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F2020-0224 - Calcs
RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 F//.nn O r O.A ^� (� / HYDRAULIC CALCULATIONS 'i/IQI�I �`QG 2 Ito 9 E OVe cofty1f FOR WEDGE HOUSE SECOND FLOOR 2HD CALC AT LIVING ROOM FILE NUMBER: 13960 DATE: APR 22, 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: 26.6 gpm TOTAL WATER REQUIRED (including hose): 31.6 qpm FLOW AND PRESSURE (@ BOR): 26.6 qpm @ 30.2 psi REQUIRED PRESSURE (@ SRC): 96.0 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: RUBI G. 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 _ _ CALC.SDF NEWPORT BEACH\FIRE SPRINKLERS\CALLS\INITIAL\2HD AT SOURCE 0.0 GPM DATE: 4/22/2020, HOSE STREAM GPM OTHER JOB TITLE: ' .0 26.6 GPM TOTAL DISCHARGE FROM WATER SUPPLY DATA NODE ANALYSIS DATA NODE TYPE - P(PSI) DSURE RESID. FLOW TAG ELEVATION TAL SOURCE STATIC @ PRESS. @ DEMAND PRESS. NODE PRESS. PRESS. (GPM) PSI) (GPM) (PSI) TAG (PSI) (PSI) 8.2 - - - 2 20.0 66.0 20.0 1500.0 66.0 31.6 46.0 SRC - - - 4 20.0 _ _ _ 14.2 AGGREGATE FLOW ANALYSIS: 31.6 GPM TOTAL FLOW AT SOURCE ALLOWANCE AT SOURCE 0.0 GPM TOTAL HOSE STREAM GPM OTHER HOSE STREAM ALLOWANCES .0 26.6 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TYPE - P(PSI) DSURE I(GPM) NODE TAG ELEVATION (FT) 20.0 K= 4.90 7.0 13.0 1 8.2 - - - 2 20.0 K= 9.90 7.7 13.6 3 20.0 _ _ 10.7 - - - 4 20.0 _ _ _ 14.2 - - - 5 20.0 - _ _ 15.0 - - - 6 20.0 - - - 15.1 - - - 7 20.0- - - 1155. 1 - - - 8 20.0 - - - .1 - - - 9 20.0 - - - 21.4 - - - 10 10.0 - - - 21.4 - - - 11 10.0 - - - 21.0 - - - 12 10.0 - - - 20.0 - - - 13 10.0 - - - 19.7 - - - 14 10.0 - - - 21.7 - - - TR 10.0 _ _ - _ 24.4 FS 5.0 _ _ -- _ 27.4 _ _ _ FSI 5.0 - - - 30.2 _ - _ BR 2.0 2.0 - - - HOSE STREAM 333. 5.0 U1 - 33.0 U2 -2.0 - - - - - 34.2 - - - U3 -3.0 - - 38.2 - - - -3.0 -4.0 SOURCE 46.0 31.6 SRC SPRINKLER SYSTEM HYDRAULIC ANALYSIS...___ Page 3 9,: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF JB 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 -13.0 1.101 PL 15.33 PF 1.2 1 20.0 4.9 7.0 13.0 4.4 150 FTG 2F3E PE 0.0 2 20.0 0.0 8.2 0.0 0.031 TL 38.33 PV Pipe: 2 - - 13.6 1.101 PL .1.58 PF 0.5 2 20.0 0.0 8.2 0.0. 4.6 - 150 FTG 2FET -PE 0.0 3 20.0 4.9 7.7 13.6 0.033 TL 15.58 PV Pipe: 3 -26.6 1.101 PL 13.00 PF 2.5 2 20.0 0.0 8.2 0.0 9.0 150 FTG 2FT2R PE 0.0 4 20.0 0.0 10.7 0.0 0.115 TL 22.00 PV Pipe: 4 -26.6 1.101 PL 7.00 PF 3.5 4 .20.0 0.0 10.7 0.0 9.0 150 FTG 2F3E PE 0.0 5 20.0 0.0 14.2 0.0 0.115 TL 30.00 PV Pipe: 5 -9.2 1.101 PL 15.33 PF 0.8 5 20.0 0.0 14.2 0.0 3.1 150 FTG 3E2T2R PE 0.0 6 20.0 0.0 15.0 0.0 0.016 TL 48.33 PV Pipe: 6 -17.4 1.101 PL 15.00 PF 0.9 5 20.0 0.0 14.2 0.0 5.9 150 FTG 2FR PE 0.0 7 20.0 0.0 15.1 0.0 0.052 TL 18.00 PV Pipe: 7 0.0 1.101 PL 6.16 PF 0.0 7 20.0 0.0 15.1 0.0 0.0 150 FTG 2F2ETR PE 0.0 8 20.0 0.0 15.1 0.0 0.000 TL 28.16 PV Pipe: 8 -17.4 1.394 PL 30.00 PF 1.6 7 20.0 0.0 15.1 0.0 3.7 150 FTG 4F6ET3R PE 0.0 9 20.0 0.0 16.7 0.0 0.017 TL 95.00 PV Pipe: 9 -17.4 1.394 PL 10.00 PF 0.3 9 20.0 0.0 16.7 0.0 3.7 150 FTG E PE 4.3 10 10.0 0.0 21.4 0.0 0.017 TL 18.00 PV Pipe: 10 -5.7 1.394 PL 14.00 PF 0.1 10 10.0 0.0 21.4 0.0 1.2 150 FTG 2FTR PE 0.0 11 10.0 0.0 21.4 0.0 0.002 TL 25.00 PV Pipe: 11 9.2 1.394 PL 22.50 PF 0.4 11 10.0 0.0 21.4 0.0 1.9 150 FTG 2F4E2TR PE 0.0 12 10.0 0.0 21.0. 0.0 0,005 TL 71.50 PV Pipe: 12 9.2 1.101 PL 17.33 PF 1.0 12 10.0 0.0 21.0 0.0 3.1 150 FTG 2F5ET3R PE 0.0 13 10.0 0.0 20.0 0.0 0.016 TL 62.33 PV SPRINKLERS SYSTEM HYDRAULIC ANALYSIS- -- Page 4 DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.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: 13 9.2 1.101 PL 3.33 PF 0.4 13 10.0 0.0 20.0 0.0 3.1 150 FTG 2ET PE 0.0 14 10.0 0.0 19.7 0.0 0.016 TL 22.33 PV Pipe: 14 9.2. 1.101 PL 10.00 PF 0.4 14 10.0 0.0 19.7 0.0 3.1 150 FTG ET PE -4.3 6 20.0 0.0 15.0 0.0. 0.016 TL 22.00 PV Pipe: 15 -11.7 1.394 PL 21.25 PF 0.4 10 10.0 0.0 21.4 0.0 2.5 150 FTG 2F3T2R PE 0.0 TR 10.0 0.0 21.7 0.0 0.008 TL 45.25 PV Pipe: 16 14.9 1.394 PL 9.66 PF 0.3 TR 10.0 0.0 21.7 0.0 3.1 150 FTG ETR PE 0.0 11 10.0 0.0 21.4 0.0 0.013 TL 24.66 PV Pipe: 100 -26.6 1.394 PL 5.00 PF 0.5. TR 10.0 0.0 21.7 0.0 5.6 150 FTG ER PE 2.2 FS 5.0 0.0 24.4 0.0 0.037 TL 14.00 PV Pipe: 101 FIXED PRESSURE LOSS DEVICE FBI 5.0 0.0 27.4 0.0 3.0 psi, 26.6 gpm FS 5.0 0.0 24.4 0.0 Pipe: 102 -26.6 1.101 PL 4.00 PF 1.5 FSl 5.0 0.0 27.4 0.0 9.0 150 FTG RC PE 1.3 BR 2.0 0.0 30.2 0.0 0.115 TL 13.00 PV Pipe: 103 -26.6 1.055 PL 3.00 PF 0.9 BR 2.0 0.0 30.2 0.0 9.8 150 FTG E PE 0.0 U1 2.0 H.S. 31.0 5.0 0.142 TL 6.00 PV Pipe: 104 -31.6 1.985 PL 4.00 PF 0.2 Ul 2.0 H.S. 31.0 5.0 3.3 150 FTG ET PE 1.7 U2 -2.0 0.0 33.0 0.0 0.009 TL 22.00 PV Pipe: 105 -31.6 2.003 PL 63.75 PF 0.8 U2 -2.0 0.0 33.0 0.0 3.2 150 FTG 3E PE 0.4 U3 -3.0 0.0 34.2 0.0 0.009 TL 96.75 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -3.0 0.0 38.2 0.0 4.0 psi, 31.6 gpm U3 -3.0 0.0 34.2 0.0 Pipe: 107 -31,6 0.995 PL 8.25 PF 7.3 U4 -3.0 0.0 38.2 0.0 13.0 150 FTG TX PE 0.4 SRC -4.0 SRCE 46.0 (N/A) 0.259 TL 28.25 PV SPRINKLER.. SYSTEM. HYDRAULIC .ANALYSIS --- DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF JOB TITLE: 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 0.065 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 65.94 psi with a flow of 40.58 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 11.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.394 2.00 S.00 6.00 1.00 1.00 11.00 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 1.985 6.00 12.00 2.00 4.00 0.50 14.00 1.00 12.00 - - - -- SPRINKLER SYSTEM HYDRAULIC ANALYSIS-- -...... Page 6 - DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF JOB TITLE: 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.7 DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF JOB TITLE: c c c u F M i 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 rl p� r 1p N d' M N r1 O 01C4m0 41 as W W MMM W N u T 0 N m N +� G rl +� UI Fa a ro G o w m .,1 v 41 H U H 'd O OJ SA 'O W UI N N N J ttl ro N O 0 0 0 +1 G ro � � G a o 0 O P. rd -0 S j N O ro .a k ro Ga N A v ro N u m ro U d H a4 C a) N N C 31 a ro -H 0 m rtl C q O rl N N 0 O z -- - --- -- --- - - SPRINKLER SYSTEM HYDRAULIC_ ANALYSIS Page 6 _.. '. DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF JOB TITLE: WATER SUPPLY CURVE 72+ I I 660\ I \ I \ I \ 60+ \\ - I \ I \ I \ 54+ \\ I \ I \ I \ P 48+ \ R X \\ E \ S \ S 42+ \ U \\ R \ E \ 36+ \ ( I \ P \\ S \ I 30+ \ I \ I \\ I \ 24+ \ I \ I \ * <-20.0 psi @ 1500 gpm 18+ Flow Test Point I I 12+ LEGEND " X = Required Water Supply " 46.00 psi @ 31.6 gpm 6+ " 0 = Available Water Supply " 65.96 psi @ 31.6 gpm I " -+---*---------------------------------------------------------- 400 ---+-----+------+-------+-----+-------+-----------+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 WEDGE HOUSE SECOND FLOOR 1HD CALC AT BEDROOM 2 FILE NUMBER: 13460 DATE: APR 22, 2020 -DESIGN DATA- .00CUPANCY CLASSIFICATION: - NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. £t. AREA OF APPLICATION: 400.0 sq. ft. COVERAGE: PER SPRINKLER: 400.