 0.0 0.0 18.8 0.0 1.9 150 FTG E PE 2.2 FS -5.0 0.0 21.1 0.0 0.004 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 1HD.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 24.1 0.0 3.0 psi, 12.0 gpm FS -5.0 0.0 21.1 0.0 Pipe: 102 FS1 -5.0 0.0 24.1 BR -8.0 0.0 25.7 -12.0 1.101 PL 3.00 PF 0.3 0.0 4.0 150 FTG 2RC PE 1.3 0.0 0.026 TL 13.00 PV Pipe: 103 -12.0 1.055 PL 2.00 PF 0.3 BR -8.0 0.0 25.7 0.0 4.4 150 FTG 2E PE 0.0 U1 -8.0 H.S. 26.0 5.0 0.033 TL 8.00 PV Pipe: 104 -17.0 1.025 PL 10.00 PF 0.9 U1 -8.0 H.S. 26.0 5.0 6.6 150 FTG E PE -4.3 U2 2.0 0.0 22.6 0.0 0.071 TL 13.00 PV Pipe: 105 -17.0 2.003 PL 70.00 PF 0.3 U2 2.0 0.0 22.6 0.0 1.7 150 FTG 5E PE 6.5 U3 -13.0 0.0 29.4 0.0 0.003 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 33.4 0.0 4.0 psi, 17.0 gpm U3 -13.0 0.0 29.4 0.0 Pipe: 107 -17.0 0.995 PL 10.00 PF 2.5 U4 -13.0 0.0 33.4 0.0 7.0 150 FTG TX PE 0.9 SRC -15.0 SRCE 36.7 (N/A) 0.082 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 computer program in accordance with NFPA13 (2016) under license no. 38061304 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 0.001 gpm and a maximum imbalance at any node of 0.051 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 7.0 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 1HD.SDF JOB TITLE: 70.97 psi with a flow of 26.81 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HNC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N X Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 1HD.SDF JOB TITLE: 0 0 m 0 0 0 0 0 0 0 0 0 0 0 0 0 0 o c r w in m M N ,-1 o i 04 M)0w as wmmp 9W - -a 9) 1- 0 v U N 7 0 N W N .i .0 C W 4J w ro a a N O to .J 01 H U C E 0 O N H D w y ro w w 7 N mA ro w D N 4J .0 ro 0 C O O m •D N w l� N W A +J N rd U ro •.1 (0 v v a s� •.I 7 N N N N C $4 N •H a a w v +1 w m .0 m N ro a a o H N N 0 O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 1HD.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I I \ I \ 60+ \ I \\ I I \ 54+ \ I \ I \ I \ P 48+ \ R I \ E I \\ S I \ S 42+ \ U I \ R I \ E I \ 36X \ ( I \ P I \\ S I \ I 30+ \ I \ I I \ 24+ \ I \ I \ I * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 12+ LEGEND I I X = Required Water Supply I 36.74 psi @ 17.0 gpm 6+ " I 0 = Available Water Supply " I 70.99 psi @ 17.0 gpm " 0++-+---+----+-----+------+-----r--+------------------------------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 2ND FLOOR 2 HD GYM CALC FILE NUMBER: 13526 DATE: MAY 18, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 324.0 sq. ft. COVERAGE PER SPRINKLER: 196.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 20.0 gpm TOTAL WATER REQUIRED (including hose): 25.1 gpm FLOW AND PRESSURE (@ BOR): 20.0 gpm @ 37.6 psi REQUIRED PRESSURE (@ SRC): 52.7 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY RAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 2HD.SDF JOB TITLE: 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 71.0 20.0 1500.0 71.0 25.1 52.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 25.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 K= 3.70 7.3 10.0 2 30.0 - - - - 7.7 - - - 3 30.0 K= 3.70 7.3 10.0 4 30.0 - - - - 10.4 - - - 5 30.0 - - -- 10.4 - - - 6 15.0 - - - - 18.3 - - - 7 15.0 - - - - 19.8 - -- 7A 15.0 - - - - 20.0 - - - 7B 15.0 - - - - 20.0 - - - 7C 15.0 - - - - 20.1 - - - 7D 15.0 - - - - 20.1 - - - 8 15.0 - - - - 21.3 - - - 9 15.0 - - - - 21.3 - - - 10 15.0 - - - - 21.5 - - - 11 15.0 - - - - 21.5 - - - 12 30.0 - - - - 14.8 - - - 13 30.0 - - - - 14.8 - - - 14 30.0 - - - - 14.8 - - - 15 30.0 - - - - 14.8 - - - 16 30.0 - - - - 14.8 - - - 17 20.0 - - - - 19.1 - - - 18 20.0 - - - - 19.1 - - - 19 20.0 - - - - 19.1 - - - 20 20.0 - - - - 19.1 - - - 21 20.0 - - - - 19.1 - - - 22 20.0 - - - - 19.1 - - - 23 15.0 - - - - 22.3 - - - 24 15.0 - - - - 22.4 - - - 25 15.0 - - - - 21.0 - - - 25A 15.0 - - - - 20.5 - - - 25B 15.0 - - - - 20.5 - - - 25C 15.0 - - - - 20.3 - - - 25D 15.0 - - - - 20.3 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 2HD.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - 20.3 - - - 26 0.0 - - - - 29.2 - - - TR 0.0 - - - - 29.8 - - - FS -5.0 - - - - 32.2 - - - FS1 -5.0 - - - - 35.2 - - - BR -8.0 - - - - 37.4 - - - U1 -8.0 HOSE STREAM 38.0 5.0 U2 2.0 - - - - 35.6 - - - U3 -13.0 - - - - 42.8 - - - U4 -13.0 - - - - 46.8 - - - SRC -15.0 SOURCE 52.7 25.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 2HD.SDF JOB TITLE: 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 -10.0 1.101 PL 6.92 PF 0.4 1 30.0 3.7 7.3 10.0 3.4 150 FTG 2E PE 0.0 2 30.0 0.0 7.7 0.0 0.019 TL 20.92 Pv Pipe: 2 10.0 1.101 PL 7.08 PF 0.4 2 30.0 0.0 7.7 0.0 3.4 150 FIG ET PE 0.0 3 30.0 3.7 7.3 10.0 0.019 TL 19.08 PV Pipe: 3 -20.0 1.101 PL 25.67 PF 2.7 2 30.0 0.0 7.7 0.0 6.7 150 FTG ET2R PE 0.0 4 30.0 0.0 10.4 0.0 0.068 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 10.4 0.0 0.0 150 FTG E2R PE 0.0 5 30.0 0.0 10.4 0.0 0.000 TL 22.58 PV Pipe: 5 -20.0 1.101 PL 15.00 PF 1.4 4 30.0 0.0 10.4 0.0 6.7 150 FTG T PE 6.5 6 15.0 0.0 18.3 0.0 0.068 TL 20.00 PV Pipe: 6 -20.0 1.101 PL 10.42 PF 1.5 6 15.0 0.0 18.3 0.0 6.7 150 FTG ET PE 0.0 7 15.0 0.0 19.8 0.0 0.068 TL 22.42 PV Pipe: 7 -10.7 1.101 PL 5.33 PF 0.2 7 15.0 0.0 19.8 0.0 3.6 150 FTG T PE 0.0 7A 15.0 0.0 20.0 0.0 0.021 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 20.0 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 20.0 0.0 0.000 TL 14.42 PV Pipe: 7B -10.7 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 20.0 0.0 3.6 150 FTG R PE 0.0 7C 15.0 0.0 20.1 0.0 0.021 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 20.1 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 20.1 0.0 0.000 TL 30.17 PV Pipe: 7D -10.7 1.101 PL 46.08 PF 1.2 7C 15.0 0.0 20.1 0.0 3.6 150 FTG TER PE 0.0 8 15.0 0.0 21.3 0.0 0.021 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 21.3 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 21.3 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 2HD.SDF JOB TITLE: 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: 9 -10.7 1.101 PL 9.33 PF 0.2 8 15.0 0.0 21.3 0.0 3.6 150 FTG 2R PE 0.0 10 15.0 0.0 21.5 0.0 0.021 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 21.5 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 21.5 0.0 0.000 TL 20.75 PV Pipe: it 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 21.3 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 14.8 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 14.8 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 14.8 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 14.8 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 14.8 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 14.8 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 14.8 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 14.8 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 14.8 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 14.8 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 19.1 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 19.1 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 19.1 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 19.1 0.0 0.0 150 FIG 4ET PE 0.0 19 20.0 0.0 19.1 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 9.83 PF 0.0 19 20.0 0.0 19.1 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 19.1 0.0 0.000 TL 28.83 PV Pipe: 20 0.0 1.101 PL 7.08 PF 0.0 19 20.0 0.0 19.1 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 19.1 0.0 0.000 TL 26.08 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 19.1 0.0 0.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 19.1 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 2HD.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 19.1 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 14.8 0.0 0.000 TL 31.00 PV Pipe: 23 -10.7 1.101 PL 27.08 PF 0.8 10 15.0 0.0 21.5 0.0 3.6 150 FTG E2R PE 0.0 23 15.0 0.0 22.3 0.0 0.021 TL 36.08 PV Pipe: 24 -20.0 1.598 PL 2.25 PF 0.1 23 15.0 0.0 22.3 0.0 3.2 150 FTG T PE 0.0 24 15.0 0.0 22.4 0.0 0.011 TL 10.25 PV Pipe: 25 9.3 1.101 PL 61.17 PF 1.3 23 15.0 0.0 22.3 0.0 3.1 150 FTG ETSR PE 0.0 25 15.0 0.0 21.0 0.0 0.017 TL 78.17 PV Pipe: 26 9.3 1.101 PL 16.00 PF 0.5 25 15.0 0.0 21.0 0.0 3.1 150 FTG ETR PE 0.0 25A 15.0 0.0 20.5 0.0 0.017 TL 29.00 PV Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 20.5 0.0 0.0 150 FIG ET PE 0.0 25B 15.0 0.0 20.5 0.0 0.000 TL 17.50 PV Pipe: 26B 9.3 1.101 PL 7.58 PF 0.2 25A 15.0 0.0 20.5 0.0 3.1 150 FTG T2R PE 0.0 25C 15.0 0.0 20.3 0.0 0.017 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 20.3 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 20.3 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 20.3 0.0 0.0 150 FTG 2E2R PE 0.0 25E 15.0 0.0 20.3 0.0 0.000 TL 24.42 PV Pipe: 26F 9.3 1.101 PL 15.33 PF 0.5 25C 15.0 0.0 20.3 0.0 3.1 150 FTG 2T2R PE 0.0 7 15.0 0.0 19.8 0.0 0.017 TL 27.33 PV Pipe: 27 -20.0 1.598 PL 15.00 PF 0.3 24 15.0 0.0 22.4 0.0 3.2 150 FTG E PE 6.5 26 0.0 0.0 29.2 0.0 0.011 TL 24.00 PV Pipe: 28 -20.0 1.598 PL 25.00 PF 0.7 26 0.0 0.0 29.2 0.0 3.2 150 FTG 4ER PE 0.0 TR 0.0 0.0 29.8 0.0 0.011 TL 62.00 PV Pipe: 100 -20.0 1.598 PL 5.00 PF 0.2 TR 0.0 0.0 29.8 0.0 3.2 150 FTG E PE 2.2 FS -5.0 0.0 32.2 0.0 0.011 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 2HD.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 35.2 0.0 3.0 psi, 20.0 gpm FS -5.0 0.0 32.2 0.0 Pipe: 102 -20.0 1.101 PL 3.00 PF 0.9 FS1 -5.0 0.0 35.2 0.0 6.7 150 FIG 2RC PE 1.3 BR -8.0 0.0 37.4 0.0 0.068 TL 13.00 PV Pipe: 103 -20.0 1.055 PL 2.00 PF 0.7 BR -8.0 0.0 37.4 0.0 7.3 150 FTG 2E PE 0.0 Ul -8.0 H.S. 38.0 5.0 0.084 TL 8.00 Pv Pipe: 104 -25.0 1.025 PL 10.00 PF 1.9 U1 -8.0 H.S. 38.0 5.0 9.7 150 FTG E PE -4.3 U2 2.0 0.0 35.6 0.0 0.146 TL 13.00 Pv Pipe: 105 -25.0 2.003 PL 70.00 PF 0.7 U2 2.0 0.0 35.6 0.0 2.5 150 FTG 5E PE 6.5 U3 -13.0 0.0 42.8 0.0 0.006 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 46.8 0.0 4.0 psi, 25.0 gpm U3 -13.0 0.0 42.8 0.0 Pipe: 107 -25.1 0.995 PL 10.00 PF 5.1 U4 -13.0 0.0 46.8 0.0 10.3 150 FTG TX PE 0.9 SRC -15.0 SRCE 52.7 (N/A) 0.169 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 computer program in accordance with NFPA13 (2016) under license no. 38061304 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 0.142 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 10.3 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FIR - 2HD.SDF JOB TITLE: 70.96 psi with a flow of 31.85 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALLS\INITIAL\2ND FIR - 2HD.SDF JOB TITLE: 0 0 m 0 0 0 0 0 0 0 o a 0 0 0 0 0 0 0 r t0 Ifs -0 M N rl O 1 0 µ'p U' W as W wwAaW `•'aa-H '7 UI U N 0 O N AJ N .1 4 0 11 7 of 41 v ro a a V o 0 U1 � 4J H U 7 0 v 0 w 4 ro W 0 w ro v v C N rl 1J ro N w 0 0 x ro a 0 O 0 0 m ro ij Vl O w N A 4J N ld ro 0 N ro v C H •.i 7 N co N N U1 G SI a w v w -1 ,C N N ro C A O t N N 0 O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 2HD.