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FPS 200 9 0Z10 1 . J2(o7O Set) ,4LtQ /3 /v( REC A PROFESSIONAL FIRE SYSTEMS APR 2 0 2009 17272 S. STEINER ROAD BEAVERCREEK, OR 97004 CITY OF TIGARD BUILDING DIVISIg'•I HYDRAULIC CALCULATIONS FOR Apex Industries Roof Area FILE NUMBER: Roof Area DATE: APR 9, 2009 - DESIGN DATA - OCCUPANCY CLASSIFICATION: Roof Area Over Clean Room Per NFPA P3 DENSITY: .20 gpm /sq. ft. AREA OF APPLICATION: (Entire Area) 2451 sq. ft. COVERAGE PER SPRINKLER: 120 sq. ft. Max. NUMBER OF SPRINKLERS CALCULATED: 27 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 758.7 gpm TOTAL WATER REQUIRED (including hose): 1008.8 gpm FLOW AND PRESSURE (@ BOR): 758.8 gpm @ 53.5 psi SPRINKLER ORIFICE SIZE: 1/2" inch NAME OF CONTRACTOR: A Professional Fire Systems, Co. DESIGN /LAYOUT BY: R. Berry AUTHORITY HAVING JURISDICTION: City Of Tigard CONTRACTOR CERTIFICATION NUMBER: 41650 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 16061181 ) HRS SYSTEMS, INC. TUCKER, GA 30084 X 01° PRO,c4 wive C OREGON EXPIRES: 12��l1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 • DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) Z 106.0 96.0 2500.0 104.1 1008.8 59.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1008.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 758.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 16.9 K= 5.60 23.2 27.0 2 16.9 K= 5.60 24.5 27.7 3 16.6 - - - - 39.6 - - - 4 16.9 K= 5.60 24.3 27.6 . 5 16.9 K= 5.60 27.1 29.2 6 16.6 - - - - 38.0 - - - 7 16.6 - - - - 39.6 - - - 8 16.9 K =.5.60 23.5 27.2 9 16.9 K= 5.60 24.9 27.9 10 16.6 - - - - 40.2 - - - 11 16.9 K= 5.60 25.2 28.1 12 16.9 K= 5.60 28.1 29.7 13 16.6 - - - - 39.4 - - - 14 16.6 - - - - 41.1 - - - 15 16.9 K= 5.60 24.5 27.7 16 16.9 K= 5.60 25.9 28.5 17 16.6 - - - - 41.8 - - - 18 16.9 K= 5.60 26.8 29.0 19 =:.. 16.9 K= 5.60 29.9 30.6 20 , 0:6. 6 - - - - 41.9 21 /...,;*" ;= /, r: 1 FQ•:1 "6 :: ' .6 - - - - 43.6 - - - 22y-:.V, e' ' `'16•: K= 5.60 18 . 9 24.3 24 ' "''' � • 1 '.. 9y K= 5.60 21.2 25.8 • 24 16.9 K= 5.60 29.8 30.6 25V' ti';•:e; .0. 10;' - - - - 37.5 - - - 2 6\l •'1 f _1ei.§ K= 5.60 23.2 27.0 27 "<11G'9 K= 5.60 25.9 28.5 28 '`16.6 � - - - - 36.3 - - - 2 9�':.t....,, •^ �, .:: �1: :61;.,6,, - - - - 38.8 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 30 16.9 K= 5.60 19.4 24.6 31 16.9 K= 5.60 21.7 26.1 32 16.9 K= 5.60 30.5 31.0 33 16.6 - - - - 38.4 - - - 34 16.9 K= 5.60 24.6 27.8 35 16.9 K= 5.60 27.5 29.4 36 16.6 - - - - 38.5 - - - 37 16.6 - - - - 41.1 - - - 38 16.9 K= 5.60 20.6 25.4 39 16.9 K= 5.60 23.1 26.9 40 16.9 K= 5.60 32.5 31.9 41 16.6 - - - - 40.9 - - - 42 16.9 K= 5.60 26.5 28.8 43 16.9 K= 5.60 29.6 30.4 44 16.6 - - - - 41.3 - - - 45 16.6 - - - - 44.1 - - - A 15.4 - - - - 41.1 - - - B 15.4 - - - - 41.2 - - - C 15.4 - - - - 41.7 - - - D 15.4 - - - - 42.7 - - - E 15.4 - - - - 43.3 - - - F 15.4 - - - - 45.3 - - - G 15.4 - - - - 45.3 - - - H 15.4 - - - - 40.0 - - - I 15.4 - - - - 40.3 - - - J 15.4 - - - - 41.0 - - - K 15.4 - - - - 42.7 - - - L 15.4 - - - - 43.6 - - - M 15.4 - - - - 46.1 - - - N 15.4 - - - - 45.8 - - - 0 15.4 - - - - 45.8 - - - P 1.5 - - - - 53.5 - - - X 0.0 - - - - 56.4 - - - Y 0.0 - - - - 60.6 - - - Z 3.0 SOURCE 59.5 758.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 • DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System 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 -27.0 1.049 PL 6.00 PF 1.4 1 16.9 5.6 23.2 27.0 10.0 120 FTG - - -- PE 0.0 2 16.9 5.6 24.5 27.7 0.226 TL 6.00 PV Pipe: 2 -54.7 1.049 PL 12.83 PF 14.9 2 16.9 5.6 24.5 27.7 20.3 120 FTG T PE 0.1 3 16.6 0.0 39.6 0.0 0.837 TL 17.83 PV Pipe: 3 -54.7 1.610 PL 1.25 PF 1.0 3 16.6 0.0 39.6 0.0 8.6 120 FTG T PE 0.5 A 15.4 0.0 41.1 0.0 0.104 TL 9.25 PV Pipe: 4 -54.7 2.469 PL 10.00 PF 0.1 A 15.4 0.0 41.1 0.0 3.7 120 FTG - - -- PE 0.0 B 15.4 0.0 41.2 0.0 0.013 TL 10.00 PV Pipe: 5 -27.6 1.049 PL 12.00 PF 2.8 4 16.9 5.6 24.3 27.6 10.2 120 FTG - - -- PE 0.0 5 16.9 5.6 27.1 29.2 0.236 TL 12.00 PV Pipe: 6 -56.8 1.049 PL 12.00 PF 10.8 5 16.9 5.6 27.1 29.2 21.1 120 FTG - - -- PE 0.1 6 16.6 0.0 38.0 0.0 0.896 TL 12.00 PV - Pipe: 7 -56.8 1.380 PL 0.92 PF 1.6 6 16.6 0.0 38.0 0.0 12.2 120 FTG T PE 0.0 7 16.6 0.0 39.6 0.0 0.236 TL 6.92 PV Pipe: 8 -56.8 1.610 PL 1.25 PF 1.0 7 16.6 0.0 39.6 0.0 8.9 120 FTG T PE 0.5 B 15.4 0.0 41.2 0.0 0.111 TL 9.25 PV Pipe: 9 -111.4 2.469 PL 10.00 PF 0.5 B 15.4 0.0 41.2 0.0 7.5 120 FTG - - -- PE 0.0 C 15.4 0.0 41.7 0.0 0.048 TL 10.00 PV Pipe: 10 -27.2 1.049 PL 6.00 PF 1.4 8 16.9 5.6 23.5 27.2 10.1 120 FTG - - -- PE 0.0 9 16.9 5.6 24.9 27.9 0.229 TL 6.00 PV Pipe: 11 -55.1 1.049 PL 12.83 PF 15.1 9 16.9 5.6 24.9 27.9 20.5 120 FTG T PE 0.1 10 16.6 0.0 40.2 0.0 0.849 TL 17.83 PV - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System 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: 12 -55.1 1.610 PL 1.25 PF 1.0 10 16.6 0.0 40.2 0.0 8.7 120 FTG T PE 0.5 C 15.4 0.0 41.7 0.0 0.105 TL 9.25 PV Pipe: 13 -166.6 2.469 PL 10.00 PF 1.0 C 15.4 0.0 41.7 0.0 11.2 120 FTG - - -- PE 0.0 D 15.4 