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 1 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 21.0 gpm TOTAL WATER REQUIRED (including hose): 26.0 gpm FLOW AND PRESSURE (@ BOR): 21.0 gpm @ 34.2 psi REQUIRED PRESSURE (@ SRC): 47.2 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. -- -- --------- SPRINKLER SYSTEM HYDRAULIC ANALYSIS I___. - Page - 2 ----.- DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\lHD CALC.SDF JOB TITLE: GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 21.0 WATER SUPPLY DATA NODE ANALYSIS DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ 1 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 66.0 20.0 1500.0 66.0 26.0 47.2 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 26.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 21.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI)..,. ..:.(GPM) 1 20.0 - - - - 20.6 - - - 2 20.0 - - - - 20.6 - - - 3 20.0 - - - - 20.6 - - - 4 20.0 - - - - 20.6 - - - 5 20.0 - - - - 20.6 - - - 6 20.0 - - - - 21.0 - - - 7 20.0 - - - - 20.5 - - - 8 20.0 K= 4.90 18.4 21.0 9 20.0 - - - - 21.7 - - - 10 10.0 - - - - 26.2 - - - 11 10.0 - - - - 26.3 - - - 12 10.0 - - - - 26.1 - - - 13 10.0 - - - - 25.6 - - - 14 10.0 - - - - 25.5 - - - TR 10.0 - - - - 26.5 - - - FS 5.0 - - - - 29.0 - - - FS1 5.0 - - - - 32.0 - - - BR 2.0 - - - - 34.2 - - - Ul 2.0 HOSE STREAM 34.8 5.0 U2 -2.0 - - - - 36.6 - - - U3 -3.0 - - - - 37.7 - - - U4 -3.0 - - - - 41.7 - - - SRC -4.0 SOURCE 47.2 26.0 -- SPRINKLER SYSTEM .HYDRAULIC ANALYSIS..._.. __...-._ _Page 3 DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1HD CALC.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 15.33 PF 0.0 1 20.0 0.0 20.6 0.0 0.0 150 FTG 2F3E PE 0.0 2 20.0 0.0 20.6 0.0 0.000 TL 38.33 PV Pipe: 2 0.0 1.101 PL 1.58 PF 0.0 2 20.0 0.0 20.6 0.0 0.0 150 FTG 2FET PE 0.0 3 20.0 0.0 .20.6 0.0 0.000 TL 15.58 PV Pipe: 3 0.0 1.101 PL 13.00 PF 0.0 2 20.0 0.0 20.6 0.0 0.0 150 FTG 2FT2R PE 0.0 4 20.0 0.0 20.6 0.0 0.000 TL 22.00 PV Pipe: 4 0.0 1.101 PL 7.00 PF 0.0 4 20.0 0.0 20.6 0.0 0.0 150 FTG 2F3E PE 0.0 5- 20.0 0._0 20.6 0..0 0.000. TL_ 30..00 PV _ Pipe: 5 -6.1� 1.101 PL 15.33 PF 0.4 5 20.0 0.0 20.6 0.0 2.0 150 FTG 3E2T2R PE 0.0 6 20.0 0.0 21.0 0.0 0.007 TL 48.33 PV Pipe: 6 6.1 1.101 PL 15.00 PF 0.1 5 20.0 0.0 20.6 0.0 2.0 150 FTG 2FR PE 0.0 7 20.0 0.0 20.5 0.0 0.007 TL 18.00 PV Pipe: 7 21.0 1.101 PL 6.16 PF 2.1 7 20.0 0.0 20.5 0.0 7.1 150 FTG 2F2ETR PE 0.0 8 20.0 4.9 18.4 21.0 0.074 TL 28.16 PV Pipe: 8 -14.9 1.394 PL 30.00 PF 1.2 7 20.0 0.0 20.5 0.0 3.1 150 FTG 4F6ET3R PE 0.0 9 20.0 0.0 21.7 0.0 0.013 TL 95.00 PV Pipe: 9 -14.9 1.394 PL 10.00 PF 0.2 9 20.0 0.0 21.7 0.0 3.1 150 FTG E PE 4.3 10 10.0 0.0 26.2 0.0 0.013 TL 18.00 PV Pipe: 10 -5.5 1.394 PL 14.00 PF 0.0 10 10.0 0.0 26.2 0.0 1.2 150 FTG 2FTR PE 0.0 11 10.0 0.0 26.3 0.0 0.002 TL 25.00 PV Pipe: 11 6.1. 1.394 PL 22.50 PF 0.2 11 10.0 0.0 26.3 0.0 1.3 150 FTG 2F4E2TR PE 0.0 12 10.0 0.0 26.1 0.0 :.0.002 TL. 71.50 PV Pipe: 12 6.1 1.101 PL 17.33 PF 0.5 12 10.0 0.0 26.1 0.0 2.0 150 FTG 2F5ET3R PE 0.0 13 10.0 0.0 25.6 0.0 0.007 TL 62.33 PV --- ---SPRINKLER SYSTEM HYDRAULIC ANALYSIS- _- page A --- DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALLS\INITIAL\1HD CALC.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: 13 6.1 1.101 PL 3.33 PF 0.2 13 10.0 0.0 25.6 0.0 2.0 150 FTG 2ET PE 0.0 14 10.0 0.0 25.5 0.0 0.007 TL 22.33 PV Pipe: 14 6.1, 1.101 PL 10.00 PF 0.2 14 10.0 0.0 25.5 0.0 2.0: 150 FTG ET PE -4.3 6, 20.0 0.0 21.0 0.0 0.007 TL 22.00 PV Pipe: 15 -9.4.. 1.394 PL 21.25 PF 0.2 10 10.0 0.0 26.2 0.0 2.0 150 FTG 2F3T2R PE 0.0 TR 10.0 0.0 26.5 0.0 0.005 TL 45.25 PV Pipe: 16 11.6 1.394 PL 9.66 PF 0.2 TR 10.0 0.0 26.5 0.0 2.4 150 FTG ETR PE 0.0 11 10.0 0.0 26.3 0.0 0.008 TL 24.66 PV Pipe: 100, -21.0. 1.394 PL 5.00 PF 0.3 TR 10.0 0.0 26.5 0.0 4.4 150 FTG ER PE 2.2 FS - 5.0 0.0 29.0 0.0 0.024 TL 14.00 PV Pipe: 101 FIXED PRESSURE LOSS DEVICE FS1 5.0 0.0 32.0 0.0 3.0 psi, 21.0 gpm FS 5.0 0.0 29.0 0.0 Pipe: 102 -21.0 1.101 PL 4.00 PF 1.0 FS1 5.0 0.0 32.0 0.0 7.1 150 FTG RC PE 1.3 BR 2.0 0.0 34.2 0.0 0.074 TL 13.00 PV Pipe: 103 -21.0 1.055 PL 3.00 PF 0.5 BR 2.0 0.0 34.2 0.0 7.7 150 FTG E PE 0.0 U1 2.0 H.S. 34.8 5.0 0.092 TL 6.00 PV Pipe: 104 -26.0 1.985 PL 4.00 PF 0.1 Ul 2.0 H.S. 34.8 5.0 2.7 150 FTG ET PE 1.7 U2 -2.0 0.0 36.6 0.0 0.006 TL 22.00 PV Pipe: 105 -26.0 2.003 PL 63.75 PF 0.6 U2 -2.0 0.0 36.6 0.0 2.6 150 FTG 3E PE 0.4 U3 -3.0 0.0 37.7 0.0 0.006 TL 96.75 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -3.0 0.0 41.7 0.0 4.0 psi, 26.0 gpm U3 -3.0 0.0 37.7 0.0 Pipe:- 107 -26.0 0.995 PL 8.25 PF 5.1 U4 -3.0 0.0 41.7 0.0 10.7 150 FTG TX PE 0.4 SRC -4.0 SRCE 47.2 (N/A) 0.181 TL 28.25 PV - SPRINKLER SYSTEM HYDRAULIC. ANALYSIS ___Page 5- _ -- /22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1HD CALC.SDF :TLE: �S (HASS): '(1) Calculations wereerformed b% P } 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 0.006 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 10.7 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 65.96 psi with a flow of 32.21 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 E1 Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.394 2.00 8.00 6.00 1.00 1.00 11.00 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 1.985 6.00 12.00 2.00 4.00 0.50 14.00 1.00 12.