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I\ I 66+ \ I I \ I \ 60+ \ I \\ I I \ 54+ \ X \ I I \ P 48+ \ R \ E I \\ S I \ S 42+ \ U I \ R \ E I \ 36+ \ ( I \ P I \\ S \ 1 30+ \ I \ I I \ 24+ \ I \ I \ I * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 12+ LEGEND I" I X = Required Water Supply IT 1 52.73 psi @ 25.1 gpm 6+ I 0 = Available Water Supply " I 70.97 psi @ 25.1 gpm " 0++_+___+____+_--__+______+__----__+________+____-_--_+___________+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 2ND FLOOR 1 HD BATH 1 CALC FILE NUMBER: 13526 DATE: MAY 18, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 225.0 sq. ft. COVERAGE PER SPRINKLER: 225.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 1 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 12.0 gpm TOTAL WATER REQUIRED (including hose): 17.0 gpm FLOW AND PRESSURE (@ BOB): 12.0 gpm @ 33.5 psi REQUIRED PRESSURE (@ SRC): 99.5 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 1HD.SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SRC 71.0 20.0 1500.0 AGGREGATE FLOW ANALYSIS AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 71.0 17.0 44.5 TOTAL FLOW AT SOURCE 17.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 12.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 11.1 - - - 2 30.0 - - - - 11.1 - - - 3 30.0 - - - - 11.1 - - - 4 30.0 - - - - 11.1 - - - 5 30.0 K= 3.70 10.5 12.0 6 15.0 - - - - 18.1 - - - 7 15.0 - - - - 18.7 - - - 7A 15.0 - - - - 18.8 - - - 7B 15.0 - - - - 18.8 - - - 7C 15.0 - - - - 18.8 - - - 7D 15.0 - - - - 18.8 - - - 8 15.0 - - - - 19.3 - - - 9 15.0 - - - - 19.3 - - - 10 15.0 - - - - 19.4 - - - 11 15.0 - - - - 19.4 - - - 12 30.0 - - - - 12.8 - - - 13 30.0 - - - - 12.8 - - - 14 30.0 - - - - 12.8 - - - 15 30.0 - - - - 12.8 - - - 16 30.0 - - - - 12.8 - - - 17 20.0 - - - - 17.1 - - - 18 20.0 - - - - 17.1 - - - 19 20.0 - - - - 17.1 - - - 20 20.0 - - - - 17.1 - - - 21 20.0 - - - - 17.1 - - - 22 20.0 - - - - 17.1 - - - 23 15.0 - - - - 19.7 - - - 24 15.0 - - - - 19.7 - - - 25 15.0 - - - - 19.2 - - - 25A 15.0 - - - - 19.0 - - - 258 15.0 - - - - 19.0 - - - 25C 15.0 - - - - 18.9 - - - 25D 15.0 - - - - 18.9 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 1HD.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - 18.9 - - - 26 0.0 - - - - 26.3 - - - TR 0.0 - - - - 26.6 - - - FS -5.0 - - - - 28.8 - - - FS1 -5.0 - - - - 31.8 - - - BR -8.0 - - - - 33.5 - - - U1 -8.0 HOSE STREAM 33.7 5.0 U2 2.0 - - - - 30.3 - - - U3 -13.0 - - - - 37.2 - - - U4 -13.0 - - - - 41.2 - - - SRC -15.0 SOURCE 44.5 17.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 1HD.SDF JOB TITLE: 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 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 11.1 0.0 0.0 150 FTG 2E PE 0.0 2 30.0 0.0 11.1 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 11.1 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 11.1 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 11.1 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 11.1 0.0 0.000 TL 39.67 PV Pipe: 4 12.0 1.101 PL 13.58 PF 0.6 4 30.0 0.0 11.1 0.0 4.0 150 FTG E2R PE 0.0 5 30.0 3.7 10.5 12.0 0.026 TL 22.58 PV Pipe: 5 -12.0 1.101 PL 15.00 PF 0.5 4 30.0 0.0 11.1 0.0 4.0 150 FTG T PE 6.5 6 15.0 0.0 18.1 0.0 0.026 TL 20.00 PV Pipe: 6 -12.0 1.101 PL 10.42 PF 0.6 6 15.0 0.0 18.1 0.0 4.0 150 FTG ET PE 0.0 7 15.0 0.0 18.7 0.0 0.026 TL 22.42 PV Pipe: 7 -6.4 1.101 PL 5.33 PF 0.1 7 15.0 0.0 18.7 0.0 2.2 150 FTG T PE 0.0 7A 15.0 0.0 18.8 0.0 0.008 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 18.8 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 18.8 0.0 0.000 TL 14.42 PV Pipe: 7B -6.4 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 18.8 0.0 2.2 150 FTG R PE 0.0 7C 15.0 0.0 18.8 0.0 0.008 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 18.8 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 18.8 0.0 0.000 TL 30.17 PV Pipe: 7D -6.4 1.101 PL 46.08 PF 0.5 7C 15.0 0.0 18.8 0.0 2.2 150 FTG T6R PE 0.0 8 15.0 0.0 19.3 0.0 0.008 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 19.3 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 19.3 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 1HD.SDF JOB TITLE: 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: 9 -6.4 1.101 PL 9.33 PF 0.1 8 15.0 0.0 19.3 0.0 2.2 150 FTG 2R PE 0.0 10 15.0 0.0 19.4 0.0 0.008 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 19.4 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 19.4 0.0 0.000 TL 20.75 PV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 19.3 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 12.8 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 12.8 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 12.8 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 12.8 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 12.8 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 12.8 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 12.8 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 12.8 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 12.8 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 12.8 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 17.1 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 17.1 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 17.1 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 17.1 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 17.1 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 9.83 PF 0.0 19 20.0 0.0 17.1 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 17.1 0.0 0.000 TL 28.83 PV Pipe: 20 0.0 1.101 PL 7.08 PF 0.0 19 20.0 0.0 17.1 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 17.1 0.0 0.000 TL 26.08 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 17.1 0.0 0.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 17.1 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - IHD.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 17.1 0.0 0.0 150 FIG 3E PE -4.3 16 30.0 0.0 12.8 0.0 0.000 TL 31.00 Pv Pipe: 23 -6.4 1.101 PL 27.08 PF 0.3 10 15.0 0.0 19.4 0.0 2.2 150 FTG E2R PE 0.0 23 15.0 0.0 19.7 0.0 0.008 TL 36.08 PV Pipe: 24 -12.0 1.598 PL 2.25 PF 0.0 23 15.0 0.0 19.7 0.0 1.9 150 FIG T PE 0.0 24 15.0 0.0 19.7 0.0 0.004 TL 10.25 PV Pipe: 25 5.6 1.101 PL 61.17 PF 0.5 23 15.0 0.0 19.7 0.0 1.9 150 FTG ETSR PE 0.0 25 15.0 0.0 19.2 0.0 0.006 TL 78.17 PV Pipe: 26 5.6 1.101 PL 16.00 PF 0.2 25 15.0 0.0 19.2 0.0 1.9 150 FTG ETR PE 0.0 25A 15.0 0.0 19.0 0.0 0.006 TL 29.00 PV Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 19.0 0.0 0.0 150 FTG ET PE 0.0 25B 15.0 0.0 19.0 0.0 0.000 TL 17.50 PV Pipe: 26B 5.6 1.101 PL 7.58 PF 0.1 25A 15.0 0.0 19.0 0.0 1.9 150 FTG T2R PE 0.0 25C 15.0 0.0 18.9 0.0 0.006 TL 14-.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 18.9 0.0 0.0 150 FIG R PE 0.0 25D 15.0 0.0 18.9 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 18.9 0.0 0.0 150 FIG 2E2R PE 0.0 25E 15.0 0.0 18.9 0.0 0.000 TL 24.42 PV Pipe: 26F 5.6 1.101 PL 15.33 PF 0.2 25C 15.0 0.0 18.9 0.0 1.9 150 FTG 2T2R PE 0.0 7 15.0 0.0 18.7 0.0 0.006 TL 27.33 PV Pipe: 27 -12.0 1.598 PL 15.00 PF 0.1 24 15.0 0.0 19.7 0.0 1.9 150 FTG E PE 6.5 26 0.0 0.0 26.3 0.0 0.004 TL 24.00 PV Pipe: 28 -12.0 1.598 PL 25.00 PF 0.3 26 0.0 0.0 26.3 0.0 1.9 150 FIG 4ER PE 0.0 TR 0.0 0.0 26.6 0.0 0.004 TL 62.00 PV Pipe: 100 -12.0 1.598 PL 5.00 PF 0.1 TR 0.0 0.0 26.6 0.0 1.9 150 FTG E PE 2.2 FS -5.0 0.0 28.8 0.0 0.004 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FIR - 1HD.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOE. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 31.8 0.0 3.0 psi, 12.0 gpm FS -5.0 0.0 28.8 0.0 Pipe: 102 -12.0 1.101 PL 3.00 PF 0.3 FS1 -5.0 0.0 31.8 0.0 4.0 150 FTG 2RC PE 1.3 BR -8.0 0.0 33.5 0.0 0.026 TL 13.00 PV Pipe: 103 -12.0 1.055 PL 2.00 PF 0.3 BR -8.0 0.0 33.5 0.0 4.4 150 FTG 2E PE 0.0 U1 -8.0 H.S. 33.7 5.0 0.033 TL 8.00 PV Pipe: 104 -17.0 1.025 PL 10.00 PF 0.9 U1 -8.0 H.S. 33.7 5.0 6.6 150 FTG E PE -4.3 U2 2.0 0.0 30.3 0.0 0.071 TL 13.00 PV Pipe: 105 -17.0 2.003 PL 70.00 PF 0.3 U2 2.0 0.0 30.3 0.0 1.7 150 FTG 5E PE 6.5 U3 -13.0 0.0 37.2 0.0 0.003 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 41.2 0.0 4.0 psi, 17.0 gpm U3 -13.0 0.0 37.2 0.0 Pipe: 107 -17.0 0.995 PL 10.00 PF 2.5 U4 -13.0 0.0 41.2 0.0 7.0 150 FTG TX PE 0.9 SRC -15.0 SRCE 44.5 (N/A) 0.083 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 computer program in accordance with NFPA13 (2016) under license no. 38061304 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 0.001 gpm and a maximum imbalance at any node of 0.046 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 7.0 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 1HD.SDF JOB TITLE: 70.97 psi with a flow of 24.53 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 1HD.SDF JOB TITLE: 0 0 m 0 0 0 0 0 0 0 o c 0 w r �o v1 w cn N .•i o i 04Dtaw aswmw0aw —aW'H- C v U N C O V1 91 U 4 k .i }1 C W 11 v ro a c 4J O V1 Q V H U q 0 b O N sa ro w m ro v v C 11 'i J1 ro N v D N v o N x ro 0 C O O N 'O N v V W N A 4J M ro ro U rl ul v v C N •.i C Vl N co N W C M •� a a v U 41 a)i a w W ro a a o •i N GI 0 O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2ND FLR - 1HD.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I I \ I \ 60+ \ I \ I \ I \ 54+ \ I I \ I \ P 48+ \ R I \ E X \\ S I \ S 42+ \ U I \ R I \ E \ 36+ \ ( I \ P \\ S I \ I 30+ \ I \ I \ 24+ \ I \ I \ I * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I 12+ LEGEND I " I X = Required Water Supply " 1 44.52 psi @ 17.0 gpm 6+ " I 0 = Available Water Supply " I 70.99 psi @ 17.0 gpm " _+---+----+-----+_-----+-_------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 1ST FLOOR 2 HD GUEST SUITE CALC FILE NUMBER: 13526 DATE: MAY 18, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 450.0 sq. ft. COVERAGE PER SPRINKLER: 225.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 24.4 gpm TOTAL WATER REQUIRED (including hose): 29.4 gpm FLOW AND PRESSURE (@ BOR): 24.4 gpm @ 30.8 psi REQUIRED PRESSURE (@ SRC): 49.1 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD.SDF JOB TITLE: i s t.4 Y-1;7.3i19 4 A'447.4" SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 71.0 20.0 1500.0 71.0 29.4 49.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 29.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 24.