0.0 42.7 0.0 0.102 TL 10.00 PV Pipe: 14 -28.1 1.049 PL 12.00 PF 2.9 11 16.9 5.6 25.2 28.1 10.4 120 FTG - - -- PE 0.0 12 16.9 5.6 28.1 29.7 0.244 TL 12.00 PV Pipe: 15 -57.8 1.049 PL 12.00 PF 11.1 12 16.9 5.6 28.1 29.7 21.5 120 FTG - - -- PE 0.1 13 16.6 0.0 39.4 0.0 0.928 TL 12.00 PV Pipe: 16 -57.8 1.380 PL 0.92 PF 1.7 13 16.6 0.0 39.4 0.0 12.4 120 FTG T PE 0.0 14 16.6 0.0 41.1 0.0 0.244 TL 6.92 PV Pipe: 17 -57.8 1.610 PL 1.25 PF 1.1 14 16.6 0.0 41.1 0.0 9.1 120 FTG T PE 0.5 D 15.4 0.0 42.7 0.0 0.115 TL 9.25 PV Pipe: 18 -224.4 3.068 PL 10.00 PF 0.6 D 15.4 0.0 42.7 0.0 9.7 120 FTG - - -- PE 0.0 E 15.4 0.0 43.3 0.0 0.061 TL 10.00 PV Pipe: 19 -27.7 1.049 PL 6.00 PF 1.4 15 16.9 5.6 24.5 27.7 10.3 120 FTG - - -- PE 0.0 16 16.9 5.6 25.9 28.5 0.238 TL 6.00 PV Pipe: 20 -56.2 1.049 PL 12.83 PF 15.7 16 16.9 5.6 25.9 28.5 20.9 120 FTG T PE 0.1 17 16.6 0.0 41.8 0.0 0.881 TL 17.83 PV Pipe: 21 -56.2 1.610 PL 1.25 PF 1.0 17 16.6 0.0 41.8 0.0 8.9 120 FTG T PE 0.5 E 15.4 0.0 43.3 0.0 0.109 TL 9.25 PV Pipe: 22 -280.6 3.068 PL 6.67 PF 2.0 E 15.4 0.0 43.3 0.0 12.2 120 FTG T PE 0.0 F 15.4 0.0 45.3 0.0 0.093 TL 21.67 PV Pipe: 23 -29.0 1.049 PL 12.00 PF 3.1 18 16.9 5.6 26.8 29.0 10.8 120 FTG - - -- PE 0.0 19 16.9 5.6 29.9 30.6 0.259 TL 12.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 • DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System 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: 24 -59.6 1.049 PL 12.00 PF 11.8 19 16.9 5.6 29.9 30.6 22.1 120 FTG - - -- PE 0.1 20 16.6 0.0 41.9 0.0 0.982 TL 12.00 PV Pipe: 25 -59.6 1.380 PL 0.92 PF 1.8 20 16.6 0.0 41.9 0.0 12.8 120 FTG T PE 0.0 21 16.6 0.0 43.6 0.0 0.258 TL 6.92 PV Pipe: 26 -59.6 1.610 PL 1.25 PF 1.1 21 16.6 0.0 43.6 0.0 9.4 120 FTG T PE 0.5 G 15.4 0.0 45.3 0.0 0.122 TL 9.25 PV Pipe: 27 -59.6 4.026 PL 3.33 PF 0.0 G 15.4 0.0 45.3 0.0 1.5 120 FTG - - -- PE 0.0 F 15.4 0.0 45.3 0.0 0.001 TL 3.33 PV Pipe: 28 -340.3 6.065 PL 65.75 PF 0.5 F 15.4 0.0 45.3 0.0 3.8 120 FTG T PE 0.0 N 15.4 0.0 45.8 0.0 0.005 TL 95.75 PV Pipe: 29 -24.3 1.049 PL 12.17 PF 2.3 22 16.9 5.6 18.9 24.3 9.0 120 FTG - - -- PE 0.0 . 23 16.9 5.6 21.2 25.8 0.187 TL 12.17 PV Pipe: 30 -50.1 1.049 PL 12.17 PF 8.7 23 16.9 5.6 21.2 25.8 18.6 120 FTG - - -- PE 0.0 24 16.9 5.6 29.8 30.6 0.711 TL 12.17 PV Pipe: 31 -80.7 1.380 PL 10.83 PF 7.6 24 16.9 5.6 29.8 30.6 17.3 120 FTG T PE 0.1 25 16.6 0.0 37.5 0.0 0.452 TL 16.83 PV Pipe: 32 -80.7 1.610 PL 1.25 PF 2.0 25 16.6 0.0 37.5 0.0 12.7 120 FTG T PE 0.5 H 15.4 0.0 40.0 0.0 0.213 TL 9.25 PV Pipe: 33 -80.7 2.469 PL 10.00 PF 0.3 H 15.4 0.0 40.0 0.0 5.4 120 FTG - - -- PE 0.0 I 15.4 0.0 40.3 0.0 0.027 TL 10.00 PV Pipe: 34 -27.0 1.049 PL 12.00 PF 2.7 26 16.9 5.6 23.2 27.0 10.0 120 FTG - - -- PE 0.0 27 16.9 5.6 25.9 28.5 0.226 TL 12.00 PV Pipe: 35 -55.5 1.049 PL 12.00 PF 10.3 27 16.9 5.6 25.9 28.5 20.6 120 FTG - - -- PE 0.1 28 16.6 0.0 36.3 0.0 0.858 TL 12.