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS ---- ------Page-6 DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1HD CALC.SDF JOB TITLE: 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 7 _. _..._ .. DATE: 4/22/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1HD CALC.SDF JOB TIT" I O O O O C m N O O O a w a a w N N a a w a m. SPRI KLER RAULIC ANALYSIS DATE: 4/22/2020, NEWPORT NBEACH\FIREMSPRIDNKLERS\CALLS\INITIAL\1HD CALC.geF - -Page 8 JOB TITLE: ' WATER SUPPLY CURVE 72+ I I 660\ I \ I \ I \ 60+ I \ I \ I \ 54+ \\ I \ I \ I \ P 48+ \ R X E \ S \ S 42+ \ U \\ R E 36+ ( I \ P \\ S I 30+ \ I \ I \\ 24+ \ I \ I \ 18+ x-20.0 psi @ 1500 gpm Flow Test Point I 12+ LEGEND I „ X = Required Water Supply 147.20 psi @ 26.0 gpm 6+ 0 = Available Water Supply 65.97 psi @ 26.0 gpm I„ 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 WEDGE HOUSE SECOND FLOOR 2HD CALC AT LIVING ROOM FILE NUMBER: 13460 DATE: MAY 27, 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. £t. max. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 26.4 qpm TOTAL WATER REQUIRED (including hose): 31.4 gpm FLOW AND PRESSURE (@ BOR): 26.4 qpm @ 32.6 psi REQUIRED PRESSURE (@ SRC): 48.3 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE SPRINKLER SYSTEM - __-DR HYDRAULIC ANALYSIS Page 2 4 DATE: 5/27/2020, NEWPORT BEACH\FIRE HOSE STREAM ALLOWANCES SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF JOB TITLE: DISCHARGE FROM ACTIVE SPRINKLERS 26.4 GPM 20.0 K= 4.90 7.0 WATER SUPPLY DATA 20.0 - - - - 7.9 - - - 3 SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 66.0 20.0 1500.0 66.0 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 20.0 K= 4.90 7.0 13.0 2 20.0 - - - - 7.9 - - - 3 20.0 K= 4.90 7.4 13.4 4 20.0 - - - - 10.4 - - - 5 20.0 - - - - 15.7 - - - 6 20.0 - - - - 16.4 - - - 7 20.0 - - - - 16.7 - - - 8 20.0 - - - - 16.7 - - - 9 20.0 - - - - 18.3 - - - 10 10.0 - - - - 22.9 - - - 11 10.0 - - - - - 23.3 - - - 12 10.0 - - - - 23.0 - - - 13 10.0 - - - - 21.3 - - - 14 10.0 - - - - 21.1 - - - TR 10.0 - - - - 24.2 - - - FS 5.0 - - - - 26.8 - - - FS1 5.0 - - - - 29.8 - - - BR 2.0 - - - - 32.6 - - - U1 2.0 HOSE STREAM 33.4 5.0 U2 -2.0 - - - - 35.3 - - - U3 -3.0 - - - - 36.6 - - - U4 -3.0 - - - - 40.6 - - - SRC -4.0 SOURCE. 48.3 31.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS page 3 ,27/2020 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL.\2HD, CALC.SDF /fLE: �'E 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 -13.0 1.101 PL 13.00 PF 0.9 1 20.0 4.9 7.0 13.0 4.4 150 FTG 2F2E PE 0.0 2 20.0 0.0 7.9 0.0 0.031 TL 29.00 PV Pipe: 2 13.4 1.101 PL 1.00 PF 0.5 2 '-20.0 0.0 7.9 0.0 4.5 150 FIG 2FET. PE 0.0 3 20.0 4.9 7.4 13..4. 0.032 TL 15.00 PV Pipe: 3 -26.4 1.101 PL 13.08 PF 2.5 2 20.0 0.0 7.9 0.0 8.9 150 FTG 2FT2R PE 0.0 4 20.0 0.0 10.4 0.0 0.113 TL 22.08 PV Pipe: 4 -26.4 1.101 PL 9.16 PF 5.2 4 20.0 0.0 10.4 0.0 8.9 150 FTG 2F5E PE 0.0 5 20.0 0.0 15.7 0,.0, 0.113. TL 46.16 PV Pipe: 5 -9.1 1.101 PL 14.42 PF 0.7 5 20.0 0.0 15.7 0.0 3.1 150 FTG 2E3TR PE 0.0 6 20.0 0.0 16.4 0.0 0.016 TL 44.42 PV Pipe: 6 -17.2 1.101 PL 15.25 PF 1.0 5 20.0 0.0 15.7 0.0 5.8 150 FTG 2F3R PE 0.0 7 20.0 0.0 16.7 0.0 0.052 TL 20.25 PV Pipe: 7 0.0 1.101 PL 5.08 PF 0.0 7 20.0 0.0 16.7 0.0 0.0 150 FTG 2FET PE 0.0 8 20.0 0.0 16.7 0.0 0.000 TL 19.08 PV Pipe: 8 -17.2 1.394 PL 30.50 PF 1.6 7 20.0 0.0 16.7 0.0 3.6 150 FTG 4F5E3TR PE 0.0 9 20.0 0.0 18.3 0.0 0.016 TL 97.50 PV Pipe: 9 -17.2 1.394 PL 10.00 PF 0.3 9 20.0 0.0 18.3 0.0 3.6 150 FTG T PE 4.3 10 10.0 0.0 22.9 0.0 0.016 TL 16.00 PV Pipe: 10 -17.2 1.394 PL 14.00 PF 0.4 10 10.0 0.0 22.9 0.0 3.6 150 FTG 2FTR PE 0.0 11 10.0 0.0 23.3 0.0 0.016 TL 25.00 PV Pipe: li 9.1 .1.394 PL 23.50 PF 0.4 11 10.0 0.0 23.3 0.0 1.9 150 FTG 2F4E2TR PE 0.0 12 10.0 0.0 23.0 0.0 0.005 TL 72.50 PV Pipe: 12 9.1 1.101 PL 45.00 PF 1.6 12 10.0 0.0 23.0 0.0 3.1 150 FTG 6F5E3TR PE 0.0 13 10.0 0.0 21.3 0.0 0.016 TL 102.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS. Page 9. DATE: 5/27/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. \� A END ELEV. NOZ. PT DISC. VEL (FPS) SUM. FL/FT (FT) (PSI) � NODES (FT) (K) (PSI) (GPM) -- - - Pipe: 13 9.1 1.101 PL 3.33 PF 0.2 �l 13 10.0 0.0 21.3 0.0 3.1 150 FTG ET PE 0.0 I 14 10.0 0.0 21.1 0.0 0.016 TL 15.33 PV ) Pipe: 14 9.1. 1.101 PL 10.00 PF 0.4 14 10.0 0.0 21.1 0.0 3.1 150 FTG 2E PE -4.3 6 20.0 0.0 16.4 0.0 0.016 TL 24.00 PV Pipe: 16 -26.4 1.394 PL 9.66 PF 0.9 11 10.0 0.0 23.3 0.0 5.5 150 0.036 TL 24E 66 PV TR RE 0.0 TR 10.0 0.0 24.2 0.0 Pipe: 100 -26.4 1.394 PL 5.00 PF 0.4 TR 10.0 0.0 29.2 0.0 5.5 150 FTG TR PE 2.2 FS 5.0 0.0 26.8 0.0 0.036 TL 12.00 PV Pipe: 1.01 .FIXED PRESSURE LOSS DEVICE FS1 5.0 0.0 29.8 0.0 3.0 psi, 26.4 gpm FS 5.0 0.0 26.6 0.0 Pipe: 102 -26.4 1.101 PL 4.00 PF 1.5 FSI 5.0 0.0 29.6 0.0 8.9 150 0.119 TL RC PF 13.00 PV 1.3 BR 2.0 0.0 32.6 0.0 Pipe: 103 -26.4 1.055 PL 3.00 PF 0.8 gg 2.0 0.0 32.6 0.0 9.7 150 FTG E BE 0:0 U1 2.0 H.S. 33.4 5.0 0.140 TL 6.00 PV Pipe: 104 -31.4 1.985 PL 4.00 PF 0.2 U1 2.0 H.S. 33.9 5.0 3.3 150 FTG ET PE 1.7 02 -2.0 0.0 35.3 0.0 0.009 TL 22.00 PV Pipe: 105 -31.4 2.003 PL 63.75 PF 0.8 U2 -2.0 0.0 35.3 0.0 3.2 150 FTG 3E PE 0.4 U3 -3.0 0.0 36.6 0.0 0.008 TL 96.75 PV Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -3.0 0.0 40.6 0.0 4.0 psi, 31.4 gpm U3 -3.0 0.0 36.6 0.0 Pipe: 107 -31.4 0.995 PL 8.25 PF 7.2 U4 -3.0 0.0 40.6 0.0 12.9 150 0.256 TL TX BE 28.25 PV 0.4 SRC -4.0 SRCE 48.3 (N/A) _ SPRINKLER SYSTEM HYDRAULIC ANALYSIS -2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF ,'(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 providean average imbalance at each node of 0.001 gp um imbalance at any node of 0.010gpm- (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 12.9 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 65.95 psi with a flow of 38.83 gpm• (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Lengths in Feet Diameter Equivalent Fitting G (in) F E T R K E1 Tee RunT Kplg ChkVly Gate 95 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.101 8.00 6.00 1.00 1.00 11.00 3.00 1.394 2.00 11.00 10.00 1.00 1.00 17.00 3.00 2.003 2.00 PAGE: K MATERIAL: CT -K HWC: 150 Lengths in Feet Diameter Equivalent Fitting C G N X (in) E T F R K 45 -Ell TeeRun Kouplg ChkVly GatVly NPTee AngV v Ell Tee 2.00 0.00 6.00 0.00 6.00 14.00 0.995 2.00 6.00 1.00 PAGE: L MATERIAL: CT -L HWC: 150 Lengths -in--Feet Diameter Equivalent Fitting G N (in) E T F R X 95-E11 TeeRun Kouplg ChkVly GatVly N2Tee E11 Tee 4.00 0.50 19.00 1.00 12.00 1.985 6.00 12.00 2.