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 5.4 - - - 2 30.0 - - - - 5.4 - - - 3 30.0 - - - - 5.4 - - - 4 30.0 - - - - 5.4 - - - 5 30.0 - - - - 5.4 - - - 6 15.0 - - - - 11.9 - - - 7 15.0 - - - - 11.9 - - - 7A 15.0 - - - - 12.1 - - - 7B 15.0 - - - - 12.1 - - - 7C 15.0 - - - - 12.2 - - - 7D 15.0 - - - - 12.2 - - - 8 15.0 - - - - 13.6 - - - 9 15.0 - - - - 13.6 - - - 10 15.0 - - - - 13.9 - - - 11 15.0 - - - - 13.9 - - - 12 30.0 - - - - 7.1 - - - 13 30.0 - - - - 7.1 - - - 14 30.0 - - - - 7.1 - - - 15 30.0 - - - - 7.1 - - - -16 30.0 - - - - 7.1 - - - 17 20.0 - - - - 11.4 - - - 18 20.0 - - - - 11.4 - - - 19 20.0 - - - - 11.4 - - - 20 20.0 - - - - 11.4 - - - 21 20.0 - - - - 11.4 - - - 22 20.0 - - - - 11.4 - - - 23 15.0 - - - - 14.8 - - - 24 15.0 - - - - 15.0 - - - 25 15.0 - - - - 12.5 - - - 25A 15.0 - - - - 11.6 - - - 25B 15.0 - - - - 11.6 - - - 25C 15.0 K= 3.70 11.2 12.4 25D 15.0 - - - - 11.2 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 K= 3.70 10.5 12.0 26 0.0 - - - - 21.8 - - - TR 0.0 - - - - 22.8 - - - FS -5.0 - - - - 25.2 - - - FS1 -5.0 - - - - 28.2 - - - BR -8.0 - - - - 30.8 - - - U1 -8.0 HOSE STREAM 31.8 5.0 U2 2.0 - - - - 30.0 - - - U3 -13.0 - - - - 37.4 - - - U4 -13.0 - - - - 41.4 - - - SRC -15.0 SOURCE 49.1 29.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD.SDF JOB TITLE: 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 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 5.4 0.0 0.0 150 FTG 2E PE 0.0 2 30.0 0.0 5.4 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 5.4 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 5.4 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 5.4 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 5.4 0.0 0.000 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 5.4 0.0 0.0 150 FTG E2R PE 0.0 5 30.0 0.0 5.4 0.0 0.000 TL 22.58 PV Pipe: 5 0.0 1.101 PL 15.00 PF 0.0 4 30.0 0.0 5.4 0.0 0.0 150 FTG T PE 6.5 6 15.0 0.0 11.9 0.0 0.000 TL 20.00 PV Pipe: 6 0.0 1.101 PL 10.42 PF 0.0 6 15.0 0.0 11.9 0.0 0.0 150 FTG ET PE 0.0 7 15.0 0.0 11.9 0.0 0.000 TL 22.42 PV Pipe: 7 -11.6 1.101 PL 5.33 PF 0.3 7 15.0 0.0 11.9 0.0 3.9 150 FTG T PE 0.0 7A 15.0 0.0 12.1 0.0 0.025 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 12.1 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 12.1 0.0 0.000 TL 14.42 PV Pipe: 7B -11.6 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 12.1 0.0 3.9 150 FTG R PE 0.0 7C 15.0 0.0 12.2 0.0 0.025 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 12.2 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 12.2 0.0 0.000 TL 30.17 PV Pipe: 7D -11.6 1.101 PL 46.08 PF 1.4 7C 15.0 0.0 12.2 0.0 3.9 150 FTG T6R PE 0.0 8 15.0 0.0 13.6 0.0 0.025 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 13.6 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 13.6 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD.SDF JOB TITLE: 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: 9 -11.6 1.101 PL 9.33 PF 0.3 8 15.0 0.0 13.6 0.0 3.9 150 FTG 2R PE 0.0 10 15.0 0.0 13.9 0.0 0.025 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 13.9 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 13.9 0.0 0.000 TL 20.75 FV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 13.6 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 7.1 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 7.1 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 7.1 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 7.1 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 7.1 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 7.1 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 7.1 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 7.1 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 7.1 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 7.1 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 11.4 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 11.4 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 11.4 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 11.4 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 11.4 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 9.83 PF 0.0 19 20.0 0.0 11.4 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 11.4 0.0 0.000 TL 28.83 PV Pipe: 20 0.0 1.101 PL 7.08 PF 0.0 19 20.0 0.0 11.4 0.0 0.0 150 FIG 2ET PE 0.0 21 20.0 0.0 11.4 0.0 0.000 TL 26.08 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 11.4 0.0 0.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 11.4 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/16/2020PORT BEACH\FIRE SPRINKLERS\CALLS\INITIAL\1ST FLR - 2HD.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 11.4 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 7.1 0.0 0.000 TL 31.00 PV Pipe: 23 -11.6 1.101 PL 27.08 PF 0.9 10 15.0 0.0 13.9 0.0 3.9 150 FIG E2R PE 0.0 23 15.0 0.0 14.8 0.0 0.025 TL 36.08 PV Pipe: 24 -24.4 1.598 PL 2.25 PF 0.2 23 15.0 0.0 14.8 0.0 3.9 150 FTG T PE 0.0 24 15.0 0.0 15.0 0.0 0.016 TL 10.25 PV Pipe: 25 12.7 1.101 PL 61.17 PF 2.3 23 15.0 0.0 14.8 0.0 4.3 150 FTG ETSR PE 0.0 25 15.0 0.0 12.5 0.0 0.030 TL 78.17 PV Pipe: 26 12.7 1.101 PL 16.00 PF 0.9 25 15.0 0.0 12.5 0.0 4.3 150 FTG ETR PE 0.0 25A 15.0 0.0 11.6 0.0 0.030 TL 29.00 PV Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 11.6 0.0 0.0 150 FTG ET PE 0.0 25B 15.0 0.0 11.6 0.0 0.000 TL 17.50 PV Pipe: 26B 12.7 1.101 PL 7.58 PF 0.4 25A 15.0 0.0 11.6 0.0 4.3 150 FIG T2R PE 0.0 25C 15.0 3.7 11.2 12.4 0.030 TL 14.58 PV Pipe: 26D 12.0 1.101 PL 0.50 PF 0.0 25C 15.0 3.7 11.2 12.4 4.0 150 FTG R PE 0.0 25D 15.0 0.0 11.2 0.0 0.026 TL 1.50 PV Pipe: 26E 12.0 1.101 PL 8.42 PF 0.6 25D 15.0 0.0 11.2 0.0 4.0 150 FTG 2E2R PE 0.0 25E 15.0 3.7 10.5 12.0 0.026 TL 24.42 PV Pipe: 26F -11.6 1.101 PL 15.33 PF 0.7 25C 15.0 3.7 11.2 12.4 3.9 150 FTG 2T2R PE 0.0 7 15.0 0.0 11.9 0.0 0.025 TL 27.33 PV Pipe: 27 -24.4 1.598 PL 15.00 PF 0.4 24 15.0 0.0 15.0 0.0 3.9 150 FIG E PE 6.5 26 0.0 0.0 21.8 0.0 0.016 TL 24.00 PV Pipe: 28 -24.4 1.598 PL 25.00 PF 1.0 26 0.0 0.0 21.8 0.0 3.9 150 FTG 4ER PE 0.0 TR 0.0 0.0 22.8 0.0 0.016 TL 62.00 PV Pipe: 100 -24.4 1.598 PL 5.00 PF 0.2 TR 0.0 0.0 22.8 0.0 3.9 150 FTG E PE 2.2 FS -5.0 0.0 25.2 0.0 0.016 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/16/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FIR - 2HD.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FSl -5.0 0.0 28.2 0.0 3.0 psi, 24.4 gpm FS -5.0 0.0 25.2 0.0 Pipe: 102 -24.4 1.101 PL 3.00 PF 1.3 FS1 -5.0 0.0 28.2 0.0 8.2 150 FTG 2RC PE 1.3 BR -8.0 0.0 30.8 0.0 0.098 TL 13.00 PV Pipe: 103 -24.4 1.055 PL 2.00 PF 1.0 BR -8.0 0.0 30.8 0.0 8.9 150 FTG 2E PE 0.0 U1 -8.0 H.S. 31.8 5.0 0.121 TL 8.00 PV Pipe: 104 -29.4 1.025 PL 10.00 PF 2.6 U1 -8.0 H.S. 31.8 5.0 11.4 150 FTG E PE -4.3 U2 2.0 0.0 30.0 0.0 0.196 TL 13.00 PV Pipe: 105 -29.4 2.003 PL 70.00 PF 0.9 U2 2.0 0.0 30.0 0.0 3.0 150 FTG 5E PE 6.5 U3 -13.0 0.0 37.4 0.0 0.008 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 41.4 0.0 4.0 psi, 29.4 gpm U3 -13.0 0.0 37.4 0.0 Pipe: 107 -29.4 0.995 PL 10.00 PF 6.8 U4 -13.0 0.0 41.4 0.0 12.1 150 FTG TX PE 0.9 SRC -15.0 SRCE 49.1 (N/A) 0.226 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 computer program in accordance with NFPA13 (2016) under license no. 38061304 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 0.003 gpm and a maximum imbalance at any node of 0.122 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 12.1 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD.SDF JOB TITLE: 70.94 psi with a flow of 38.21 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 5/16/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD.SDF JOB TITLE: 0 a rn 0 O O N ri 0 0 m r•� lV 0 0 0 0 0 0 0 r o a O O O O O 0 O r r l0 to V rl N rl O I a 400FA as w w w 0 9 w --ato-1— 05 w U FI O O w m w 4J C .-I 1) 7 (0 it w ro a C 9) O w w +0 43 H U 0 0 w o w u ro w of rn ro w w O 11 .-I ro N w O m 4J x W 0 O O O ro v A.I w w 411 A w w w u u ro •ri w ro w q u •rl 7 N w w w w R H •�I a a w ro +1 w rA x N ro 0 0 0 r••I N w AJ O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATES/18/2020PORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1ST FLR - 2HD.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I I \ I \ 60+ \ I \ I \ I \ 54+ \ I \ I \ x \ P 48+ \ R I \ E I \\ S I \ S 42+ \ D \ R I \ E I \ 36+ \ ( I \ P \\ S \ 1 30+ \ I \ I I \ 24+ \ I \ I \ I * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 12+ LEGEND I" I X = Required Water Supply IT 49.09 psi @ 29.4 gpm 6+ I 0 = Available Water Supply " I 70.96 psi @ 29.4 gpm 0++-+---+----+-----+--_---+-----,--+--------+---------------------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 1ST FLOOR 1 ED GUEST BATH CALC FILE NUMBER: 13526 DATE: NOV 10, 2020 -DESIGN DATA- ZZ�5�� Aye OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 225.0 sq. £t. COVERAGE PER SPRINKLER: 225.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 1 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 12.0 gpm TOTAL WATER REQUIRED (including hose): 17.0 gpm FLOW AND PRESSURE (@ BOR): 12.0 gpm @ 25.9 psi REQUIRED PRESSURE (@ SRC): 37.0 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY RAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS. INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 1HD.SDF JOB TITLE: 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 71.0 20.0 1500.0 71.0 17.0 37.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 17.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 12.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 - _30...0___ - _..... _. 4.8 2 30.0 - - - - 4.8 - - - 3 30.0 - - - - 4.8 - - - 4 30.0 - - - - 4.8 - - - 5 30.0 - - -- 4.8 - - - 6 15.0 - - - - 11.3 - - - 7 15.0 - - - - 11.3 - - - 7A 15.0 - - - - 11.3 - - - 7B 15.0 - - - - 11.3 - - - 7C 15.0 - - - - 11.3 - - - 7D 15.0 - - - - 11.3 - - - 8 15.0 - - - - 11.7 - - - 9 15.0 - - - - 11.7 - - - 10 15.0 - - - - 11.8 - - - 11 15.0 - - - - 11.8 - - - 12 30.0 - - - - 5.2 - - - 13 30.0 - - - - 5.2 - - - 14 30.0 - - - - 5.2 - - - 15 30.0 - - 5.2 - - - 16 30.0 - - - - 5.2 - - - 17 20.0 - - - - 9.5 - - - 18 20.0 - - - - 9.5 - - - 19 20.0 - - - - 9.5 - - - 20 20.0 - - - - 9.5 - - - 21 20.0 - - - - 9.5 - - - 22 20.0 - - - - 9.5 - - - 23 15.0 - - - - 12.0 - - - 24 5.0 - - - - 16.7 - - - 25 15.0 - - - - 11.2 - - - 25A 15.0 - - - - - 11.0 - - - 25B 15.0 K= 3.70 10.5 12.0 25C 15.0 - - - - 11.1 - - - 25D 15.0 - - - - 11.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 1HD.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - 11.1 - - - 26 0.0 - - - - 18.9 - - - TR 0.0 - - - - 19.1 - - - FS -5.0 - - - - 21.3 - - - FS1 -5.0 - - - - 24.3 - - - BR -8.0 - - - - 25.9 - - - U1 -8.0 HOSE STREAM 26.2 5.0 U2 2.0 - - - - 22.8 - - - U3 -13.0 - - - - 29.6 - - - U4 -13.0 - - - - 33.6 - - - SRC -15.0 SOURCE 37.0 17.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 .• DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 1HD.SDF JOB TITLE: 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 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 4.8 0.0 0.0 150 FTG 2E PE 0.0 2 30.0 0.0 4.8 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 4.8 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 4.8 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 4.8 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 4.8 0.0 0.000 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 4.8 0.0 0.0 150 FTG E2R PE 0.0 5 30.0 0.0 4.8 0.0 0.000 TL 22.58 PV Pipe:-5---- - ----- -- 0.0 --1-.101-PL--15.00- -PF- -0.0 -- 4 30.0 0.0 4.8 0.0 0.0 150 FTG T PE 6.5 6 15.0 0.0 11.3 0.0 0.000 TL 20.00 PV Pipe: 6 0.0 1.101 PL 10.42 PF 0.0 6 15.0 0.0 11.3 0.0 0.0 150 FTG ET PE 0.0 7 15.0 0.0 11.3 0.0 0.000 TL 22.42 PV Pipe: 7 -5.6 1.101 PL 5.33 PF 0.1 7 15.0 0.0 11.3 0.0 1.9 150 FTG T PE 0.0 7A 15.0 0.0 11.3 0.0 0.006 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 11.3 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 11.3 0.0 0.000 TL 14.42 PV Pipe: 7B -5.6 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 11.3 0.0 1.9 150 FTG R PE 0.0 7C 15.0 0.0 11.3 0.0 0.006 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 11.3 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 11.3 0.0 0.000 TL 30.17 PV Pipe: 7D -5.6 1.101 PL 46.08 PF 0.4 7C 15.0 0.0 11.3 0.0 1.9 150 FTG T6R PE 0.0 8 15.0 0.0 11.7 0.0 0.006 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 11.7 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 11.7 0.0 0.000 TL 20.08 PV - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 1HD.SDF JOB TITLE: 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: 9 -5.6 1.101 PL 9.33 PF 0.1 8 15.0 0.0 11.7 0.0 1.9 150 FTG 2R PE 0.0 10 15.0 0.0 11.8 0.0 0.006 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 11.8 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 11.8 0.0 0.000 TL 20.75 PV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 11.7 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 5.2 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 5.2 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 5.2 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 5.2 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 5.2 0.0 0.000 TL 23.75 FV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 5.2 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 5.2 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 5.2 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 5.2 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 5.2 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 9.5 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 9.5 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 9.5 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 9.5 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 9.5 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 13.50 PF 0.0 19 20.0 0.0 9.5 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 9.5 0.0 0.000 TL 32.50 PV Pipe: 20 0.0 1.101 PL 8.67 PF 0.0 19 20.0 0.0 9.5 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 9.5 0.0 0.000 TL 27.67 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 9.5 0.0 0.0 150 FIG 2E2TR PE 0.0 22 20.0 0.0 9.5 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 ., DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 1HD.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 9.5 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 5.2 0.0 0.000 TL 31.00 FV Pipe: 23 -5.6 1.101 PL 27.08 PF 0.2 10 15.0 0.0 11.8 0.0 1.9 150 FTG E2R PE 0.0 23 15.0 0.0 12.0 0.0 0.006 TL 36.08 FV Pipe: 24 -12.0 1.598 PL 23.58 PF 0.4 23 15.0 0.0 12.0 0.0 1.9 150 FIG 6ET PE 4.3 24 5.0 0.0 16.7 0.0 0.004 TL 85.58 PV Pipe: 25 6.4 1.101 PL 74.50 PF 0.8 23 15.0 0.0 12.0 0.0 2.2 150 FTG ETSR PE 0.0 25 15.0 0.0 11.2 0.0 0.008 TL 91.50 PV Pipe: 26 6.4 1.101 PL 16.00 PF 0.2 25 15.0 0.0 11.2 0.0 2.2 150 FTG ETR PE 0.0 25A 15.-0 _._ 0..0-1-1-.0- - 0..0_--0-.008-TL-- 29.00 --PV- Pipe: 26A 12.0 1.101 PL 5.50 PF 0.5 25A 15.0 0.0 11.0 0.0 4.0 150 FTG ET PE 0.0 25B 15.0 3.7 10.5 12.0 0.026 TL 17.50 PV Pipe: 26B -5.6 1.101 PL 7.58 PF 0.1 25A 15.0 0.0 11.0 0.0 1.9 150 FTG T2R PE 0.0 25C 15.0 0.0 11.1 0.0 0.006 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 11.1 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 11.1 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 11.1 0.0 0.0 150 FTG 2E2R PE 0.0 25E 15.0 0.0 11.1 0.0 0.000 TL 24.42 PV Pipe: 26F -5.6 1.101 PL 15.33 PF 0.2 25C 15.0 0.0 11.1 0.0 1.9 150 FTG 2T2R PE 0.0 7 15.0 0.0 11.3 0.0 0.006 TL 27.33 PV Pipe: 27 -12.0 1.598 PL 5.00 PF 0.1 24 5.0 0.0 16.7 0.0 1.9 150 FTG E PE 2.2 26 0.0 0.0 18.9 0.0 0.004 TL 14.00 PV Pipe: 28 -12.0 1.598 PL 3.50 PF 0.1 26 0.0 0.0 18.9 0.0 1.9 150 FTG 3ER PE 0.0 TR 0.0 0.0 19.1 0.0 0.004 TL 31.50 PV Pipe: 100 -12.0 1.598 PL 5.00 PF 0.1 TR 0.0 0.0 19.1 0.0 1.9 150 FTG E PE 2.2 FS -5.0 0.0 21.3 0.0 0.004 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALLS\D2\1ST FLR - 1HD.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 24.3 0.0 3.0 psi, 12.0 gpm FS -5.0 0.0 21.3 0.0 Pipe: 102 -12.0 1.101 PL 3.00 PF 0.3 FS1 -5.0 0.0 24.3 0.0 4.0 150 FIG 2RC PE 1.3 BR -8.0 0.0 25.9 0.0 0.026 TL 13.00 PV Pipe: 103 -12.0 1.055 PL 2.00 PF 0.3 BR -8.0 0.0 25.9 0.0 4.4 150 FTG 2E PE 0.0 U1 -8.0 H.S. 26.2 5.0 0.033 TL 8.00 PV Pipe: 104 -17.0 1.025 PL 10.00 PF 0.9 U1 -8.0 H.S. 26.2 5.0 6.6 150 FIG E PE -4.3 U2 2.0 0.0 22.8 0.0 0.071 TL 13.00 PV Pipe: 105 -17.0 2.003 PL 70.00 PF 0.3 U2 2.0 0.0 22.8 0.0 1.7 150 FTG 5E PE 6.5 U3 -13.0 0.0 29.6 0.0 0.003 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 33.6 0.0 4.0 psi, 17.0 gpm U3 -13.0 0.0 29.6 0.0 Pipe: 107 -17.0 0.995 PL 10.00 PF 2.5 U4 -13.0 0.0 33.6 0.0 7.0 150 FTG TX PE 0.9 SRC -15.0 SRCE 37.0 (N/A) 0.082 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) under license no. 64623334 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 0.001 gpm and a maximum imbalance at any node pf 0.051 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 7.0 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 1HD.SDF JOB TITLE: 70.97 psi with a flow of 26.67 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: X MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N X Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter ---- Equivalent -Fitting -Lengths -in- Feet- ---- ----- - ---- - -- --- - -- --- (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 w SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 1HD.SDF JOB TITLE: ac O W .H N a 0 0 0 N 0 0 w 0 0 0 0 0 0 0 o a 0 0 o 0 0 0 0 r ko in a fn N .-i o i 0 .4 D o w a 9 w w w 0 9 W " a N -1 � m N U is O O N N al 1-i ,4 r-i 0 iJ 7 N i N ro a a +3 o N •.i al +� H U 0 b o at N U W rg N ro N N ° u r-I -p ro N D w U N 4J x ro H 0 a ro v N N m N A .p u ro ro U •.i N Id ai a u N Na) N N R N a w v N v ,c w N ro q q O H N al 0 O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 1HD.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I \ I \ I \ 60+ \ I \ I \ I \ 54+ \ I \ I \ I \ P 48+ \ R I \ E I \\ S \ U I \ R I \ E X \ 36+ \ ( I \ P I \\ S I \ I 30+ \ I \ I I \ 24+ \ I \ I \ I * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 1= - 12+ LEGEND I" I X = Required Water Supply " I 36.96 psi @ 17.0 gpm " 6+ I 0 = Available Water Supply I 70.99 psi @ 17.0 gpm -+---+----+-----+--____+--_-----+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 1ST FLOOR 2 HD LIVING ROOM CALC FILE NUMBER: 13526 DATE: NOV10, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 392.0 sq. ft. COVERAGE PER SPRINKLER: 196.0 sq. £t. max. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 20.1 gpm TOTAL WATER REQUIRED (including hose): 25.1 gpm FLOW AND PRESSURE (@ BOR): 20.1 gpm @ 35.2 psi REQUIRED PRESSURE (@ SRC): 50.6 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 11/10/202ORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FIR - 2HD PROOF.SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SRC 71.0 20.0 1500.0 AGGREGATE FLOW ANALYSIS: AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 71.0 25.1 50.6 TOTAL FLOW AT SOURCE 25.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 -_ 30--0 __ _ -- _- - - _. - 12.-0_._ -. __--- - 2 30.0 - - - - 12.0 - - - 3 30.0 - - - - 12.0 - - - 4 30.0 - - - - 12.0 - - - 5 30.0 - - - - 12.0 - - - 6 15.0 - - - - 18.5 - - - 7 15.0 - - - - 18.5 - - - 7A 15.0 - - - - 18.5 - - - 7B 15.0 - - - - 18.5 - - - 7C 15.0 - - - - 18.4 - - - 7D 15.0 - - - - 18.4 - - - 8 15.0 - - - - 18.0 - - - 9 15.0 - - - - 16.7 - - - 10 15.0 - - - - 18.4 - - - 11 15.0 - - - - 18.4 - - - 12 30.0 - - - - 8.7 - - - 13 30.0 - - - - 8.1 - - - 14 30.0 - - - - 8.3 - - - 15 30.0 - - - - 8.3 - - - 16 30.0 - - - - 7.9 - - - 17 20.0 - - - - 11.9 - - - 18 20.0 - - - - 11.1 - - - 19 20.0 - - -- 7.9 --- 20 20.0 K= 3.70 7.3 10.0 21 20.0 K= 3.70 7.4 10.1 22 20.0 - - - - 11.8 - - - 23 15.0 - - - - 19.7 - - - 24 5.0 - - - - 25.0 - - - 25 15.0 - - - - 19.0 - - - 25A 15.0 - - - - 18.8 - - - 25B 15.0 - - - - 18.8 - - 25C 15.0 - - - - 18.7 - - - 25D 15.0 - - - - 18.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 11/10/2020RT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD PROOF.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - 18.7 - - - 26 0.0 - - - - 27.3 - - - TR 0.0 - - - - 27.7 - - - FS -5.0 - - - - 30.0 - - - FS1 -5.0 - - - - 33.0 - - - BR -8.0 - - - - 35.2 - - - U1 -8.0 HOSE STREAM 35.9 5.0 U2 2.0 - - - - 33.4 - - - U3 -13.0 - - - - 40.6 - - - U4 -13.0 - - - - 44.6 - - - SRC -15.0 SOURCE 50.6 25.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 11/10/2020RT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD PROOF.SDF JOB TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. 8T DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 12.0 0.0 0.0 150 FTG 2E PE 0.0 2 30.0 0.0 12.0 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 12.0 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 12.0 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 12.0 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 12.0 0.0 0.000 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 12.0 0.0 0.0 150 FTG E2R PE 0.0 5 30.0 0.0 12.0 0.0 0.000 TL 22.58 PV Pipe:- 5 --- - --0.0 - 1.