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System 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: 36 -55.5 1.380 PL 4.92 PF 2.5 28 16.6 0.0 36.3 0.0 11.9 120 FTG T PE 0.0 29 16.6 0.0 38.8 0.0 0.226 TL 10.92 PV Pipe: 37 -55.5 1.610 PL 1.25 PF 1.0 29 16.6 0.0 38.8 0.0 8.7 120 FTG T PE 0.5 I 15.4 0.0 40.3 0.0 0.107 TL 9.25 PV Pipe: 38 -136.1 2.469 PL 10.00 PF 0.7 I 15.4 0.0 40.3 0.0 9.1 120 FTG - - -- PE 0.0 J 15.4 0.0 41.0 0.0 0.070 TL 10.00 PV Pipe: 39 -24.6 1.049 PL 12.17 PF 2.3 30 16.9 5.6 19.4 24.6 9.1 120 FTG - - -- PE 0.0 31 16.9 5.6 21.7 26.1 0.191 TL 12.17 P\ Pipe: 40 -50.7 1.049 PL 12.17 PF 8.9 31 16.9 5.6 21.7 26.1 18.8 120 FTG - - -- PE 0.0 32 16.9 5.6 30.5 31.0 0.728 TL 12.17 PV Pipe: 41 -81.7 1.380 PL 10.83 PF 7.8 32 16.9 5.6 30.5 31.0 17.5 120 FTG T PE 0.1 33 16.6 0.0 38.4 0.0 0.462 TL 16.83 PV Pipe: 42 -81.7 1.610 PL 1.25 PF 2.0 33 16.6 0.0 38.4 0.0 12.9 120 FTG T PE 0.5 J 15.4 0.0 41.0 0.0 0.218 TL 9.25 PV Pipe: 43 -217.8 2.469 PL 10.00 PF 1.7 J 15.4 0.0 41.0 0.0 14.6 120 FTG - - -- PE 0.0 K 15.4 0.0 42.7 0.0 0.167 TL 10.00 PV Pipe: 44 -27.8 1.049 PL 12.00 PF 2.9 34 16.9 5.6 24.6 27.8 10.3 120 FTG - - -- PE 0.0 35 16.9 5.6 27.5 29.4 0.239 TL 12.00 PV Pipe: 45 -57.1 1.049 PL 12.00 PF 10.9 35 16.9 5.6 27.5 29.4 21.2 120 FTG - - -- PE 0.1 36 16.6 0.0 38.5 0.0 0.907 TL 12.00 PV • Pipe: 46 -57.1 1.380 PL 4.92 PF 2.6 36 16.6 0.0 38.5 0.0 12.3 120 FTG T PE 0.0 37 16.6 0.0 41.1 0.0 0.239 TL 10.92 PV Pipe: 47 -57.1 1.610 PL 1.25 PF 1.0 37 16.6 0.0 41.1 0.0 9.0 120 FTG T PE 0.5 K 15.4 0.0 42.7 0.0 0.113 TL 9.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System 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: 48 -274.9 3.068 PL 10.00 PF 0.9 K 15.4 0.0 42.7 0.0 11.9 120 FTG - - -- PE 0.0 L 15.4 0.0 43.6 0.0 0.089 TL 10.00 PV Pipe: 49 -25.4 1.049 PL 12.17 PF 2.5 38 16.9 5.6 20.6 25.4 9.4 120 FTG - - -- PE 0.0 39 16.9 5.6 23.1 26.9 0.203 TL 12.17 PV Pipe: 50 -52.4 1.049 PL 12.17 PF 9.4 39 16.9 5.6 23.1 26.9 19.4 120 FTG - - -- PE 0.0 40 16.9 5.6 32.5 31.9 0.772 TL 12.17 PV Pipe: 51 -84.3 1.380 PL 10.83 PF 8.2 40 16.9 5.6 32.5 31.9 18.1 120 FTG T PE 0.1 41 16.6 0.0 40.9 0.0 0.490 TL 16.83 PV Pipe: 52 -84.3 1.610 PL 1.25 PF 2.1 41 16.6 0.0 40.9 0.0 13.3 120 FTG T PE 0.5 L 15.4 0.0 43.6 0.0 0.231 TL 9.25 PV Pipe: 53 -359.2 3.068 PL 2.00 PF 2.5 L 15.4 0.0 43.6 0.0 15.6 120 FTG T PE 0.0 . M 15.4 0.0 46.1 0.0 0.146 TL 17.00 PV Pipe: 54 -28.8 1.049 PL 12.00 PF 3.1 . 