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS DATE: 5/27/2020, NEWBEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDFPage 6 JOB TITLE: PAGE: M MATERIAL: CT -M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G Ell Tee 45 -Ell TeeRun Koupig 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 ?0, NEWPORT. BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF7 o 0 o r 0 0 • w C o 0 0 o m M N ti O N �a� �w wawm� maw am-� - _-- Page 8 6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS ---. DATE: 5/27/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\2HD CALC.SDF - - -- JOB TITLE: - - WATER SUPPLY CURVE 72+ I I I 660\ \ I \ I \ I \ 60+ \\ - I \ I \ I \ 54+ \\ I \ I \ I \ P 48X \ R \\ E \ S \ S 42+ \ U \\ R \ E \ 36+ \ ( I \ P \\ S \ 130+ \ I \ I \\ I \ 24+ \ I \ * <-20.0 psi @ 1500 gpm Flow Test Point 18+ I 12+ LEGEND X = Required Water Supply -.- ----- 48.26 psi @ 31.4 gpm -- -- 6+ 0 = Available Water Supply 65.96 psi @ 31.4 gpm +------+--------+-------- +---------+-----------+ 0++-+---+----+----- 2000 O(GPM) 400 600 800 1000 1200 F1400 1600 1800 RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR WEDGE HOUSE SECOND FLOOR 1HD CALC AT BEDROOM 2 FILE NUMBER: 13460 DATE: MAY 27, 2020 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION DENSITY: 0.05 gpm/sq. ft. AREA OF APPLICATION: 400.0 sq. £t. COVERAGE PER SPRINKLER: 400.0 -sq. £t. max. NUMBER OF SPRINKLERS CALCULATED: 1 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 21.0 gpm TOTAL WATER REQUIRED (including hose): 26.0 gpm FLOW AND PRESSURE (@ BOR): 21.0 gpm @ 39.2 psi REQUIRED PRESSURE (@ SRC): 47.1 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. - DATE:.. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2.. 5./27/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1HD CALC.SDF _. JOB TITLE: GPM TOTAL FLOW AT SOURCE 0.0 - WATER SUPPLY DATA (FT) OTHER - D.0 SOURCE STATIC NODE PRESS. TAG (PSI) RESID. PRESS. (PSI) FLOW @ (GPM) AVAIL. PRESS -.-:.@.DEMAND (PSI) TOTAL - (GPM) PRESD. (PSI) SRC 66.0 20.0 1500.0 66.0 26.0 47.1 AGGREGATE FLOW ANALYSIS: NODE ANALYSIS DATA 26.0 GPM TOTAL FLOW AT SOURCE 0.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE (FT) OTHER HOSE STREAM ALLOWANCES D.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 21.0 GPM NODE ANALYSIS DATA TYPE PRESSURE DISCHARGE NODE TAG ELEVATION NODE (PSI) (GPM). (FT) 1 20.0 - - - - 19.9 - 20.0 - - - - 19.9 - - 2 - 19.9 - - - 3 20.0 - - - - 4 20.0 - - - - 19.9 - - 5 20.0 - - - - 19.9 - - - - 6 20.0 - - - - 20.3 - - 7 20.0 - - - - 19.8 18.4 - - - 21.0 8 20.0 K= 4.90 9 20.0 - - - - 21.0 10 10.0 - - - - 25.5 - - - 11 10.0 - - - - 25.9 - - - 12 10.0 - - - - 25.7 - - - 13 10.0 - - - - 24.9 - - - - 14 10.0 - - - - 24.8 - - - TR 10.0 - - - - 26.4 - - FS 5.0 - - - - 28.9 - - - FSI 5.0 - - - - 31.9 - - - BR 2.0 - - - - 34.2 - - - 5.0 U1 2.0 HOSE STREAM 34.7 U2 -2.0 - - - - 36.6 - - - U3 -3.0 - - - - 37.6 - - - -3.0 - - - - 41.6 - - - U4 SOURCE 47.1 26.0 SRC -4.0 SPRINKLER. SYSTEM HYDRAULIC ANALYSIS Page /2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\lHD CALC.SDF3 dTA iTAG END Q(GPM) DIA(IN) LENGTH PRESS. ELEV NODES M. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.101 PL 13.00 PF 0.0 1 20.0 0.0 19.9 0.0 0.0 150 FTG 2F2E PE 0.0 2 20.0 0.0 19.9 0.0 0.000 TL 29.00 PV Pipe: 2. 0.0 1.101 PL 1.00 PF 0.0 2 20:0 0.0 19.9 0.0 0.0 150 FTG 2FET HE 0.0 3.. 20.0 0.0 19.9 0.0 0.000 TL 15.00 -PV 2 Pipe: 3 0.0 1.101 PL 13.08 PF 0.0 20.0 0.0 19.9 0.0 0.0 150 FTG 2FT2R PE 0.0 4 20.0 0.0 19.9 0.0 0.000 TL 22.08 PV 4 Pipe: 4 0.0 1.101 PL 9.16 PF 0.0 5 20.0 0.0 19..9 0.0 0.0 150 FTG 2F5E PE 0.0 20.0 0.0 19.9 0.0 --.. ..0.000 TL .96,16 PV Pipe: 5 5 -6.1 1.101 PL 14.42 PF 0.3 20.0 0.0 19.9 0.0 2.1 150 FTG 2E3TR PE 0.0 6 20.0 0.0 20.3 0.0 0.008 TL 49.42 PV Pipe. 6 6.1 1.101 PL 15.25 PF 0.2 5 20.0 0.0 19.9 0.0 2.1 7 150 FTG 2F3R PE 0.0 20.0 0.0 19.8 0.0 0-.008 TL 20.25 PV 7 Pipe: 7 21.0 1.101 PL 5.08 PF 1.4 20.0 0.0 19.8 0.0 7.1 8 20.0 4.9 18.4 21.0 150 FTG 2FET HE 0.0 0.079 TL 19.0$ pV ' 7 Pipe: 8 -14.9 1.394 PL 30.50 PF 1.2 20.0 0.0 19.8 0.0 3.1 9 150 FTG 9F5E3TR PE 0.0 20.0 0.0 21.0 0.0 0.013 TL 97.50 PV Pipe: 9 9 -14.9 1.394 PL 10.00 PF 0.2 20.0 0.0 21.0 0.0 3.1 150 FTG 10 10.0 0.0 25.50.0 T PE 4.3 0.013 TL 16.00 PV 10 Pipe: 10 -14.9 1.394 PL 14.00 PF 0.3 10.0 0.0 25.5 0.0 3.1 150 FTG 2FTR PE 0.0 11 10.0 0.0 25.9 0.0 - 0.013 TL 25.00 PV Pipe: 11 394 PL 23.50 11 10.0 0.0 25.9 0.0 1.3 1.150 FTG 2F4E2TRPFPE 0 0.0 12 10.0 0.0 25.7 0.0 0.002 TL 72.50 PV 12 Pipe: 12 6.1 1.101 PL 45.00 PF 10.0 0.0 25.7 0.8 0.0 2.1 150 FTG 6F5E3TR PE 0.0 13 10.0 0.0 24.9 0.0 0.008 TL 102.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page -4- DATE: NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1HD CALC.SDF _ -5/27 /2020, _ JOB TITLE: " PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS END ELEV. NOZ. PT DISC. VEL (FPS) FL/FT (FT) SUM(PSI). NODES (FT) (K) (PSI) (GPM) -. 6.1 1.101 PL 3.33 PF 0.1-. Pipe: 10.0 0.0 24.9 0.0 2.1 150 FTG ET PE 0.0 13 14 10.0 0.0 29.8 0.0 0.008 TL 15.33 PV Pipe: 14 6.1 1.101 PL 10.00 PF 0.2 0 2150 2E pE 14 10.0 0.0 29.8 0..1; 0.008 TL G -9.3 24.00 PV 6 20.0 0.0 20.3 0.0 -21.0 1.394 PL 9.66 PF 0.6 Pipe: 16 11 10.0 0.0 25.9 0.0 4.4 0.024 TL 24E 66 PV 0.0 TR 10.0 0.0 26.4 0.0 -21.0 1.394 PL 5.00 PF 0.3 Pipe: 100 TR 10.0 0.0 26.4 0.0 4.4 150 0.024 TL 12.00 PV 2.2 FS 5.0 0.0 28.9 0.0 FIXED PRESSURE LOSS. DEVICE Pipe: 101 - - FBI 5.0 0.0 31.9 0.0 3.0 psi, 21.0 gpm FS 5.0 0.0 28.9 0.0 Pipe: 102 -21.0`1 1.101 PL 4.00 PF 1.0 RC PE FS1 -5.0 0.0 31.9 0.0 7 1 0.074 TL150 FTG 13.00 PV 1.3 BR 2.0 0.0 34.2 0.0 -21.0 1.055 PL 3.00 PF 0.5 Pipe: 103 FT BR 2.0 0.0 34.2 0.0 7.7 0.0902 TLG 6.00 PV U1 0• 2.0 H.S. 34.7 5.0 -26.0 1.985 PL 4.00 PF 0.1 Pipe: 104ET PE150 U1 2.0 H.S. 34.7 5.0 2.7 0.006 TL 22.00 PV 1.7 U2 -2.0 0.0 36.6 0.0 -26.0 2.003 PL 63.75 PF 0.6 Pipe: 1053E PE U2 -2.0 0.0 36.6 0.0 2.6 150 0.006 TL 96.75 PV 0 4 U3 -3.0 0.0 37.6 0.0 Pipe: 106 FIXED PRESSURE LOSS DEVICE U4 -3.0 0.0 41.6 0.0 4.0 psi, 26.0 gpm U3 -3.0 0.0 37.6 0.0 Pipe: 107 -26.0 0.995 PL 8.25 PF 5.1 TX PE -- U4 -3.0 0.0 41.6 0.0 10.7 0.1801 FI 28.25 PV 0.4 SRC -4.0 SRCE 47.1 (N/A) Page SPRINKLER SYSTEM HYDRAULIC ANALYSIS - 2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\lHD CALC.SDF ,LkASS) : Calculations were performed by the HASS 8.8 computer program in accordance with NFPA13 (201 under license no. 38061304 Igranted by Inc. HRS Systems, 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 amaximum imbalance at any node of 0.012,: 'gPm• (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 10.7 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 65.96 psi with a flow of 32.25 gpm. (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150Lengths in Feet Diameter Equivalent Fitting K C G F E T R (in) El Tee RunT Kplg ChkV1v Gate 45 1..00 5.00 1.00 1.00 8.00 2.0 00 7 1.101 6.00 1.00 1.00 11.00 3.00 1.394 2.00 8.