-101-PL- 15-.00- -PT -- -0 ;0 - 4 30.0 0.0 12.0 0.0 0.0 150 FTG T PE 6.5 6 15.0 0.0 18.5 0.0 0.000 TL 20.00 PV Pipe: 6 0.0 1.101 PL 10.42 PF 0.0 6 15.0 0.0 18.5 0.0 0.0 150 FTG ET PE 0.0 7 15.0 0.0 18.5 0.0 0.000 TL 22.42 PV Pipe: 7 6.0 1.101 PL 5.33 PF 0.1 7 15.0 0.0 18.5 0.0 2.0 150 FTG T PE 0.0 7A 15.0 0.0 18.5 0.0 0.007 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 18.5 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 18.5 0.0 0.000 TL 14.42 PV Pipe: 7B 6.0 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 18.5 0.0 2.0 150 FIG R PE 0.0 7C 15.0 0.0 18.4 0.0 0.007 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 18.4 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 18.4 0.0 0.000 TL 30.17 PV Pipe: 7D 6.0 1.101 PL 46.08 PF 0.4 7C 15.0 0.0 18.4 0.0 2.0 150 FTG T6R PE 0.0 8 15.0 0.0 18.0 0.0 0.007 TL 57.08 PV Pipe: 8 20.1 1.101 PL 8.08 PF 1.4 8 15.0 0.0 18.0 0.0 6.8 150 FTG ET PE 0.0 9 15.0 0.0 16.7 0.0 0.068 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 11/10/2020RT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD PROOF.SDF JOB TITLE: 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: 9 -14.1 1.101 PL 9.33 PF 0.4 8 15.0 0.0 18.0 0.0 4.7 150 FTG 2R PE 0.0 10 15.0 0.0 18.4 0.0 0.036 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 18.4 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 18.4 0.0 0.000 TL 20.75 PV Pipe: 11 20.1 1.101 PL 15.00 PF 1.5 9 15.0 0.0 16.7 0.0 6.8 150 FTG E PE -6.5 12 30.0 0.0 8.7 0.0 0.068 TL 22.00 PV Pipe: 12 11.0 1.101 PL 6.08 PF 0.6 12 30.0 0.0 8.7 0.0 3.7 150 FTG 2ETR PE 0.0 13 30.0 0.0 8.1 0.0 0.023 TL 26.08 PV Pipe: 13 9.0 1.101 PL 12.75 PF 0.4 12 30.0 0.0 8.7 0.0 3.0 150 FIG 2TR PE 0.0 14 30.0 0.0 8.3 0.0 0.016 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 8.3 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 8.3 0.0 0.000 TL 5.50 PV Pipe: 15 9.0 1.101 PL 9.08 PF 0.4 14 30.0 0.0 8.3 0.0 3.0 150 FTG 3T PE 0.0 16 30.0 0.0 7.9 0.0 0.016 TL 24.08 PV Pipe: 16 11.0 1.101 PL 10.00 PF 0.5 13 30.0 0.0 8.1 0.0 3.7 150 FTG 2E PE 4.3 17 20.0 0.0 11.9 0.0 0.023 TL 24.00 PV Pipe: 17 11.0 1.101 PL 18.33 PF 0.7 17 20.0 0.0 11.9 0.0 3.7 150 FTG ETR PE 0.0 18 20.0 0.0 11.1 0.0 0.023 TL 31.33 PV Pipe: 18 20.1 1.101 PL 14.17 PF 3.2 18 20.0 0.0 11.1 0.0 6.8 150 FTG 4ET PE 0.0 19 20.0 0.0 7.9 0.0 0.068 TL 47.17 PV Pipe: 19 10.0 1.101 PL 13.50 PF 0.6 19 20.0 0.0 7.9 0.0 3.4 150 FTG 2ET PE 0.0 20 20.0 3.7 7.3 10.0 0.019 TL 32.50 PV Pipe: 20 10.1 1.101 PL 8.67 PF 0.5 19 20.0 0.0 7.9 0.0 3.4 150 FTG 2ET PE 0.0 21 20.0 3.7 7.4 10.1 0.019 TL 27.67 PV Pipe: 21 -9.0 1.101 PL 14.17 PF 0.6 18 20.0 0.0 11.1 0.0 3.0 150 FIG 2E2TR PE 0.0 22 20.0 0.0 11.8 0.0 0.016 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 11/10/2020RT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD PROOF.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HN(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 22 -9.0 1.101 PL 10.00 PF 0.5 22 20.0 0.0 11.8 0.0 3.0 150 FTG 3E PE -4.3 16 30.0 0.0 7.9 0.0 0.016 TL 31.00 PV Pipe: 23 -14.1 1.101 PL 27.08 PF 1.3 10 15.0 0.0 18.4 0.0 4.7 - 150 FIG E2R PE 0.0 23 15.0 0.0 19.7 0.0 0.036 TL 36.08 PV Pipe: 24 -20.1 1.598 PL 23.58 PF 1.0 23 15.0 0.0 19.7 0.0 3.2 150 FTG 6ET PE 4.3 24 5.0 0.0 25.0 0.0 0.011 TL 85.58 PV Pipe: 25 6.0 1.101 PL 74.50 PF 0.7 23 15.0 0.0 19.7 0.0 2.0 150 FTG ETSR PE 0.0 25 15.0 0.0 19.0 0.0 0.007 TL 91.50 PV Pipe: 26 6.0 1.101 PL 16.00 PF 0.2 25 15.0 0.0 19.0 0.0 2.0 150 FTG ETR PE 0.0 25A 15.0- 0.0---18-.-8---0.0------0.007-TL 29-.00--PV --------------- --- Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 18.8 0.0 0.0 150 FTG ET PE 0.0 25B 15.0 0.0 18.8 0.0 0.000 TL 17.50 PV Pipe: 26B 6.0 1.101 PL 7.58 PF 0.1 25A 15.0 0.0 18.8 0.0 2.0 150 FTG T2R PE 0.0 25C 15.0 0.0 18.7 0.0 0.007 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 18.7 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 18.7 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 18.7 0.0 0.0 150 FIG 2E2R PE 0.0 25E 15.0 0.0 18.7 0.0 0.000 TL 24.42 PV Pipe: 26F 6.0 1.101 PL 15.33 PF 0.2 25C 15.0 0.0 18.7 0.0 2.0 150 FTG 2T2R PE 0.0 7 15.0 0.0 18.5 0.0 0.007 TL 27.33 PV Pipe: 27 -20.1 1.598 PL 5.00 PF 0.2 24 5.0 0.0 25.0 0.0 3.2 150 FTG E PE 2.2 26 0.0 0.0 27.3 0.0 0.011 TL 14.00 PV Pipe: 28 -20.1 1.598 PL 3.50 PF 0.4 26 0.0 0.0 27.3 0.0 3.2 150 FTG 3ER PE 0.0 TR 0.0 0.0 27.7 0.0 0.011 TL 31.50 PV Pipe: 100 -20.1 1.598 PL 5.00 PF 0.2 TR 0.0 0.0 27.7 0.0 3.2 150 FTG E PE 2.2 FS -5.0 0.0 30.0 0.0 0.011 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 11/10/2020RT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD PROOF.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 33.0 0.0 3.0 psi, 20.1 gpm FS -5.0 0.0 30.0 0.0 Pipe: 102 -20.1 1.101 PL 3.00 PF 0.9 FS1 -5.0 0.0 33.0 0.0 6.8 150 FTG 2RC PE 1.3 BR -8.0 0.0 35.2 0.0 0.068 TL 13.00 PV Pipe: 103 -20.1 1.055 PL 2.00 PF 0.7 BR -8.0 0.0 35.2 0.0 7.4 150 FTG 2E PE 0.0 U1 -8.0 H.S. 35.9 5.0 0.084 TL 8.00 PV Pipe: 104 -25.1 1.025 PL 10.00 PF 1.9 U1 -8.0 H.S. 35.9 5.0 9.7 150 FTG E PE -4.3 U2 2.0 0.0 33.4 0.0 0.146 TL 13.00 PV Pipe: 105 -25.1 2.003 PL 70.00 PF 0.7 U2 2.0 0.0 33.4 0.0 2.6 150 FTG 5E PE 6.5 U3 -13.0 0.0 40.6 0.0 0.006 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 44.6 0.0 4.0 psi, 25.1 gpm U3 -13.0 0.0 40.6 0.0 Pipe: 107 -25.1 0.995 PL 10.00 PF 5.1 U4 -13.0 0.0 44.6 0.0 10.3 150 FTG TX PE 0.9 SRC -15.0 SRCE 50.6 (N/A) 0.169 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) under license no. 64623334 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 0.001 gpm and a maximum imbalance at any node of 0.050 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 10.3 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 11/10/2020RT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD PROOF.SDF JOB TITLE: 70.96 psi with a flow of 32.07 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HNC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L EWC: 150 Diameter - ---- Equivalent--Fitting-Lengths-in-Feet --- ---- - - -- -- --- -- (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 11/10/202ORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD PROOF.SDF JOB TITLE: V in v a m ti a H O N O Q � z� a .. yl U a ' W N W ro o 4J w w a w F 0 0 O 0 0 0 0 0 0 0 o c O O O O O O O ' � � N 'C M N '-1 O 1 I 0 F400F4 W 9 N 0 w 0 a w - -am•.i n ro D N U O N (4 y V C .-1 .0 U W L1 v ro a a q O Vrl 4J N E U p S D o ro 4 ro w m ro v v q u .� -p ro m di w D 0 x ro 0 0 N 'U u v 11 N N A 4J ski ro ro U v ro q H N (D W N W a si •�+ a a v v -H v •.i x rn N ro a a o rl N 0) 4J O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 30 DATE: 11/10/2020RT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD PROOF.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I I \ I \ 60+ \ I \ I \ I \ 54+ \ I \ x \ I \ P 48+ \ R I \ E I \\ S I \ _.. 542+ U I \ R I \ E I \ 36+ \ ( I \ P I \\ S I \ 1 30+ \ I \ I \ 24+ \ I \ I \ 1 * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I I- 12+ LEGEND TT 1 11 X = Required Water Supply 50.57 psi @ 25.1 gpm 6+ 0 = Available Water Supply 70.97 psi @ 25.1 gpm 0++-+---+----+-----+------+-----'---------------------------------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 1ST FLOOR 2 ED GARAGE CALC FILE NUMBER: 13526 DATE: NOV 10, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 512.0 sq. ft. COVERAGE PER SPRINKLER: 256.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 26.4 gpm TOTAL WATER REQUIRED (including hose): 31.4 gpm FLOW AND PRESSURE (@ BOR): 26.4 gpm @ 29.3 psi REQUIRED PRESSURE (@ SRC): 49.1 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD GARAGE.SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SRC 71.0 20.0 1500.0 AGGREGATE FLOW ANALYSIS: AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 71.0 31.4 49.1 TOTAL FLOW AT SOURCE 31.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 _.30.0 __ _ _ _ _. _-_1...7_.. 1.7- ___._____ 2 30.0 - - - - 1.7 - - - 3 30.0 - - -- 1.7 - - - 4 30.0 - - -- 1.7 - - - 5 30.0 - - -- 1.7 - - - 6 15.0 - - - - 8.2 - - - 7 15.0 - - - - 8.2 - - - 7A 15.0 - - - - 8.0 - - - 7B 15.0 K= 4.90 7.5 13.4 7C 15.0 - - - - 8.0 - - - 7D 15.0 K= 4.90 7.0 13.0 8 15.0 - - - - 10.2 - - - 9 15.0 - - - - 10.2 - - - 10 15.0 - - - - 10.7 - - - 11 15.0 - - - - 10.7 - - - 12 30.0 - - - - 3.7 - - - 13 30.0 - - - - 3.7 - - - 14 30.0 - - - - 3.7 - - - 15 30.0 - - - - 3.7 - - - 16 30.0 - - - - 3.7 - - - 17 20.0 - - -- 8.1 --- 18 20.0 - - - - 8.1 - - - 19 20.0 - - - - 8.1 - - - 20 20.0 - - - - 8.1 - - - 21 20.0 - - - - 8.1 - - - 22 20.0 - - - - 8.1 - - - 23 15.0 - - - - 12.1 - - - 24 5.0 - - - - 18.0 - - - 25 15.0 - - - - 9.9 - - - 25A 15.0 - - - - 9.2 - - - 25B 15.0 - - - - 9.2 - - - 25C 15.0 - - - - 8.9 - - - 25D 15.0 - - - - 8.9 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD GARAGE.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - 8.9 - - - 26 0.0 - - - - 20.5 - - - TR 0.0 - - - - 21.1 - - - FS -5.0 - - - - 23.5 - - - FSS -5.0 - - - - 26.5 - - - BR -8.0 - - - - 29.3 - - - U1 -8.0 HOSE STREAM 30.4 5.0 U2 2.0 - - - - 28.9 - - - U3 -13.0 - - - - 36.5 - - - U4 -13.0 - - - - 40.5 - - - SRC -15.0 SOURCE 49.1 31.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2RD GARAGE.SDF JOB TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HN(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 1.7 0.0 0.0 150 FTG 2E PE 0.0 2 30.0 0.0 1.7 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 1.7 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 1.7 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 1.7 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 1.7 0.0 0.000 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 1.7 0.0 0.0 150 FTG E2R PE 0.0 5 30.0 0.0 1.7 0.0 0.000 TL 22.58 PV Pipe: 5 _ _. _ - _- _-0.0 -. -1.101 PL_ ..15.00 --PF-- 0..0._- 4 30.0 0.0 1.7 0.0 0.0 150 FTG T PE 6.5 6 15.0 0.0 8.2 0.0 0.000 TL 20.00 PV Pipe: 6 0.0 1.101 PL 10.42 PF 0.0 6 15.0 0.0 8.2 0.0 0.0 150 FTG ET PE 0.0 7 15.0 0.0 8.2 0.0 0.000 TL 22.42 PV Pipe: 7 11.4 1.101 PL 5.33 PF 0.2 7 15.0 0.0 8.2 0.0 3.8 150 FTG T PE 0.0 7A 15.0 0.0 8.0 0.0 0.024 TL 10.33 PV Pipe: 7A 13.4 1.101 PL 2.42 PF 0.5 7A 15.0 0.0 8.0 0.0 4.5 150 FTG ET PE 0.0 7B 15.0 4.9 7.5 13.4 0.032 TL 14.42 PV Pipe: 7B -2.0 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 8.0 0.0 0.7 150 FTG R PE 0.0 7C 15.0 0.0 8.0 0.0 0.001 TL 1.50 PV Pipe: 7C 13.0 1.101 PL 11.17 PF 0.9 7C 15.0 0.0 8.0 0.0 4.4 150 FTG 2ET PE 0.0 7D 15.0 4.9 7.0 13.0 0.031 TL 30.17 PV Pipe: 7D -15.0 1.101 PL 46.08 PF 2.3 7C 15.0 0.0 8.0 0.0 5.1 150 FTG T6R PE 0.0 8 15.0 0.0 10.2 0.0 0.040 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 10.2 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 10.2 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD GARAGE.SDF JOB TITLE: 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: 9 -15.0 1.101 PL 9.33 PF 0.5 8 15.0 0.0 10.2 0.0 5.1 150 FTG 2R PE 0.0 10 15.0 0.0 10.7 0.0 0.040 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 10.7 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 10.7 0.0 0.000 TL 20.75 PV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 10.2 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 3.7 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 3.7 0.0 0.0 150 FIG 2ETR PE 0.0 13 30.0 0.0 3.7 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 3.7 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 3.7 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 3.7 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 3.7 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 3.7 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 3.7 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 3.7 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 8.1 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 8.1 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 8.1 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 8.1 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 8.1 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 13.50 PF 0.0 19 20.0 0.0 8.1 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 8.1 0.0 0.000 TL 32.50 PV Pipe: 20 0.0 1.101 PL 8.67 PF 0.0 19 20.0 0.0 8.1 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 8.1 0.0 0.000 TL 27.67 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 8.1 0.0 0.