42 16.9 5.6 26.5 28.8 10.7 120 FTG - - -- PE 0.0 43 16.9 5.6 29.6 30.4 0.256 TL 12.00 PV Pipe: 55 -59.3 1.049 PL 12.00 PF 11.6 43 16.9 5.6 29.6 30.4 22.0 120 FTG - - -- PE 0.1 44 16.6 0.0 41.3 0.0 0.971 TL 12.00 PV Pipe: 56 -59.3 1.380 PL 4.92 PF 2.8 44 16.6 0.0 41.3 0.0 12.7 120 FTG T PE 0.0 45 16.6 0.0 44.1 0.0 0.255 TL 10.92 PV Pipe: 57 -59.3 1.610 PL 1.25 PF 1.1 45 16.6 0.0 44.1 0.0 9.3 120 FTG T PE 0.5 O 15.4 0.0 45.8 0.0 0.120 TL 9.25 PV Pipe: 58 -59.3 4.026 PL 3.33 PF 0.0 O 15.4 0.0 45.8 0.0 1.5 120 FTG - - -- PE 0.0 N 15.4 0.0 45.8 0.0 0.001 TL 3.33 PV Pipe: 59 -399.5 6.065 PL 4.67 PF 0.3 N 15.4 0.0 45.8 0.0 4.4 120 FTG TL PE 0.0 M 15.4 0.0 46.1 0.0 0.006 TL 43.67 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System 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: 60 -758.7 6.065 PL 25.75 PF 1.4 M 15.4 0.0 46.1 0.0 8.4 120 FTG EA PE 6.0 P 1.5 0.0 53.5 0.0 0.021 TL 67.75 PV Pipe: 61 -758.7 6.280 PL 138.00 PF 2.2 P 1.5 0.0 53.5 0.0 7.9 140 FTG EG PE 0.6 X 0.0 0.0 56.4 0.0 0.013 TL 165.00 PV Pipe: 62 FIXED PRESSURE LOSS DEVICE Y 0.0 0.0 60.6 0.0 4.2 psi, 758.7 gpm X 0.0 0.0 56.4 0.0 Pipe: 63 -758.8 6.280 PL 16.00 PF 0.2 Y 0.0 0.0 60.6 0.0 7.9 140 FTG - - -- PE -1.3' Z 3.0 SRCE 59.5 (N /A) 0.013 TL 16.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 7.9 computer program under license no. 16061181 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 (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 0.163 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 22.1 ft /sec at pipe 24. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System • PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkV1v BfyVly GatVly A1mChk DPV1v NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 8.00 2.469 6.00 12.00 4.00 14.00 7.00 1.00 10.00 10.00 12.00 3.068 7.00 15.00 5.00 16.00 10.00 1.00 13.00 13.00 15.00 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 6.065 14.00 30.00 9.00 32.00 11.00 3.00 28.00 28.00 30.