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 PAGE: K MATERIAL: CT -K HWC: 150 Equivalent Fitting Lengths in Feet N X Diameter R K C G E T F (in) ChkVly GatV 1v NPTee AngV v Ell Tee 45 -Ell TeeRun Kouplg 6.00 0.00 6.00 14.00 0.995 2.00 6.00 1.00 2.00 0.00 PAGE: L MATERIAL: CT -L HWC: 150 Diameter Equivalent Fitting LengKhs in Feet G N T F R (in) E Tee 45 -Ell TeeRun Kouplg ChkVjv 14.0 GatVly NPTee E11 1.985 6.00 12.00 2.00 4.00 0.50 14.00 1.00 12.00 SPRINKLER_SYSTEM HYDRAULIC ANALYSIS DATE: 5/27/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1HD CALC.age SDFB JOB TITLE: PAGE: M MATERIAL: CT -M HWC: 150 Diameter Equivalent Fittin (in) E T F g Lengths in Feet - Ell R K C G Tee 45 -Ell, TeeRun Kouplg ChkVly GatVly N 1.055 3.00 7.00 1.00 2.00 NP 0.00 .8.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS_ -/27/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL.\1HD CALPaSDF7 TLE: I o 0 0 0 0 o r M N H O N ��Cacvw w � SPRINKLER SYSTEM HYDRAULIC ANALYSIS- Page - 8 - DATE: 5/27/2020, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\INITIAL\1HD CALC.SDF JOB TITLE: WATER SUPPLY CURVE 72+ I I I 660\ I \ I \ I \ 60+ \\ I \ I \ I \ 54+ \\ I \ I \ I \ P 48+ \ R % \\ E \ S \ S 42+ \ U \\ R I \ E I \ 36+ \ ( I \ P \\ S \ I 30+ \ I \ I \ I \ 24+ \ I \ I * <-20.0 Psi @ 1500 gpm I Flow Test Point 18+ I I 12+ LEGEND I g = Required Water Supply -_- I 47.13 psi @ 26.0 4Pm - 6+ „ 0 = Available Water Supply _ 65.97 psi @ 26.0 gpm +---------+-----------+ O 1 0++-+---+----+----- +-- +--------+------600 1800 2000 400 600 800 1000 1200 FLOW (GPM)16 RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR WEDGE HOUSE SECOND FLOOR 2HD CALC AT LIVING ROOM FILE NUMBER: 13460 DATE: JAN 21, 2021 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION 0.05 qpm/sq.ft.. DENSITY: AREA OF APPLICATION: 512.0 sq. ft. COVERAGE PER SPRINKLER: 256.0 sq. £t. 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 @ 32.6 psi REQUIRED PRESSURE (@ SRC): 50.0 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM , HRS SYSTEMS, INC. `kv`k -0101 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 1/21/2021, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC.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 66.0 20.0 1500.0 66.0 31.4 50.0 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 20.0 K= 4.90 7.0 13.0 2 20.0 - - - - 7.9 - - - 3 20.0 K= 4.90 7.4 13.4 4 20.0 - - - - 10.4 - - - 5 20.0 - - - - 15.7 - - - 6 20.0 - - - - 16.4 - - - 7 20.0 - - - - 16.7 - - - 8 20.0 - - - - 16.7 - - - 9 20.0 - - - - 18.3 - - - 10 10.0 - - - - 22.9 - - - 11 10.0 - - - - 23.3 - - - 11A 10.0 - - - - 23.3 - - - 11B 10.0 - - - - 23.3 - - - 11C 10.0 - - - - 23.3 - - - 11D 10.0 - - - - 23.3 - - - 12 10.0 - - - - 22.9 - - - 13 10.0 - - - - 21.3 - - - 14 10.0 - - - - 21.1 - - - TR 10.0 - - - - 24.2 - - - FS 5.0 - - - - 26.8 - - - FSl 5.0 - - - - 29.8 - - - BR 2.0 - - - - 32.6 - - - U1 2.0 HOSE STREAM 34.6 5.0 U2 -2.0 - - - - 36.9 - - - U3 -3.0 - - - - 38.3 - - - U4 -3.0 - - - - 42.3 - - - SRC -4.0 SOURCE 50.0 31.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1/21/2021, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC.SDF JOB TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL (FPS) FW�SUM. (FT) NODES (FT) (K) (PSI) (GPM) FT (PSI) -13.0 1.101 PL 13.00 PF 0.9 Pipe: 1 1 20.0 4.9 7.0 13.0 4.4 0.030 G 0.0 TL29.00 PV 2 20.0 0.0 7.9 0.0 13-.4 1.101 PL 1.00 PF 0.5 Pipe: 20.0 0.0 7.9 0.0 9.5 150 FTG 2FET PE 0.0 20.032 TL 15.00 PV 3 20.0 4.9 7.4 13.4 -26.4 1.101 PL 13.08 PF 2.5 Pipe: 20.0 0.0 7.9 0.0 8.9 150 FTG 2FT2R PE 0.0 2 0.113 TL 22.08 PV q 20.0 0.0 10.4 0.0 -26.4 1.101 PL 9.16 PF 5.2 Pipe: 20.0 0.0 10.4 0.0 8.9 150 FTG 215E PE 0.0 4 5 20.0 0.0 15.7 0.0 0.113 TL 46.16 PV -9.1 1.101 PL 14.42 PF 0.7 Pipe: 20 0 0.0 15.7 0.0 3.1 150 FTG 2E3TR PE 0.0 5 6 20.0 0.0 16.9 0.0 0.016 TL 44.42 PV -17.3 1.101 PL 15.25 PF 1.1 Pipe: 20.0 0.0 15.7 0.0 5.8 150 FTG 2F3R PE 7 20.0 0.0 16.7 0.0 0.0 5 0.052 TL 20.25 PV Pipe: 7 0.0 1.101 PL 5.08 PF 0.0 ET PE 7 20.0 0.0 16.7 0.0 0.0 150 0.000 TL 19.08 PV 0.0 8 20.0 0.0 16.7 0.0 Pipe: 8 -17.3 1.394 PL 30.50 PF 1.6 7 20.0 0.0 16.7 0.0 3.6 150 0.016 TL 97550TRPVPE 0.0 9 20.0 0.0 18.3 0.0 -17.3 1.394 PL 10.00 PF 0.3 Pipe: 9 9 20.0 0.0 18.3 0.0 3.6 150 0.016 TL 16.00 PV 4 3 10 10.0 0.0 22.9 0.0 -17.3 1.394 PL 14.00 PF 0.4 Pipe: 10 10 10.0 0.0 22.9 0.0 3.6 150 0.016 TL 25.00 PV 0.0 11 10.0 0.0 23.3 0.0 Pipe: 11 9.1 1.394 PL 3.25 PF 0.0 11 10.0 0.0 23.3 0.0 1'9 15 0.000 TL T PE 9.25 PV 0.0 11A 10.0 0.0 23.3 0.0 0.0 1.101 PL 14.00 PF 0.0 Pipe: 11A 11A 10.0 0.0 23.3 0.0 0.0 150 0.000 TL 22.00 PV 0.0 1lB 10.0 0.0 23.3 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 1/21/2021, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC.SDF4 JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) NODES (FT) (K) (PSI) (GPM) FL/FT (FT) SUM. (PSI) Pipe: 11B 0.0 1.101 PL 1.00 PF 0.0 11B 10.0 0.0 23.3 0.0 0.0 150 FTG ET PE 0.0 11C 10.0 0.0 23.3 0.0 0.000 TL 13.00 PV Pipe: 11C 0.0 1.101 PL 10.42 PF 0.0 11B 10.0 0.0 23.3 0.0 0.0 150 FTG ETR PE 0.0 11D 10.0 0.0 23.3 0.0 0.000 TL 23.42 PV Pipe: 12 9.1 1.394 PL 19.33 PF 0.3 11A 10.0 0.0 23.3 0.0 1.9 150 FTG 2F4E2TR PE 0.0 12 10.0 0.0 22.9 0.0 0.005 TL 68.33 PV Pipe: 13 9.1 1.101 PL 45.00 PF 1.6 12 10.0 0.0 22.9 0.0 3.1 150 FTG 6F5E3TR PE 0.0 13 10.0 0.0 21.3 0.0 0.016 TL 102.00 PV Pipe: 19 9.1 1.101 PL 3.33 PF 0,2 13 10.0 0.0 21.3 0.0 3.1 150 FTG ET PE 0.0 14 10.0 0.0 21.1 0.0 0.016 TL 15.33 PV Pipe: 15 9.1 1.101 PL 10.00 PF 0.4 14 10.0 0.0 21.1 0.0 3.1 150 FTG 2E PE -4.3 6 20.0 0.0 16.4 0.0 0.016 TL 29.00 PV 11 Pipe: 16 -26.4 1.399 PL 9.66 PF 0.9 10.0 0.0 23.3 0.0 5.5 150 FTG ETR PE 0.0 TR 10.0 0.0 24.2 0.0 0.036 TL 24.66 PV TR Pipe: 100 -26.9 1.399 PL 5.00 PF 0.9 10.0 0.0 24.2 0.0 5.5 150 FTG TR PE 2.2 FS 5.0 0.0 26.8 0.0 0.036 TL 12.00 PV Pipe: 101 FIXED PRESSURE LOSS DEVICE FSI 5.0 0.0 29.8 0.0 FS 5.0 0.0 26.8 0.0 3.0 psi; 26.9 gpm FS1 Pipe: 102 -26.4 1.101 PL 4.00 PF 1.5 5.0 0.0 29.8 0.0 8.9 BR 150 FTG RC PE 1.3 2.0 0.0 32.6 0.0 0.113 TL 13.00 PV Pipe: 103 BR -26.4 1.527 PL 52.00 PF 2.0 2.0 0.0 32.6 0.0 4.6 150 FTG 7E PE 0.0 U1 2.0 H.S. 34.6 5.0 0.023 TL 87.00 PV Pipe: 104 U1 -31.4 1.505 PL 9.00 PF 0.6 2.0 H.S. 34.6 5.0 5.7 150 FTG ET PE 1.7 U2 -2.0 0.0 36.9 0.0 0.034 TL 17.00 PV Pipe: 105 U2 -31.9 2.003 PL 85.25 PF 1.0 -2.0 0.0 36.9 0.0 3.2 150 FTG 3E PE 0.4 U3 -3.0 0.0 38.3 0.0 0.008 TL 118.