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 8.1 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD GARAGE.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 8.1 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 3.7 0.0 0.000 TL 31.00 PV Pipe: 23 -15.0 1.101 PL 27.08 PF 1.4 10 15.0 0.0 10.7 0.0 5.1 150 FTG E2R PE 0.0 23 15.0 0.0 12.1 0.0 0.040 TL 36.08 PV Pipe: 24 -26.4 1.598 PL 23.58 PF 1.6 23 15.0 0.0 12.1 0.0 4.2 150 FTG 6ET PE 4.3 24 5.0 0.0 18.0 0.0 0.019 TL 85.58 PV Pipe: 25 11.4 1.101 PL 74.50 PF 2.2 23 15.0 0.0 12.1 0.0 3.8 150 FTG ETSR PE 0.0 25 15.0 0.0 9.9 0.0 0.024 TL 91.50 PV Pipe: 26 11.4 1.101 PL 16.00 PF 0.7 25 15.0 0.0 9.9 0.0 3.8 150 FTG ETR PE 0.0 25A 15.0-- 0.0 9.2- 0.0 _... _--0.024--T-L---29.00-_PV Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 9.2 0.0 0.0 150 FTG ET PE 0.0 25B 15.0 0.0 9.2 0.0 0.000 TL 17.50 PV Pipe: 26B 11.4 1.101 PL 7.58 PF 0.4 25A 15.0 0.0 9.2 0.0 3.8 150 FTG T2R PE 0.0 25C 15.0 0.0 8.9 0.0 0.024 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 8.9 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 8.9 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 8.9 0.0 0.0 150 FTG 2E2R PE 0.0 25E 15.0 0.0 8.9 0.0 0.000 TL 24.42 PV Pipe: 26F 11.4 1.101 PL 15.33 PF 0.7 25C 15.0 0.0 8.9 0.0 3.8 150 FTG 2T2R PE 0.0 7 15.0 0.0 8.2 0.0 0.024 TL 27.33 PV Pipe: 27 -26.4 1.598 PL 5.00 PF 0.3 24 5.0 0.0 18.0 0.0 4.2 150 FTG E PE 2.2 26 0.0 0.0 20.5 0.0 0.019 TL 14.00 PV Pipe: 28 -26.4 1.598 PL 3.50 PF 0.6 26 0.0 0.0 20.5 0.0 4.2 150 FTG 3ER PE 0.0 TR 0.0 0.0 21.1 0.0 0.019 TL 31.50 PV Pipe: 100 -26.4 1.598 PL 5.00 PF 0.3 TR 0.0 0.0 21.1 0.0 4.2 150 FTG E PE 2.2 FS -5.0 0.0 23.5 0.0 0.019 TL 14.00 PV . SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD GARAGE.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 26.5 0.0 3.0 psi, 26.4 gpm FS -5.0 0.0 23.5 0.0 Pipe: 102 -26.4 1.101 PL 3.00 PF 1.5 FS1 -5.0 0.0 26.5 0.0 8.9 150 FTG 2RC PE 1.3 BR -8.0 0.0 29.3 0.0 0.114 TL 13.00 PV Pipe: 103 -26.4 1.055 PL 2.00 PF 1.1 BR -8.0 0.0 29.3 0.0 9.7 150 FTG 2E PE 0.0 U1 -8.0 H.S. 30.4 5.0 0.140 TL 8.00 PV Pipe: 104 -31.4 1.025 PL 10.00 PF 2.9 U1 -8.0 H.S. 30.4 5.0 12.2 150 FTG E PE -4.3 U2 2.0 0.0 28.9 0.0 0.222 TL 13.00 PV Pipe: 105 -31.4 2.003 PL 70.00 PF 1.1 U2 2.0 0.0 28.9 0.0 3.2 150 FTG 5E PE 6.5 U3 -13.0 0.0 36.5 0.0 0.009 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 40.5 0.0 4.0 psi, 31.4 gpm U3 -13.0 0.0 36.5 0.0 Pipe: 107 -31.4 0.995 PL 10.00 PF 7.7 U4 -13.0 0.0 40.5 0.0 13.0 150 FTG TX PE 0.9 SRC -15.0 SRCE 49.1 (N/A) 0.257 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) under license no. 64623334 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 0.001 gpm and a maximum imbalance at any node of 0.011 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 13.0 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALLS\D2\1ST FLR - 2HD GARAGE.SDF JOB TITLE: 70.93 psi with a flow of 41.14 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HNC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter ---- Equivalent Fitting -Lengths -in Feet---- ---- -- ----- -- ---- (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALLS\D2\1ST FIR - 2HD GARAGE.SDF JOB TITLE: ro N v a E, N w a H O v1 O z r N ° a •J a " a ro o w w w a w E 3 0 O w 0 0 0 0 0 0 0 O C O o O O O O O e-I r lD If1 C' m N rl O 1 0 $400rA as wm wDaw "a0'H- 9 W 0 u 0 0 N N y 4J A '-I iJ 0 N Jl v ro a a 43 O N .14 4J W E 0 0 q 0 0) O N N ro w m ro w w 7 N rl •N ro N v U 0 4J ro .i R a ° rd N A 4J u o ro •'I N ro v q N •.a p N N N N U1 q N •a a a w ro 4J v •) x rn N ro q a o e N W 0 O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 11/10/2020T BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD GARAGE.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I I \ I \ 60+ \ I \\ I \ I \ 54+ \ I \ I \ x \ P 48+ \ R I \ E I \\ S I \ U I \ R I \ E I \ 36+ \ ( I \ P I \\ S I \ I 30+ \ I \ I I \ 24+ \ I \ I \ * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 12+ LEGEND I I X = Required Water Supply I 49.07 psi @ 31.4 gpm " 6+ " I 0 = Available Water Supply " I 70.96 psi @ 31.4 gpm " 0++-+---+----+-----+------+-----1--+"----------------------------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 2ND FLOOR 2 HD GYM CALC FILE NUMBER: 13526 DATE: NOV 10, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose): FLOW AND PRESSURE (@ BOR): REQUIRED PRESSURE (@ SRC): SPRINKLER ORIFICE SIZE: NFPA 13D, 2016 EDITION 0.05 gpm/sq. ft. 324.0 sq. ft. 196.0 sq. ft. max. 2 sprinklers 20.0 gpm 25.1 gpm 20.0 gpm @ 37.8 psi 53.2 psi 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS. INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2HD.SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SRC 71.0 20.0 1500.0 AGGREGATE FLOW ANALYSIS: AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 71.0 25.1 53.2 TOTAL FLOW AT SOURCE 25.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE (FT) _ 1 30.0--- - K=_.3..70 2 30.0 - - - - 3 30.0 K= 3.70 4 30.0 - - - - 5 30.0 - - - - 6 15.0 - - - - 7 15.0 ---- 7A 15.0 - - - - 7B 15.0 - - - - 7C 15.0 - - - - 7D 15.0 - - - - 8 15.0 - - - - 9 15.0 - - - - 10 15.0 - - - - 11 15.0 - - - - 12 30.0 - - - - 13 30.0 - - - - 14 30.0 - - - - 15 30.0 - - - - 16 30.0 - - - - 17 20.0 - - - - 18 20.0 - - - - 19 20.0 - - - - 20 20.0 - - - - 21 20.0 - - - - 22 20.0 - - - - 23 15.0 - - - - 24 5.0 - - - - 25 15.0 - - - - 25A 15.0 - - - - 25B 15.0 - - - 25C 15.0 - - - - 25D 15.0 - - - - PRESSURE DISCHARGE (PSI) (GPM) 7--3_- ___10-:0 7.7 - - - 7.3 10.0 10.4 - - - 10.4 - - - 18.3 - - - 19.8 - - - 20.0 - - - 20.0 - - - 20.1 - - - 20.1 - - - 21.3 - - - 21.3 - - - 21.6 - - - 21.6 - - - 14.8 - - - 14.8 - - - 14.8 - - - 14.8 - - - 14.8 - - - 19.2 - - - 19.2 - - - 19.2 - - - 19.2 - - - 19.2 - - - 19.2 - - - 22.4 - - - 27.7 - - - 20.9 - - - 20.5 - - - 20.5 - - - 20.2 - - - 20.2 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2HD.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - - 20.2 - - - 26 0.0 - - - - 30.0 - - - TR 0.0 - - - - 30.3 - - - FS -5.0 - - - - 32.7 - - - FS1 -5.0 - - - - 35.7 - - - BR -8.0 - - - - 37.8 - - - U1 -8.0 HOSE STREAM 38.5 5.0 U2 2.0 - - - - 36.1 - - - U3 -13.0 - - - - 43.3 - - - U4 -13.0 - - - - 47.3 - - - SRC -15.0 SOURCE 53.2 25.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2HD.SDF JOB TITLE: 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 -10.0 1.101 PL 6.92 PF 0.4 1 30.0 3.7 7.3 10.0 3.4 150 FIG 2E PE 0.0 2 30.0 0.0 7.7 0.0 0.019 TL 20.92 PV Pipe: 2 10.0 1.101 PL 7.08 PF 0.4 2 30.0 0.0 7.7 0.0 3.4 150 FTG ET PE 0.0 3 30.0 3.7 7.3 10.0 0.019 TL 19.08 PV Pipe: 3 -20.0 1.101 PL 25.67 PF 2.7 2 30.0 0.0 7.7 0.0 6.7 150 FTG ET2R PE 0.0 4 30.0 0.0 10.4 0.0 0.068 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 10.4 0.0 0.0 150 FIG E2R PE 0.0 5 30.0 0.0 10.4 0.0 0.000 TL 22.58 PV Pipe: 5 --- - --- -------20.0- 1.101 PL -15.00--PF- _1 4 4 30.0 0.0 10.4 0.0 6.7 150 FTG T PE 6.5 6 15.0 0.0 18.3 0.0 0.068 TL 20.00 PV Pipe: 6 -20.0 1.101 PL 10.42 PF 1.5 6 15.0 0.0 18.3 0.0 6.7 150 FTG ET PE 0.0 7 15.0 0.0 19.8 0.0 0.068 TL 22.42 PV Pipe: 7 -10.9 1.101 PL 5.33 PF 0.2 7 15.0 0.0 19.8 0.0 3.7 150 FTG T PE 0.0 7A 15.0 0.0 20.0 0.0 0.022 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 20.0 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 20.0 0.0 0.000 TL 14.42 PV Pipe: 7B -10.9 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 20.0 0.0 3.7 150 FTG R PE 0.0 7C 15.0 0.0 20.1 0.0 0.022 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 20.1 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 20.1 0.0 0.000 TL 30.17 PV Pipe:7D -10.9 1.101 PL 46.08 PF 1.3 7C 15.0 0.0 20.1 0.0 3.7 150 FTG T6R PE 0.0 8 15.0 0.0 21.3 0.0 0.022 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 21.3 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 21.3 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2HD.SDF JOB TITLE: 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: 9 -10.9 1.101 PL 9.33 PF 0.3 8 15.0 0.0 21.3 0.0 3.7 150 FTG 2R PE 0.0 10 15.0 0.0 21.6 0.0 0.022 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 21.6 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 21.6 0.0 0.000 TL 20.75 PV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 21.3 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 14.8 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 14.8 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 14.8 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 14.8 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 14.8 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 14.8 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 14.8 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 14.8 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 14.8 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 14.8 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 19.2 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 19.2 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 19.2 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 19.2 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 19.2 0.0 0.000 TL 47.17. PV Pipe: 19 0.0 1.101 PL 13.50 PF 0.0 19 20.0 0.0 19.2 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 19.2 0.0 0.000. TL 32.50 PV Pipe: 20 0.0 1.101 PL 8.67 PF 0.0 19 20.0 0.0 19.2 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 19.2 0.0 0.000 TL 27.67 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 19.2 0.0 0.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 19.2 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2HD.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 19.2 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 14.8 0.0 0.000 TL 31.00 PV Pipe: 23 -10.9 1.101 PL 27.08 PF 0.8 10 15.0 0.0 21.6 0.0 3.7 150 FTG E2R PE 0.0 23 15.0 0.0 22.4 0.0 0.022 TL 36.08 PV Pipe: 24 -20.0 1.598 PL 23.58 PF 1.0 23 15.0 0.0 22.4 0.0 3.2 150 FTG 6ET PE 4.3 24 5.0 0.0 27.7 0.0 0.011 TL 85.58 PV Pipe: 25 9.1 1.101 PL 74.50 PF 1.5 23 15.0 0.0 22.4 0.0 3.1 150 FTG ETSR PE 0.0 25 15.0 0.0 20.9 0.0 0.016 TL 91.50 PV Pipe: 26 9.1 1.101 PL 16.00 PF 0.5 25 15.0 0.0 20.9 0.0 3.1 150 FTG ETR PE 0.0 25A _ 15.-0 __ 0-.0 20-.5. _-0.0- ----0-.016-TL.-_29-..00-.-PV- Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 20.5 0.0 0.0 150 FTG ET PE 0.0 25B 15.0 0.0 20.5 0.0 0.000 TL 17.50 PV Pipe: 26B 9.1 1.101 PL 7.58 PF 0.2 25A 15.0 0.0 20.5 0.0 3.1 150 FTG T2R PE 0.0 25C 15.0 0.0 20.2 0.0 0.016 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 20.2 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 20.2 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 20.2 0.0 0.0 150 FTG 2E2R PE 0.0 25E 15.0 0.0 20.2 0.0 0.000 TL 24.42 PV Pipe: 26F 9.1 1.101 PL 15.33 PF 0.4 25C 15.0 0.0 20.2 0.0 3.1 150 FTG 2T2R PE 0.0 7 15.0 0.0 19.8 0.0 0.016 TL 27.33 PV Pipe: 27 -20.0 1.598 PL 5.00 PF 0.2 24 5.0 0.0 27.7 0.0 3.2 150 FTG E PE 2.2 26 0.0 0.0 30.0 0.0 0.011 TL 14.00 PV Pipe: 28 -20.0 1.598 PL 3.50 PF 0.3 26 0.0 0.0 30.0 0.0 3.2 150 FTG 3ER PE 0.0 TR 0.0 0.0 30.3 0.0 0.011 TL 31.50 PV Pipe: 100 -20.0 1.598 PL 5.00 PF 0.2 TR 0.0 0.0 30.3 0.0 3.2 150 FTG E PE 2.2 FS -5.0 0.0 32.7 0.0 0.011 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2ED.