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVly BfyVly GatVly NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 • • O • ›• W C17 WATER SUPPLY ANALYSIS H •• 120.0 Static: 106.00 psi Resid: 96.00 psi Flow: 2500.0 gpm y LEGEND r' Available pressure 1 104.13 o psi @ 1008.8 gpm y o �1 Required pressure • o 2 59.47 psi @ 1008.8 gpm G_00.0 — A. Source Supply Curve H A • B. System Demand Curve U R G (0 C rt ro E n 80.0 — (D n z • r R 7n t1 7D H x1 E o n 0 S rn — K S 60.0 — 2 w w U • > 3 R (D rt n E B K r+] l7 H 7C7 ( 40.0 — Pl c w r p H >n s ro i x z 20.0 _ zK v1 a H H 7d H LT1 0.0 B x7 0 0 r'7 -14.7 I I I I I I I I > 600 900 1200 1500 1800 2100 2400 2700 3000 m ro > FLOW (GPM) •n m C7 ro SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 - DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \ROOF AREA.SDF JOB TITLE: Apex Industries, Roof System WATER SUPPLY CURVE 108+ * \ \ \ \ \\ I 0 \ \ \ \ \ \\ I \ \ \ \ \ \\ 99+ \ \ \ \ \\ I * < -96.0 psi @ 2500 gpm I Flow Test Point 1 90+ 1 1 1 81+ 1 1 1 P 72+ R I E I S 1 S 63+ U I R I X E I 54+ ( 1 P I S I I 45+ 1 1 1 36+ 1 1 1 27+ I - • I .18+ LEGEND I I X = Required Water Supply 1 59.47 psi @ 1008.8 gpm . 9+ . I 0 = Available Water Supply " 1 104.13 psi @ 1008.8 gpm " 1 0 + + - +--- + - - - -+ + + + + + + A PROFESSIONAL FIRE SYSTEMS 17272 S. STEINER ROAD BEAVERCREEK,OR 97004 HYDRAULIC CALCULATIONS • FOR Apex Industries Clean Room FILE NUMBER: Clean Room DATE: APR 9, 2009 - DESIGN DATA - OCCUPANCY CLASSIFICATION: Clean Room Per NFPA #13 DENSITY: .20 gpm /sq. ft. AREA OF APPLICATION: (Entire Area) 2451 sq. ft. COVERAGE PER SPRINKLER: 120 sq. ft. Max. NUMBER OF SPRINKLERS CALCULATED: 28 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 673.5 gpm TOTAL WATER REQUIRED (including hose): 923.5 gpm FLOW AND PRESSURE (@ BOR): 673.5 gpm @ 44.0 psi SPRINKLER ORIFICE SIZE: 1/2" inch NAME OF CONTRACTOR: A Professional Fire Systems, Co. DESIGN /LAYOUT BY: R. Berry AUTHORITY HAVING JURISDICTION: City Of Tigard CONTRACTOR CERTIFICATION NUMBER: 41650 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 16061181 ) HRS SYSTEMS, INC. TUCKER, GA A RID PRO, 4F it rso o o° � (4 LOGO SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \CLEAN ROOM.SDF JOB TITLE: Apex Industries, Clean Room WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D • NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) Z 106.0 96.0 2500.0 104.4 923.5 49.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 923.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 673.