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1/21/2021, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC.SDF JOB TITLE: Q(GPM) DIA(IN) LENGTH PRESS. PIPE TAG SUM. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) (PSI) NODES (FT) (K) (PSI) (GPM) FIXED PRESSURE LOSS DEVICE Pipe: 106 4.0 psi, 31.4 9Pm 04 -3.0 0.0 42.3 0.0 U3 -3.0 0.0 38.3 0.0 -31.4 0.995 PL 8.25 PE 7.2 Pipe: 107 TX PE 0. 150 FTG U4 -3.0 0.0 42.3 0.0 12.9 0.256 TL 28.25 PV SRC -4.0 SRCE 50.0 (N/A) NOTES (HASS) : (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) under license n. Systems, 3,Ir 61304granted by HRS 208 Southside Square Petersburg, TN 37144 (931) 659-9760 (2) The system has been calculated to providean average imbalance at each node of 0.002 gP imum imbalance at any node of 0.055 gpm• (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 12.9 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 65.95 psi with a flow of 37.84 gpm• (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting LeF 45 E1 Tee RunE T R T ng KpKlg hs in Feet Diameter G (in) ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.394 2.00 8.00 6.00 1.00 1.00 11.00 3.00. 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 KLER EYDRAULIC ANALYSIS DATE: 1/21/2021, NEWPORTNBEACH\FIREM JOB TITLE: SPRINKLERS\CALCS\DELTA 3\2HD Page 6 CALC.SDF PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in (in) E T F Feet 0.995 R Eli Tee 45-Ell TeeRun KOuPlg ChkVly GatVly 2.00 6.00 1.00 2.00 0.00 NPTee AngVly 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Len 4 in (in) ( E T gths Feet F 1.505 R K C Eli Tee 45-Ell TeeRun KOuPlg ChkVly GatVly 4.00 9.00 NPTee 2.00 3.00 0.50 10.00 0.00 9.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in (in) E T F Feet 1.527 R K C G Ell Tee 45-Ell TeeRun KOuPlg ChkVly GatVly 5.00 9.00 N NPTee 2.00 3.00 0.50 11.00 0.00 9.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 1/21/2021, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC.SDF JOB TIT E P. 0 0 0 P 9a0w 04 x w N m z x w 04 r{ N HYDRAULIC ANALYSIS DATE: 1/21/2021, NEWPORT SPRINKLER SYSTEM Page 8 MSPRIINKLERS\CALLS\DELTA 3\2HD CALC.SDF JOB TITLE: WATER SUPPLY CURVE 72+ I I I 660\ I \ I \ I \ 60+ I \ I \ I \ 54+ I \ x P 48+ R E \ S S 42+ U \\ R E 36+ P S I 30+ \ I \ I \ I \\ 24+ I \ I \ I \ 18+ * <-20.0 psi @ 1500 gpm I Flow Test Point I 12+ LEGEND I I X = Required Water Supply IT 50.01 psi @ 31.4 gpm 6+ 0 = Available Water Supply I 65.96 psi @ 31.4 qpm IT 11 0++-+---+----+-----+------ + ___ 400 600 800 1000 1200 1400 1600 1800 FLOW (GPM) 2000 RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR WEDGE HOUSE SECOND FLOOR 1HD CALC AT BEDROOM 2 FILE NUMBER: 13460 DATE: JAN 21, 2021 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION 0.05 gpm/sq. ft. DENSITY: 400.0 sq. ft. AREA OF APPLICATION: COVERAGE PER SPRINKLER: 900.0 sq. ft. max. NUMBER OF SPRINKLERS CALCULATED: 1 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 21.0 gpm TOTAL WATER REQUIRED (including hose): 26.0 gpm FLOW AND PRESSURE (@ BOR): 21.0 gpm @ 34.2 psi REQUIRED PRESSURE (@ SRC): 98.3 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: RUBS G. AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASSCOMPUTER TEMSROGRRAAM H , HYRAULIC ANALYSIS DATE: 1/21/2021, NEWPORT SPRINKLER SYSTEM MSPRDPage 2 NKLERS\CALCS\DELTA 3\1HD CALC.SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. NODE PRESS. PRESS. @ TOTAL REQ'D TAG (PSI)PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) (GPM) (PSI) SRC 66.0 20.0 1500.0 66.0 26.0 98.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE 26.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 21.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE (FT) PRESSURE DISCHARGE (PSI) (GPM) 1 20.0 - 2 20.0 - _ - 19.9 _ _ - 3 20.0 _ - - - 19.9 _ - - 4 20.0 - - - 19.9 _ - - 5 20.0 - - - 19.9 _ - - 6 20.0 - - - 19.9 _ _ _ 7 20.0 - - - 20.3 _ _ - 8 20.0 - - - 19.8 _ _ - 9 20.0 K= 4.90 18.4 21.0 10 10.0 - - - - - 21.0 - - - 11 10.0 - - - - 25.5 - - - 11A 10.0 - - - 25.9 _ _ - 11B 10.0 _ - - - 25.8 - _ - 11C 10.0 - - - 25.8 _ _ - 11D 10.0 - - - 25.8 _ _ - 12 10.0 -- - 25.8 _ - - 13 10.0 - - - 25.7 _ _ _ 1410.0 - - - 24.9 _ - - TR 10.0 - - - 24.8 _ - - FS 5.0 - - - 26.4 - - - FSI 5.0 - _ _ _ 28.9 _ - - BR 2.0 - - - 31.9 - - - U1 2.0- - - 34.2 - - - U2 -2.0 HOSE STREAM 355 . 5.0 U3 -3.0 _ - - - 37.6 - - - U4 -3.0 - - - 38.8 - - - SRC_4.0 SOURCE 42.8 _ _ _ 48.3 26.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1/21/2021, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\1HD CALC.SDF JOB TITLE: PIPE DATA LENGTH PRESS. Q(GPM) DSA (IN) (FT) SUM. PIPE TAG DISC. VEL(FPS) HW(C) (SSI) END ELEV. NOZ. PT (PSI) (GPM) FL/FT NODES (FT) (K) 13.00 PF 0.0 0,0 1.101 PL 2F2E PE 0.0 Pipe: 1 19.9 0.0 0.0 150 FTG 1 20.0 0.0 0.000 TL 29.00 PV 20.0 0.0 19.9 0.0 0.0 2 2 150 FT 1.00 PF 0.0 .0 0.0 0.000 T1.101 PLL 2FET PE 0.0 2 20.0 0-0 0 Pipe: 19.9 15.00 PV 20.0 0.0 19.9 0.0 3 1 0.0 1.101 PL 3.08 PF 0.0 Pipe: 3 20.0 0.0 19.9 0.0 0.0 150 FTG 2FT2R PE 0.0 2 0.000 TL 22.08 PV 4 20.0 0.0 19.9 0.0 0.0 1.101 PL 9.16 PF 0.0 0,0 Pipe: 4 19 9 0.0 0.0 150 FTG 2F5E PE q 20.0 0.0 0.000 TL 46.16 PV 20.0 0.0 19.9 0.0 5144 -6.1 1.101 PL .2 PF 0.3 0,0 pipe: 5 .9 0.0 2.1 150 FTG 2E3TR PE 5 20.0 0.0 19 0.008 TL 44.42 PV 20.0 0.0 20.3 0.0 6 21 1.101 PL 150 FTG 15.25 PF 0.2 Pipe: 6 0.0 .2F3R PE 0.0 5 20.0 0.0 19.9 0.008 TL 20.25 PV 7 20.0 0.0 lg,g 0.0 1.4 21.0 1.101 PL 5.08 PF Pipe: 7 7.1 19.8 150 FTG 19F08 PE PV 7 0.0 0. 20.0 0.0 0.074 TL 20.0 4.9 18.4 21.0 8 -14.9 1.394 PL 30.50 PF 1.2 Pipe: 8 0 0 3 1 150 FTG 97.50 R PE 0.0 7 20.0 0.0 19.8 0,013 TL 97.50 PV 20.0 0.0 21.0 0.0 9 0 PF 0.2 -19.9 1.394 PL 10.0T PE 4-3 Pipe: 9 0 0 0 3.1 150 FTG 9 20.0 0.0 21 0.013 TL 16.00 PV 10.0 0.0 25.5 0.0 10 1q.00 PF 0.3 0.0 1 3.9 4. 