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 35.7 0.0 3.0 psi, 20.0 gpm FS -5.0 0.0 32.7 0.0 Pipe: 102 -20.0 1.101 PL 3.00 PF 0.9 FS1 -5.0 0.0 35.7 0.0 6.7 150 FTG 2RC PE 1.3 BR -8.0 0.0 37.8 0.0 0.068 TL 13.00 PV Pipe: 103 -20.0 1.055 PL 2.00 PF 0.7 BR -8.0 0.0 37.8 0.0 7.4 150 FTG 2E PE 0.0 U1 -8.0 H.S. 38.5 5.0 0.084 TL 8.00 PV Pipe: 104 -25.0 1.025 PL 10.00 PF 1.9 U1 -8.0 H.S. 38.5 5.0 9.7 150 FTG E PE -4.3 U2 2.0 0.0 36.1 0.0 0.146 TL 13.00 PV Pipe: 105 -25.0 2.003 PL 70.00 PF 0.7 U2 2.0 0.0 36.1 0.0 2.5 150 FTG 5E PE 6.5 U3 -13.0 0.0 43.3 0.0 0.006 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 47.3 0.0 4.0 psi, 25.0 gpm U3 -13.0 0.0 43.3 0.0 Pipe: 107 -25.1 0.995 PL 10.00 PF 5.1 U4 -13.0 0.0 47.3 0.0 10.3 150 FTG TX PE 0.9 SRC -15.0 SRCE 53.2 (N/A) 0.169 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) under license no. 64623334 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 0.157 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 10.3 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2HD.SDF JOB TITLE: 70.96 psi with a flow of 31.58 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.596 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter -- ---- Equivalent-Fitting-Lengths--in-Feet -- - --- ----- - - - --- (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2HD.SDF JOB TITLE: O 0 N ei 0 0 .4 a N a O O 0 N ro N W a N w a H O w o N z r U o •, a *' a m rn " w w a w H 3 0 0 m 0 0 0 0 0 0 0 r o m 0 0 0 0 0 o r �o N C Cl)N 1 ,� o 0 4 0 0 w a PG w w w 0 0 w `" a N •ri — n a) U $4 7 0 W In () ,J .0 r-1 w a N JJ a) a a 1 O Vl .11 4J N H 0 p 0 ro 0 v u ro w w m 0 a)O N .i 10 ro to w ro W N x ro 0 0 0 0 ro ro w w iJ Vl N A 4J W ro ro u ,0 a) ro v q u I E9 w V1 N al a) R N •.+ a a v ro +1 0 •A x w N m a a o �i N al 41 0 0 z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 2HD.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I I \ I \ 60+ \ I \ I \ I \ 54+ \ x \ I \ I \ P 48+ \ R I \ E I \\ S I \ 542+ U I \ R I \ E I \ 36+ \ ( I \ P I \\ S I \ I 30+ \ I \ I I \ 24+ \ I \ I \ * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 12+ LEGEND " I" X = Required Water Supply " I 53.22 psi @ 25.1 gpm " 6+ " I 0 = Available Water Supply " I 70.97 psi @ 25.1 gpm " 0++-+---+----+-----+------+-----'--+------------------------------+ 400 600 800 1000 1200 1400. -1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS 137; MCELROY RESIDENCE 2ND FLOOR 1 HD BATH 1 CALC FILE NUMBER: 13526 DATE: NOV 10, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: NFPA 13D, 2016 EDITION 0.05 gpm/sq. ft. 225.0 sq. ft. 225.0 sq. ft. max. 1 sprinklers 12.0 gpm TOTAL WATER REQUIRED (including hose): 17.0 gpm FLOW AND PRESSURE (@ BOR): 12.0 gpm @ 33.7 psi REQUIRED PRESSURE (@ SRC): 44.7 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 1HD.SDF JOB TITLE: 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 71.0 20.0 1500.0 71.0 17.0 44.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 17.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 12.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 __ 30.0.. _ _._.-___.-_.. _11.1 2 30.0 - - - - 11.1 - - - 3 30.0 - - - - 11.1 - - - 4 30.0 - - - - 11.1 - - - 5 30.0 K= 3.70 10.5 12.0 6 15.0 - - - - 18.1 - - - 7 15.0 - - - - 18.7 - - - 7A 15.0 - - - - 18.8 - - - 7B 15.0 - - - - 18.8 - - - 7C 15.0 - - - - 18.8 - - - 7D 15.0 - - - - 18.8 - - - 8 15.0 - - - - 19.3 - - - 9 15.0 - - - - 19.3 - - - 10 15.0 - - - - 19.4 - - - 11 15.0 - - - - 19.4 - - - 12 30.0 - - - - 12.8 - - - 13 30.0 - - - - 12.8 - - - 14 30.0 - - - - 12.8 - - - 15 30.0 - - - - 12.8 - - - 16 30.0 - - - - 12.8 - - - 17 20.0 - - - - 17.2 - - - 18 20.0 - - - - 17.2 - - - 19 20.0 - - - - 17.2 - - - 20 20.0 - - - - 17.2 - - - 21 20.0 - - - - 17.2 - - - 22 20.0 - - - - 17.2 - - - 23 15.0 - - - - 19.7 - - - 24 5.0 - - - - 24.4 - - - 25 15.0 - - - - 19.2 - - - 25A 15.0 - - - - 19.0 - - - 25B 15.0 - - - - 19.0 - - - 25C 15.0 - - - - 18.9 - - - 25D 15.0 - - - - 18.9 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 11/10/2020 NEWPORT REACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 1HD.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 - - - - 18.9 - - - 26 0.0 - - - - 26.7 - - - TR 0.0 - - - - 26.8 - - - FS -5.0 - - - - 29.0 - - - FS1 -5.0 - - - - 32.0 - - - ER -8.0 - - - - 33.7 - - - U1 -8.0 HOSE STREAM 33.9 5.0 U2 2.0 - - - - 30.5 - - - U3 -13.0 - - - - 37.4 - - - U4 -13.0 - - - - 41.4 - - - SRC -15.0 SOURCE 44.7 17.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FIR - 1HD.SDF JOB TITLE: 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 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 11.1 0.0 0.0 150 FTG 2E PE 0.0 2 30.0 0.0 11.1 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 11.1 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 11.1 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 11.1 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 11.1 0.0 0.000 TL 39.67 PV Pipe: 4 12.0 1.101 PL 13.58 PF 0.6 4 30.0 0.0 11.1 0.0 4.0 150 FTG E2R PE 0.0 5 30.0 3.7 10.5 12.0 0.026 TL 22.58 PV Pipe.:.. 5__ _ ___ __.-12.0._.. 1.101_PL_._. 15.00 PF_ 0.5_.... 4 30.0 0.0 11.1 0.0 4.0 150 FTG T PE 6.5 6 15.0 0.0 18.1 0.0 0.026 TL 20.00 PV Pipe: 6 -12.0 1.101 PL 10.42 PF 0.6 6 15.0 0.0 18.1 0.0 4.0 150 FTG ET PE 0.0 7 15.0 0.0 18.7 0.0 0.026 TL 22.42 PV Pipe: 7 -6.5 1.101 PL 5.33 PF 0.1 7 15.0 0.0 18.7 0.0 2.2 150 FTG T PE 0.0 7A 15.0 0.0 18.8 0.0 0.009 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 18.8 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 18.8 0.0 0.000 TL 14.42 PV Pipe: 7B -6.5 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 18.8 0.0 2.2 150 FTG R PE 0.0 7C 15.0 0.0 18.8 0.0 0.009 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 18.8 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 18.8 0.0 0.000 TL 30.17 PV Pipe: 7D -6.5 1.101 PL 46.08 PF 0.5 7C 15.0 0.0 18.8 0.0 2.2 150 FTG T6R PE 0.0 8 15.0 0.0 19.3 0.0 0.009 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 19.3 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 19.3 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 1HD.SDF JOB TITLE: PIPE TAG 0(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: 9 -6.5 1.101 PL 9.33 PF 0.1 8 15.0 0.0 19.3 0.0 2.2 150 FTG 2R PE 0.0 10 15.0 0.0 19.4 0.0 0.009 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 19.4 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 19.4 0.0 0.000 TL 20.75 PV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 19.3 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 12.8 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 12.8 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 12.8 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 12.8 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 12.8 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 12.8 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 12.6 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 12.8 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 12.8 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 12.8 0.0 0.0 150 FTG2E PE 4.3 17 20.0 0.0 17.2 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 17.2 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 17.2 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 1B 20.0 0.0 17.2 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 17.2 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 13.50 PF 0.0 19 20.0 0.0 17.2 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 17.2 0.0 0.000 TL 32.50 PV Pipe: 20 0.0 1.101 PL 8.67 PF 0.0 19 20.0 0.0 17.2 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 17.2 0.0 0.000 TL 27.67 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 17.2 0.0 0.0 150 FTG 2E2TR PE 0.0 22 20.0 0.0 17.2 0.0 0.000 TL 39.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 1HD.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 17.2 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 12.8 0.0 0.000 TL 31.00 PV Pipe: 23 -6.5 1.101 PL 27.08 PF 0.3 10 15.0 0.0 19.4 0.0 2.2 150 FTG E2R PE 0.0 23 15.0 0.0 19.7 0.0 0.009 TL 36.08 PV Pipe: 24 -12.0 1.598 PL 23.58 PF 0.4 23 15.0 0.0 19.7 0.0 1.9 150 FTG 6ET PE 4.3 24 5.0 0.0 24.4 0.0 0.004 TL 85.58 PV Pipe: 25 5.5 1.101 PL 74.50 PF 0.6 23 15.0 0.0 19.7 0.0 1.8 150 FTG ETSR PE 0.0 25 15.0 0.0 19.2 0.0 0.006 TL 91.50 PV Pipe: 26 5.5 1.101 PL 16.00 PF 0.2 25 15.0 0.0 19.2 0.0 1.8 150 FTG ETR PE 0.0 25A 15.0. 0_0_ _19_0. 0.0_ _._ _. 0.006. _TL _.. 29.00__PY.__ Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 19.0 0.0 0.0 150 FTG ET PE 0.0 25B 15.0 0.0 19.0 0.0 0.000 TL 17.50 PV Pipe: 26B 5.5 1.101 PL 7.58 PF 0.1 25A 15.0 0.0 19.0 0.0 1.8 150 FTG T2R PE 0.0 25C 15.0 0.0 18.9 0.0 0.006 TL 14.58 PV Pipe: 26D 0.0 1.101 PL 0.50 PF 0.0 25C 15.0 0.0 18.9 0.0 0.0 150 FTG R PE 0.0 25D 15.0 0.0 18.9 0.0 0.000 TL 1.50 PV Pipe: 26E 0.0 1.101 PL 8.42 PF 0.0 25D 15.0 0.0 18.9 0.0 0.0 150 FTG 2E2R PE 0.0 25E 15.0 0.0 18.9 0.0 0.000 TL 24.42 PV Pipe: 26F 5.5 1.101 PL 15.33 PF 0.2 25C 15.0 0.0 18.9 0.0 1.8 150 FTG 2T2R PE 0.0 7 15.0 0.0 18.7 0.0 0.006 TL 27.33 PV Pipe: 27 -12.0 1.598 PL 5.00 PF 0.1 24 5.0 0.0 24.4 0.0 1.9 150 FTG E PE 2.2 26 0.0 0.0 26.7 0.0 0.004 TL 14.00 PV Pipe: 28 -12.0 1.598 PL 3.50 PF 0.1 26 0.0 0.0 26.7 0.0 1.9 150 FTG 3ER PE 0.0 TR 0.0 0.0 26.8 0.0 0.004 TL 31.50 PV Pipe: 100 -12.0 1.598 PL 5.00 PF 0.1 TR 0.0 0.0 26.8 0.0 1.9 150 FTG E PE 2.2 FS -5.0 0.0 29.0 0.0 0.004 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 1HD.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE FS1 -5.0 0.0 32.0 0.0 3.0 psi, 12.0 gpm FS -5.0 0.0 29.0 0.0 Pipe: 102 -12.0 1.101 PL 3.00 PF 0.3 FS1 -5.0 0.0 32.0 0.0 4.0 150 FIG 2RC PE 1.3 BR -8.0 0.0 33.7 0.0 0.026 TL 13.00 PV Pipe: 103 -12.0 1.055 PL 2.00 PF 0.3 BR -8.0 0.0 33.7 0.0 4.4 150 FTG 2E PE 0.0 U1 -8.0 H.S. 33.9 5.0 0.033 TL 8.00 PV Pipe: 104 -17.0 1.025 PL 10.00 PF 0.9 U1 -8.0 H.S. 33.9 5.0 6.6 150 FTG E PE -4.3 U2 2.0 0.0 30.5 0.0 0.071 TL 13.00 PV Pipe: 105 -17.0 2.003 PL 70.00 PF 0.3 U2 2.0 0.0 30.5 0.0 1.7 150 FTG 5E PE 6.5 U3 -13.0 0.0 37.4 0.0 0.003 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 41.4 0.0 4.0 psi, 17.0 gpm U3 -13.0 0.0 37.4 0.0 Pipe: 107 -17.0 0.995 PL 10.00 PF 2.5 U4 -13.0 0.0 41.4 0.0 7.0 150 FTG TX PE 0.9 SRC -15.0 SRCE 44.7 (N/A) 0.083 TL 30.00 Pv NOTES (BASS): (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) under license no. 64623334 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 0.001 gpm and a maximum imbalance at any node of 0.053 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 7.0 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 1HD.SDF JOB TITLE: 70.97 psi with a flow of 24.42 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HNC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 -. Diameter -.. _ Equivalent. Fitting_ Lengths. in Feet._.. __ (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 1HD.SDF JOB TITLE: C7 0 0 0 0 0 0 0 o <r l� t0 N -0 en N rl O I C9 4D 0w as wmNDaw--aN•.i. ro U 11 0 O N N N 43 N 7 N iu v ro a a + O N •'I N +i H U 0 �U O N u v w N w 0 N (d N ro N N 0 N ro x 0 C O O m ro N N IN N 0 A 4J $4 ro ro U •.i N ro w a si •rl p N N N W N a u •.i a a w v +J a •�I x ur N ro a a o H N w iJ O z SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\2ND FLR - 1HD.