1.394 PL 2FTR PE 0.0 10 pipe: 10 150 FTG 10.0 0.0 25.5 0.013 TL 25.00 PV 9 0.0 11 10.0 0.0 25. 0.0 6.1 1.394 PL 3.25 PF 1. 11 0.0 150 FTG T PE 0.0 Pipe: 25.9 9.25 PV 11 10.0 0.0 0.0 0.002 TL 11A 10.0 0.0 25.8 1.101 PL 14.00 PF 0.0 0.0 pipe: 11A 0 0 0.0 150 FTG 11A 25•8 0.0 2FTR PE 0.0 10.0 0.0 25.8 0.000 TL 22.00 PV 11B 10.0 0.0 DATE: 1/21/2021, NEWPORT SPRINKLER SYSTEM MSPRIDNKLERS\CALCS\DELTA 3\lHD CALC.SDF JOB TITLE: RAULIC ANALYSIS Page 4 PIPE TAG END ELEV. NOZ.PQ(GPM) DIA(IN) LENGTH PRESS. (FT) NODES S DISC. VEL(FPS) HW(C) (K) (PSI) (GPM) (FT) SUM. Pipe: 11B FL/FT (PSI) 11B 10.0 0.025 0.0 1.101 PL 1.00 PF 0.0 11C .8 0.0 00 10.0 0.0 25.8 0.0 . 150 FTG ET PE 0.0 Pipe: 11C 0.000 TL 13.00 pV 11B 10.0 0.00.0 1.101 PL 10.42 PF 25 11D 10 '8 0.0 0.0 150 0.0 .0 0.0 25.8 0.0 FTG ETR PE 0.0 0.000 TL 23.42 PV Pipe: 12 11A 10.0 0.025.8 1.3 6.1 1.394 PL 19.33 PF 12 10.0 0.0 25.7 0.0 150 FTG 2F4E2TR PE 0 0.0 0.002 TL 68.33 PV Pipe: 13 12 10.0 0.0 25.7 6.1 1.101 PL 45.00 PF 13 0.0 2.1 150 FTG 0.8 10.0 0•p 29 9 0 0 6FSE3TR PE 0.0 0.008 TL 102.00 PV Pipe: 19 13 10.0 0.0 24.9 . 6.1 1.101 PL 3.33 PF 14 0.1 10.0 0.0 24.8 �:O 21 150 FTG ET PE 0.0 Pipe: 15 0.008 TL 15.33 PV 14 10.0 0.0 24.8 6'1 1.101 PL 10.00 PF 6 20.0 0.0 2.1 0.2 0.0 150 FTG 2E PE 20.3 0.0 -4.3 0.008 TL 24.00 pV Pipe: 16 -21.0 1.394 PL 9.66 PF 11 10.0 0,0 25 0.6 TR 10.0 0.0 26.9 �:O 4.4 150 FTG ETR PE 0.0 Pipe: 100 0.024 TL 24.66 PV -21.0 1.394 PL 5.00 PF TR 10.0 0•0 FS 26.9 0.0 9.4 150 FTG 0.3 Pipe: 101 , 5.0 0.0 28.9 p0 TR PE 2.2 0.024 TL 12.00 PV FS1 5.0 0.0 31.9 FIXED PRESSURE LOSS DEVICE FS 5.0 0.0 28.9 0.0 3.0 psi. 21.0 qpm Pipe: 102 FS1 5.0 0.0 31.9 -21.0 1.101 PL BR 9.00 PF 1.0 2.0 0.0 00 7'1 150 FTG RC PE 39.2 0.0 1.3 0.074 TL Pipe: 103 13.00 pV BR 2.0 0.0 -21.0 1.527 PL 52.00 PF U1 34'2 0.0 3.7 150 FTG 1.3 2.0 H.S. 35.5 5.0 7E PE 0.0 0.015 TL 87.00 pV Pipe: 104 Ul 2.0 H.S. 35.5 -26.0 1.505 PL 9.00 PF 0.4 U2 -2.0 0.0 37.6 5.0 4.7 150 FTG ET PE 1.7 Pipe: 105 0.024 TL 17.00 PV U2 -2.0 0.0 -26.0 2.003 PL 85.25 PF 37.6 0.7 U3 -3.0 0.0 38.8 0.0 2 6 150 FTG 3E PE 0.4 0.006 TL 118.25 pV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1/21/20211 NEWPORT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\1HD CALC.SDF JOB TITLE: Q(GPM) DIA(IN) LENGTH PRESS. PIPE TAG SUM. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) (PSI) NODES (FT) (K) (PSI) (GPM) FIXED PRESSURE LOSS DEVICE Pipe: 106 4.0 psi, 26.0 9P U4 -3.0 0.0 42.8 0.0 m U3 -3.0 0.0 38.8 0.0 -26.0 0.995 PL 8.25 PF 5.1 Pipe: 107 TX RE U4 -3.0 0.0 42.8 0.0 10.7 0.1801 TL 0• 28.25 PV SRC -4.0 SRCE 48.3 (N/A) NOTES (HASS): (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) 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 providean average um imbalance at each node o ff 00.001gpm. imbalance at any node (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 10.7 £t/sec at pipe 107. (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. (s) Available pressure at source node SRC under full flow conditions is 65.96 psi with a flow of 31.71 gpm- (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet G F F T R (in) ChkVly Gate 45 E1 Tee RunT Kp100 8.00 2.00 1.101 1.00 7.00 5.00 1.00 1.00 11.00 3.00 1.394 2.00 8.00 6.00 1.00 2.003 2.00 11.00 10.00 1.00 1.00 17.00 3.00 DATE: 1/21/2021, NEWPORT SPRINKLER RAULIC ANALYSIS JOB TITLE: BEACH\FIREMSPRIDNKLERS\CALCS\DELTA Page 6 3\1HD CALC.SDF PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet 0.995 F R K C Ell Tee 45-Ell TeeRun Kou 1 GVjv 2.00 p Chk6.0 Gat0.0 N X 6.00 1.00 2. 00 0.00 0 NPTee An14.0 6.00 0.00 6.00 14.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in (in) E T F Feet 1.505 R K Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly 4.00 NPTee 9.00 2.00 3.00 0.50 10.00 0.00 9.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in (in) E T F Feet 1.527 R K C G Ell Tee 45-Ell TeeRun Kouplg ChkVly GatVly 5.00 N NPTee 9.00 2.00 3.00 0.50 11.00 0.00 9.00 SPRINKLER SYSTEM HYDRAOLIC ANALYSIS Page 7 DATE: 1/21/2021, NEWPORT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\1HD CALC.SDF JOB TIT M7 C7 rC P c7 W a PZ W w m P a W HYD ULIC ANALYSIS KLER DATE: 1/21/2021, NEWPORTNBEACH\FIRE MSPRINKPage LERS\CALCS\DELTA 3\1HD CALC.SDF 8 JOB TITLE: WATER SUPPLY CURVE 72+ I I I 660\ I \ I \ I \ 60+ I \ I \ I \ 54+ \\ I \ I \ I \ P 48X R \\ E S 5 42+ \ U R \ E 36+ ( I \ P S 1 30+ I \ I \ I \ 24+ I \ I \ I \ 18+ 1-20.0 psi @ 1500 4em Flow Test Point I 12+ LEGEND 1p X = Required Water Supply I 48.30 psi @ 26.0 qpm 6+ I 0 = Available Water Supply I 65.97 psi @ 26.0 gpm I 0++-+---+----+----+------ +------+------ 400 600 800 1000 1200 +-----_---+-----------+ 1400 1600 1800 FLOW (GPM) 2000 RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR WEDGE HOUSE FIRST FLOOR 2HD CALC AT GARAGE FILE NUMBER: 13460 DATE: JAN 21, 2021 -DESIGN DATA - OCCUPANCY CLASSIFICATION: NFPA 13D, 2016 EDITION 0.05 gpm/sq. ft. DENSITY: 648.0 sq. ft. AREA OF APPLICATION: 324.0 sq. £t. max. COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 34.4 gPm TOTAL WATER REQUIRED (including hose): 39.3 gPm 34.4 gpm @ 28.8 psi FLOW AND PRESSURE (@ BOR): 52.1 psi REQUIRED PRESSURE (@ SRC): 7/16 inch SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF NEWPORT BEACH CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASSHRS COMPUTTEMSPROGRAM , SYSTEM HYDAULIC DATE: 1/21/2021RT BEACH\FIRE SPRINKLER SPRINKLERS\CALCS\DELTA YPage 2 3\2HD CALC-GARAGE.SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ TAG (PSI) (PSI) PRESS. @ DEMAND PRESS. (GPM) (PSI) (GPM) (PSI) SRC 66.0 20.0 1500.0 65.9 39.3 52.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL OTHER TOTAL HOSE STREAM ALLOWANCE AT SOURCE HOSE STREAM ALLOWANCES DISCHARGE FROM ACTIVE5.0 SPRINKLERS 39.3 0.0 39.3 GPM GPM GPM GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE (FT) PRESSURE DISCHARGE (PSI) (GPM) 1 20.0 _ 2 20.0 - _ -13.3 - - - 3 20.0 - - _ _ 13.3 - - - 4 20.0 _ _ - - 13.3 - _ _ 5 20.0 - - - - 13.3 _ _ _ 6 20.0 - - - 13.3 _ _ - 7 20.0 _- 13.2 _ _ - 8 20.0 _- _- _- _ 13.3 _ _ - 9 20.0 _ _ 13.3 _ _ _ 10 10.0 _ _ 13.4 _ _ _ 11 10.0 _ - 17.7 _ - _ 11A 10.0 - - - 17.8 _ - _ 11B 10.0.- - - - - 17.3 _ - _ 11C 10.0 - - - 13.2 _ _ - 11D 10.0 K= 4.90 12.5 17.4 12 10.0 K= 4.90 - 12.0 17.0 13 10.0 - - - - 17.3 - - - 14 10.0 - - - 17.5 - - - TR 10.0 _ - - - 17.5 _ _ - FS 5.0 - - - 19.2 - - - FSI 5.0 - - - 22.1 - _ - BR 2.0 _ _ _ - 25.1 - _ - Ul U2 2.0 - - - HOSE STREAM 28.8 32.0 - - - -2.0 5.0 U3 -3.0 _ _ 34.7 - - - U4 -3.0 _ - 36.6 - - - SRC -9.0 - - - 40.6 - - - SOURCE 52.1 39.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1/21/202IRT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC-GARAGE.SDF JOB TITLE: PIPE DATA Q (GPM) DIA (IN) LENGTH PRESS. (FT) SUM. PIPE TAG (PSI) END ELEV. NOZ. PT DISC. VEL (FPS) HW(C) NODES (FT) (K) (PSI) (GPM) 0.0 1.101 PL 13.00 PF 0.0 Pipe: 13 0.0 0.0 150 FTG 2F2E PE 0.0 1 20.0 0.0 13. 0.000 TL 29.00 PV 2 20.0 0.0 13.3 0.0 0.0 1.101 PL 1.00 PF 0.0 Pipe: 2 13.3 150 FTG 2FET PE 0.0 2 20.0 0.0 0.0 0.0 0.000 TL 15.00 PV 3 20.0 0.0 13.3 0.0 0.0 1 150 FTG 2FT1 PL P Pipe: 3 R PE 0.0 13.3 0.0 0.0 4 22.08 PV 2 20.0 0.0 0 0 0.000 TL 20.0 0.0 13.3 0.0 1.101 PL 9.16 PF 0.0 4 Pipe: 20.0 0.0 13.3 0.0 150 FTG 96F16 pV 0.0 5 20.0 0.0 0.0 13.3 0.000 TL 2.7 1.101 PL 14.42 PF 0.1 0.0 pipe: 5 O,g 150 FTG 2E3TR PE 5 20.0 0.0 13.3 0.0 0,002 TL 44.42 PV 6 20.0 0.0 13.2 0.0 _2 ,7 1.101 PL 15.25 PF 0.0 Pipe: 6 13.3 0.0 0.9 150 FTG 2F3R BE 0.0 5 20.0 0.0 0.002 TL 20.25 PV 7 20.0 0.0 13.3 0.0 0.0 1.101 PL 5.08 PF 0.0 7 Pipe 20.0 0.0 13.3 0.0 0.0 0.0 150 FTG 2FET PE 0.0 13.3 0.000 TL 19.08 PV 8 20.0 0.0 _2,7 1.394 PL 30.50 PF 0.1 Pipe: 8 13.3 150 FTG 4F5E3TR PE 0.0 0.0 0.6 97,50 PV 7 20.0 0.0 0 0 0.001 TL 9 20.0 0.0 13.4 _2,7 1.394 PL 10.00 PF 0.0 T PE 4.3 9 Pipe 20.0 0.0 13.4 0.6 150 FTG 16.00 PV 10 10.0 0.0 0.0 17 7 0.001 TL -2.7 1.394 PL 19.00 PF 0.0 Pipe: 100 0 0,6 150 FTG 2FTR BE 0.0 10.0 0.0 17.7 25.00 PV 10 17.8 0.0 0.001 TL 11 10.0 0.0 31.6 1.394 PL 3.25 PF 0.5 PE 0.0 Pipe: 11 0.0 6.6 150 FTG 11 10.0 0.0 17.8 0 0 0.050 TL 9.25 PV 11A 10.0 0.0 17.3 34.9 1.101 PL 14.00 PF 4•1 Pipe: 11A 11.6 150 FTG 2FTR BE 0.0 11A 10.0 0.0 17.3 0.0 0.185 TL 22.00 PV 11B 10.0 0.0 13.2 DATE: TLE: 021RT BE SPRINKLERS SYSTE HYDRAULIC ANALYSIS JOB TITLE: Page 4' �2HD CALC-GARAGE.SDF PIPE TAG END ELEV. 4(GPM) DIA(IN) LENGTH NODES NOZ. PT DISC. VEL(FPS) HW(C) PRESS. ) (FT) (FT) (K) (PSI) (GPM) SUM. FL/FT (PSI) Pipe: 11B 11B 10.0 0.0 13.2 17'4 1.101 PL 1.00 PF 11C 0.0 5.8 150 FTG 0.7 10.0 4.9 12.5 17.4 ET PE 0.0 0.052 TL 13.00 pV Pipe: 11C 11B 10.0 0.0 13'2 17.0 1.101 PL 10.42 PF 11D 10 0.0 5.7 150 FTG 1.2 .0 9.9 12.0 17.0 ETR PE 0.0 173 0.050 TL 23.42 PV Pipe: 12 11A 10.0 0.0 -2'7 1.394 PL 19.33 PF 12 10.0 0 0.0 0.6 150 FTG 2F4E2T0.0 .0 17.3 0.0 R PE 0.0 0.001 TL 68.33 pV ; Pipe: 13 12 10.0 0.0 -2'7 1.101 PL 45.00 PF 13 17.3 0.0 0.9 150 FTG 0.2 10.0 0.0 17.5 0.0 6F5E3TR PE 0.0 0.002 TL 102.00 pV Pipe: 19 13 10.0 17 0.0 -2'7 1.101 PL 3.33 PF 14 .5 0.0 0.9 150 FTG 0.0 10.0 0.0 17.5 0.0 ET PE 0.0 0.002 TL 15.33 pV Pipe: 15 14 17 10.0 0.0 -2.7 1.101 PL 10.00 pg 6 20.0 .5 0.0 0.9 150 FTG 0.0 0.0 13.2 0.0 2E PE -4.3 0.002 TL 24.00 PV Pipe: 16 11 10.0 0.0 17.8 -34.4 1.394 PL 9.66 pF TR 10.0 0.0 19.2 0.0 7 2 1.4 150 FTG ETR PE 0.0 0.059 TL 24.66 PV Pipe: 100 TR 10.0 0.0 19.2 0.0 -34.4 1.394 PL 5.00 PF 0.7 FS 5.0 0.0 22.1 0.0 7'2 150 FTG TR PE 2.2 0.059 TL 12.00 PV Pipe: 101 FS1 5.0 0.0 25.1 0.0 FIXED PRESSURE LOSS DEVICE FS 5.0 0.0 22.1 0.0 3.0 psi. 34.4 qpm Pipe: 102 FS1 5.0 0.0 25.1 -34.4 1.101 PL 4.00 pF BR 0.0 11.6 150 FTG 2.9 2.0 0.0 28.8 0.0 RC PE 1.3 0.185 TL 13.00 pV Pipe: 103 BR 2.0 0.0 28.8 -34.4 1.527 PL 52.00 PF U1 2.0 H.S. 32.0 5.0 0.0 6.0 150 FTG 7E PE 3.3 0.0 0.038 TL 87.00 PV Pipe: 109 U1 2.0 H.S. -39.9 1.505 PL 9.00 PF U2 32.0 5.0 7.1 150 FTG 0.9 -2.0 0.0 34.7 0.0 ET PE 1.7 0.052 TL 17.00 PV Pipe; 105 U2 -2.0 0.0 34.7 -39.4 2.003 PL 85.25 PF U3 0.0 4.0 150 FTG 1.5 -3.0 0.0 36.6 0.0 3E PE 0.4 0.013 TL 118.25 pV ' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1/21/2021RT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC-GARAGE.SDF JOB TITLE: Q(GPM) DIA(IN) LENGTH PRESS. PIPE TAG SUM. END ELEV. NO?. PT DISC. VEL(FPS) HW(C) (FT) (PSI) NODES (FT) (K) (PSI) (GPM) FIXED PRESSURE LOSS DEVICE Pipe: 106 4.0 psi, 39.4 gpm U4 -3.0 0.0 40.6 0.0 03 -3.0 0.0 36.6 0.0 -39.3 0.995 PL 8.25 PF PE 1 Pipe: 107 G 0,4 U4 -3.0 0.0 40.6 0.0 16.2 0.390 TL28.25 PV SRC -4.0 SRCE 52.1 (N/A) NOTES (HASS): (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2019) 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 000001 gpmm and a maximum imbalance at any node (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 16.2 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 65.93 psi with a flow of 45.59 gpm• (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet G F E T R K (in) 45 E1 Tee RunT Kplg ChkVly Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.394 2.00 8.00 6.00 1.00 1.00 11.00 3.00 2.003 2.00 11-0010.00 1.00 1.00 17.00 3.00 DATE: 1/21/2021RT SPRINKLE SYSTEM HYDRAULIC SIS BEACH\FIRE RSPRINKLERS\CALCS\DELTAY Page 6 JOB TITLE: 3\2HD CALC-GARAGE.SDF PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet T F 0.995 R K C Ell Tee 95-Ell TeeRun Kou 1 G 2.00 GatVly N x NPTee 6.00 1.00 2.00 O.000hkVly 6.00 AngVly 0.00 6.00 19.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter (in) Equivalent Fitting Lengths in Feet 1.505 E T F R K Ell C G Tee 95-Ell TeeRun Kouplg ChkVly GatVly 9.00 N NPTee 9.00 2.00 3.00 0.50 10.00 0.00 9.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter (in) Equivalent Fitting Lengths in Feet 1.527 E T F R K C G Ell Tee 95-Ell TeeRun Kouplg ChkVly Gat N 5.00 9.00 2.00 3.00 0.50 11.00 NPTee 0.00 9.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 ,/ol/7021RT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC-GARAGE.SDF DATE: JOB TIT E LL tS 0 0 0 N .1 0 � r � aawm�noaw -o.N.�._ rl N / SPRINKLER SYSTEM HYDRAULIC ANALYSIS DATE: 1/21/202IRT BEACH\FIRE SPRINKLERS\CALCS\DELTA 3\2HD CALC-GARAGPage E.SDFB JOB TITLE: WATER SUPPLY CURVE 72+ I I 660\ I \ I \ I \ 60+ I \ I \ I \ 54+ \ X I \ I \ P 48+ R E \ S S 42+ \ U R E I \ 36+ \ P S I 30+ I \ I \ I \\ 24+ I I \ I \ 18+ � I I 12+ LEGEND I I X = Required Water Supply 1 52.06 psi @ 39.3 qpm 6+ 1 0 = Available Water Supply 65.95 psi @ 39.3 gpm <-20.0 psi @ 1500 gpm Flow Test Point —T------------------------------__ --- 900 600 800 1000 1200 +-------+- 1400 1600 1800 FLOW (GPM) 2000