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I I \ 66+ \ I I \ I \ 60+ \ I \ I \ I \ 54+ \ I \ I \ I \ P 48+ \ R I \ E X \\ S I \ u I \ R I \ E I \ 36+ \ ( I \ P I \\ S I \ I 30+ \ I \ I \ 24+ \ I \ I \ * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 1= 12+ LEGEND " I' X = Required Water Supply " 44.71 psi @ 17.0 gpm " 6+ " I 0 = Available Water Supply " I 70.99 psi @ 17.0 gpm " 0++-+---+----+-----+------+-----'-----------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR MCELROY RESIDENCE 1ST FLOOR 2 HD GUEST SUITE CALC FILE NUMBER: 13526 DATE: NOV 10, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 450.0 sq. ft. COVERAGE PER SPRINKLER: 225.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 24.4 gpm TOTAL WATER REQUIRED (including hose): 29.4 gpm FLOW AND PRESSURE (@ BOR): 24.4 gpm @ 31.6 psi REQUIRED PRESSURE (@ SRC): 49.9 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: MAX QUINONEZ AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD.SDF JOB TITLE: 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 71.0 20.0 1500.0 71.0 29.4 49.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 29.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 24.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 5.4 - - - 2 30.0 - - -- 5.4 - - - 3 30.0 - - - - 5.4 - - - 4 30.0 - - -- 5.4 - - - 5 30.0 - - -- 5.4 - - - 6 15.0 - - - - 11.9 - - - 7 15.0 - - - - 11.9 - - - 7A 15.0 - - - - 12.2 - - - 7B 15.0 - - - - 12.2 - - - 7C 15.0 - - - - 12.2 - - - 7D 15.0 - - - - 12.2 - - - 8 15.0 - - - - 13.7 - - - 9 15.0 - - - - 13.7 - - - 10 15.0 - - - - 14.0 - - - 11 15.0 - - - - 14.0 - - - 12 30.0 - - - - 7.2 - - - 13 30.0 - - - - 7.2 - - - 14 30.0 - - - - 7.2 - - - 15 30.0 - - - - 7.2 - - - 16 30.0 - - - - 7.2 - - - 17 20.0 - - - - 11.6 - - - 18 20.0 - - - - 11.6 - - - 19 20.0 - - - - 11.6 - - - 20 20.0 - - - - 11.6 - - - 21 20.0 - - - - 11.6 - - - 22 20.0 - - - - 11.6 - - - 23 15.0 - - - - 15.0 - - - 24 5.0 - - - - 20.7 - - - 25 15.0 - - - - 12.4 - - - 25A 15.0 - - - - 11.6 - - - 25B 15.0 - - - - 11.6 - - - 25C 15.0 K= 3.70 11.2 12.4 25D 15.0 - - - - 11.2 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25E 15.0 K= 3.70 10.5 12.0 26 0.0 - - - - 23.1 - - - TR 0.0 - - - - 23.6 - - - FS -5.0 - - - - 26.0 - - - FS1 -5.0 - - - - 29.0 - - - BR -8.0 - - - - 31.6 - - - U1 -8.0 HOSE STREAM 32.5 5.0 U2 2.0 - - - - 30.7 - - - U3 -13.0 - - - - 38.2 - - - U4 -13.0 - - - - 42.2 - - - SRC -15.0 SOURCE 49.9 29.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD.SDF JOB TITLE: 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 0.0 1.101 PL 6.92 PF 0.0 1 30.0 0.0 5.4 0.0 0.0 150 FIG 2E PE 0.0 2 30.0 0.0 5.4 0.0 0.000 TL 20.92 PV Pipe: 2 0.0 1.101 PL 7.08 PF 0.0 2 30.0 0.0 5.4 0.0 0.0 150 FIG ET PE 0.0 3 30.0 0.0 5.4 0.0 0.000 TL 19.08 PV Pipe: 3 0.0 1.101 PL 25.67 PF 0.0 2 30.0 0.0 5.4 0.0 0.0 150 FTG ET2R PE 0.0 4 30.0 0.0 5.4 0.0 0.000 TL 39.67 PV Pipe: 4 0.0 1.101 PL 13.58 PF 0.0 4 30.0 0.0 5.4 0.0 0.0 150 FTG E2R PE 0.0 5 30.0 0.0 5.4 0.0 0.000 TL 22.58 PV Pipe:-5 - ------0.0 1-.101 PL -15.00 -PF-- 0.0 -- --- -- 4 30.0 0.0 5.4 0.0 0.0 150 FIG T PE 6.5 6 15.0 0.0 11.9 0.0 0.000 TL 20.00 PV Pipe: 6 0.0 1.101 PL 10.42 PF 0.0 6 15.0 0.0 11.9 0.0 0.0 150 FTG ET PE 0.0 7 15.0 0.0 11.9 0.0 0.000 TL 22.42 PV Pipe: 7 -12.0 1.101 PL 5.33 PF 0.3 7 15.0 0.0 11.9 0.0 4.0 150 FTG T PE 0.0 7A 15.0 0.0 12.2 0.0 0.026 TL 10.33 PV Pipe: 7A 0.0 1.101 PL 2.42 PF 0.0 7A 15.0 0.0 12.2 0.0 0.0 150 FTG ET PE 0.0 7B 15.0 0.0 12.2 0.0 0.000 TL 14.42 PV Pipe: 7a -12.0 1.101 PL 0.50 PF 0.0 7A 15.0 0.0 12.2 0.0 4.0 150 FIG R PE 0.0 7C 15.0 0.0 12.2 0.0 0.026 TL 1.50 PV Pipe: 7C 0.0 1.101 PL 11.17 PF 0.0 7C 15.0 0.0 12.2 0.0 0.0 150 FTG 2ET PE 0.0 7D 15.0 0.0 12.2 0.0 0.000 TL 30.17 PV Pipe: 7D -12.0 1.101 PL 46.08 PF 1.5 7C 15.0 0.0 12.2 0.0 4.0 150 FTG T6R PE 0.0 8 15.0 0.0 13.7 0.0 0.026 TL 57.08 PV Pipe: 8 0.0 1.101 PL 8.08 PF 0.0 8 15.0 0.0 13.7 0.0 0.0 150 FTG ET PE 0.0 9 15.0 0.0 13.7 0.0 0.000 TL 20.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FIR - 2HD.SDF JOB TITLE: 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: 9 -12.0 1.101 PL 9.33 PF 0.3 8 15.0 0.0 13.7 0.0 4.0 150 FTG 2R PE 0.0 10 15.0 0.0 14.0 0.0 0.026 TL 11.33 PV Pipe: 10 0.0 1.101 PL 9.75 PF 0.0 10 15.0 0.0 14.0 0.0 0.0 150 FTG 2TR PE 0.0 11 15.0 0.0 14.0 0.0 0.000 TL 20.75 PV Pipe: 11 0.0 1.101 PL 15.00 PF 0.0 9 15.0 0.0 13.7 0.0 0.0 150 FTG E PE -6.5 12 30.0 0.0 7.2 0.0 0.000 TL 22.00 PV Pipe: 12 0.0 1.101 PL 6.08 PF 0.0 12 30.0 0.0 7.2 0.0 0.0 150 FTG 2ETR PE 0.0 13 30.0 0.0 7.2 0.0 0.000 TL 26.08 PV Pipe: 13 0.0 1.101 PL 12.75 PF 0.0 12 30.0 0.0 7.2 0.0 0.0 150 FTG 2TR PE 0.0 14 30.0 0.0 7.2 0.0 0.000 TL 23.75 PV Pipe: 14 0.0 1.101 PL 0.50 PF 0.0 14 30.0 0.0 7.2 0.0 0.0 150 FTG T PE 0.0 15 30.0 0.0 7.2 0.0 0.000 TL 5.50 PV Pipe: 15 0.0 1.101 PL 9.08 PF 0.0 14 30.0 0.0 7.2 0.0 0.0 150 FTG 3T PE 0.0 16 30.0 0.0 7.2 0.0 0.000 TL 24.08 PV Pipe: 16 0.0 1.101 PL 10.00 PF 0.0 13 30.0 0.0 7.2 0.0 0.0 150 FTG 2E PE 4.3 17 20.0 0.0 11.6 0.0 0.000 TL 24.00 PV Pipe: 17 0.0 1.101 PL 18.33 PF 0.0 17 20.0 0.0 11.6 0.0 0.0 150 FTG ETR PE 0.0 18 20.0 0.0 11.6 0.0 0.000 TL 31.33 PV Pipe: 18 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 11.6 0.0 0.0 150 FTG 4ET PE 0.0 19 20.0 0.0 11.6 0.0 0.000 TL 47.17 PV Pipe: 19 0.0 1.101 PL 13.50 PF 0.0 19 20.0 0.0 11.6 0.0 0.0 150 FTG 2ET PE 0.0 20 20.0 0.0 11.6 0.0 0.000 TL 32.50 PV Pipe: 20 0.0 1.101 PL 8.67 PF 0.0 19 20.0 0.0 11.6 0.0 0.0 150 FTG 2ET PE 0.0 21 20.0 0.0 11.6 0.0 0.000 TL 27.67 PV Pipe: 21 0.0 1.101 PL 14.17 PF 0.0 18 20.0 0.0 11.6 0.0 0.0 150 FIG 2E2TR PE 0.0 22 20.0 0.0 11.6 0.0 0.000 TL 39.17 PV SPRINHLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FIR - 2HD.SDF JOB TITLE: 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: 22 0.0 1.101 PL 10.00 PF 0.0 22 20.0 0.0 11.6 0.0 0.0 150 FTG 3E PE -4.3 16 30.0 0.0 7.2 0.0 0.000 TL 31.00 PV Pipe: 23 -12.0 1.101 PL 27.08 PF 1.0 10 15.0 0.0 14.0 0.0 4.0 150 FTG E2R PE 0.0 23 15.0 0.0 15.0 0.0 0.026 TL 36.08 PV Pipe: 24 -24.4 1.598 PL 23.58 PF 1.4 23 15.0 0.0 15.0 0.0 3.9 150 FIG 6ET PE 4.3 24 5.0 0.0 20.7 0.0 0.016 TL 85.58 PV Pipe: 25 12.4 1.101 PL 74.50 PF 2.6 23 15.0 0.0 15.0 0.0 4.2 150 FTG ETSR PE 0.0 25 15.0 0.0 12.4 0.0 0.028 TL 91.50 PV Pipe: 26 12.4 1.101 PL 16.00 PF 0.8 25 15.0 0.0 12.4 0.0 4.2 150 FIG ETR PE 0.0 25A --15-.-0 0.0- - 11.6 - 0.0 -----0-.028-TL--29.00---PV ---- --- - --- -- -- Pipe: 26A 0.0 1.101 PL 5.50 PF 0.0 25A 15.0 0.0 11.6 0.0 0.0 150 FIG ET PE 0.0 25B 15.0 0.0 11.6 0.0 0.000 TL 17.50 PV Pipe: 26B 12.4 1.101 PL 7.58 PF 0.4 25A 15.0 0.0 11.6 0.0 4.2 150 FTG T2R PE 0.0 25C 15.0 3.7 11.2 12.4 0.028 TL 14.58 PV Pipe: 26D 12.0 1.101 PL 0.50 PF 0.0 25C 15.0 3.7 11.2 12.4 4.0 150 FTG R PE 0.0 25D 15.0 0.0 11.2 0.0 0.026 TL 1.50 PV Pipe: 26E 12.0 1.101 PL 8.42 PF 0.6 25D 15.0 0.0 11.2 0.0 4.0 150 FTG 2E2R PE 0.0 25E 15.0 3.7 10.5 12.0 0.026 TL 24.42 PV Pipe: 26F -12.0 1.101 PL 15.33 PF 0.7 25C 15.0 3.7 11.2 12.4 4.0 150 FTG 2T2R PE 0.0 7 15.0 0.0 11.9 0.0 0.026 TL 27.33 PV Pipe: 27 -24.4 1.598 PL 5.00 PF 0.2 24 5.0 0.0 20.7 0.0 3.9 150 FTG E PE 2.2 26 0.0 0.0 23.1 0.0 0.016 TL 14.00 PV Pipe: 28 -24.4 1.598 PL 3.50 PF 0.5 26 0.0 0.0 23.1 0.0 3.9 150 FIG 3ER PE 0.0 TR 0.0 0.0 23.6 0.0 0.016 TL 31.50 PV Pipe: 100 -24.4 1.598 PL 5.00 PF 0.2 TR 0.0 0.0 23.6 0.0 3.9 150 FIG E PE 2.2 FS -5.0 0.0 26.0 0.0 0.016 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD.SDF JOB TITLE: 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: 101 FIXED PRESSURE LOSS DEVICE PSI -5.0 0.0 29.0 0.0 3.0 psi, 24.4 gpm FS -5.0 0.0 26.0 0.0 Pipe: 102 -24.4 1.101 PL 3.00 PF 1.3 FS1 -5.0 0.0 29.0 0.0 8.2 150 FTG 2RC PE 1.3 BR -8.0 0.0 31.6 0.0 0.098 TL 13.00 PV Pipe: 103 -24.4 1.055 PL 2.00 PF 1.0 BR -8.0 0.0 31.6 0.0 9.0 150 FTG 2E PE 0.0 Ul -8.0 H.S. 32.5 5.0 0.121 TL 8.00 PV Pipe: 104 -29.4 1.025 PL 10.00 PF 2.6 Ul -8.0 H.S. 32.5 5.0 11.4 150 FIG E PE -4.3 U2 2.0 0.0 30.7 0.0 0.196 TL 13.00 PV Pipe: 105 -29.4 2.003 PL 70.00 PF 0.9 U2 2.0 0.0 30.7 0.0 3.0 150 FTG 5E PE 6.5 U3 -13.0 0.0 38.2 0.0 0.008 TL 125.00 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -13.0 0.0 42.2 0.0 4.0 psi, 29.4 gpm U3 -13.0 0.0 38.2 0.0 Pipe: 107 -29.4 0.995 PL 10.00 PF 6.8 U4 -13.0 0.0 42.2 0.0 12.1 150 FTG TX PE 0.9 SRC -15.0 SRCE 49.9 (N/A) 0.227 TL 30.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) under license no. 64623334 granted by EERS 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 0.001 gpm and a maximum imbalance at any node of 0.061 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 12.1 ft/sec at pipe 107. (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 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD.SDF JOB TITLE: 70.94 psi with a flow of 37.74 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 E1 Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee AngVly 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter _-- Equivalent Fitting Lengths -in Feet -_-- --- - -- -- _ --- _-- (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly NPTee 1.055 3.00 7.00 1.00 2.00 0.00 8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD.SDF JOB TITLE: a ti, 0 O O N rl S O '•I W .a al a 0 O 0 N v N a) a N y a H O w o N z r � U a a +' 4j a rd "J � j w w a w E 0 0 00 0 0 0 0 0 0 0 0 0 0 0 0 0 0 o r w N m m N .-1 o i 044 0w N 0 N w w0aw--P.M -H, a U $4 0 O N W W kJ A r-i JJ 0 al 11 a) m a 43 a U N a E U o ro U ai u ro W to ro 0 m N i io ro m ul ro 0 4J Wrd 0 R D o m ro 4J al w v A a w +i N m m U -H Ul ro a, q u N a) a) N q m •� a a w ro +1 v •n x w N N q A O r N SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 11/10/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\D2\1ST FLR - 2HD.SDF JOB TITLE: WATER SUPPLY CURVE 72+ 0\ I\ I \ 66+ \ I I \ I \ 60+ \ I \\ I \ I \ 54+ \ I \ I \ x \ P 48+ \ R I \ E I \\ S I \ U I \ R I \ E I \ 36+ \ ( I \ P \\ S \ I 30+ \ I \ I I \ 24+ \ I \ I \ I * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 1= 12+ LEGEND " I" I X = Required Water Supply " I 49.87 psi @ 29.4 gpm " 6+ " I 0 = Available Water Supply " I 70.96 psi @ 29.4 gpm " -+---+----+-----+------+--------+-------'+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)