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 10.5 K= 4.95 20.7 22.5 2 10.5 K= 4.95 20.9 22.6 3 10.5 K= 4.95 21.3 22.9 4 10.5 K= 4.95 22.3 23.4 5 10.5 K= 4.95 24.1 24.3 6 10.5 K= 4.95 26.8 25.6 7 10.5 K= 4.95 30.2 27.2 _ Al 15.4 - - - - 35.1 - - - 8 10.5 K= 4.95 20.6 22.5 9 10.5 K= 4.95 20.7 22.5 • 10 10.5 K= 4.95 21.2 22.8 11 10.5 K= 4.95 22.2 23.3 12 10.5 K= 4.95 23.5 24.0 13 10.5 K= 4.95 26.8 25.6 14 10.5 K= 4.95 30.2 27.2 Bl 15.4 - - - - 35.1 - - - 15 10.5 K= 4.95 20.6 22.5 16 10.5 K= 4.95 20.8 22.6 17 10.5 K= 4.95 21.2 22.8 18 10.5 K= 4.95 22.2 23.3 19 K= 4.95 23.5 24.0 20 0 , 0 : + K= 4.95 26.9 25.7 21 31►�KD ' r' K= 4.95 30.3 27.2 Cl r o 15. - - - - 35.2 - - - 22 3 "08`. 5 p K= 4.95 20.8 22.6 23 , 10.5 K= 4.95 21.0 22.7 24 V ol K= 4.95 21.4 22.9 25 0O ��af . K= 4.95 22.4 23.5 K= 4.95 24.2 24.3 27 _ K= 4.95 26.9 25.7 28 46.1;025- 10 'r: K= 4.95 30.3 27.3 Dl 5.4 - - - - 35.3 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \CLEAN ROOM.SDF JOB TITLE: Apex Industries, Clean Room NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) M 15.4 - - - - 36.8 - - - N 15.4 - - - - 36.1 - - - P 1.5 - - - - 44.0 - - - X 0.0 - - - - 46.4 - - - Y 0.0 - - - - 50.4 - - - Z 3.0 SOURCE 49.3 673.5 • e. . I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \CLEAN ROOM.SDF JOB TITLE: Apex Industries, Clean Room 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 -22.5 1.682 PL 8.00 PF 0.1 1 10.5 5.0 20.7 22.5 3.3 120 FTG - - -- PE 0.0 2 10.5 5.0 20.9 22.6 0.016 TL 8.00 PV Pipe: 2 -45.1 1.682 PL 8.00 PF 0.5 2 10.5 5.0 20.9 22.6 6.5 120 FTG - - -- PE 0.0 3 10.5 5.0 21.3 22.9 0.059 TL 8.00 PV Pipe: 3 -68.0 1.682 PL 8.00 PF 1.0 3 10.5 5.0 21.3 22.9 9.8 120 FTG - - -- PE 0.0 4 10.5 5.0 22.3 23.4 0.126 TL 8.00 PV Pipe: 4 -91.4 1.682 PL 8.00 PF 1.7 4 10.5 5.0 22.3 23.4 13.2 120 FTG - - -- PE 0.0 5 10.5 5.0 24.1 24.3 0.217 TL 8.00 PV Pipe: 5 -115.7 1.682 PL 8.00 PF 2.7 5 10.5 5.0 24.1 24.3 16.7 120 FTG - - -- PE 0.0 6 10.5 5.0 26.8 25.6 0.336 TL 8.00 PV Pipe: 6 -141.3 1.682 PL 7.00 PF 3.4 6 10.5 5.0 26.8 25.6 20.4 120 FTG - - -- PE 0.0 7 10.5 5.0 30.2 27.2 0.486 TL 7.00 PV Pipe: 7 -168.5 1.682 PL 0.50 PF 7.1 7 10.5 5.0 30.2 27.2 24.3 120 FTG T PE -2.1 • Al 15.4 0.0 35.1 0.0 0.673 TL 10.50 PV Pipe: 8 -168.5 6.065 PL 11.33 PF 0.0 Al 15.4 0.0 35.1 0.0 1.9 120 FTG - - -- PE 0.0 Bl 15.4 0.0 35.1 0.0 0.001 TL 11.33 PV Pipe: 9 -22.5 1.682 PL 8.00 PF 0.1 8 10.5 5.0 20.6 22.5 3.2 120 FTG - - -- PE 0.0 9 10.5 5.0 20.7 22.5 0.016 TL 8.00 PV Pipe: 10 -45.0 1.682 PL 8.00 PF 0.5 9 10.5 5.0 20.7 22.5 6.5 120 FTG - - -- PE 0.0 10 10.5 5.0 21.2 22.8 0.059 TL 8.00 PV Pipe: 11 -67.8 1.682 PL 8.00 PF 1.0 10 10.5 5.0 21.2 22.8 9.8 120 FTG - - -- PE 0.0 11 10.5 5.0 22.2 23.3 0.125 TL 8.00 PV Pipe: 12 -91.1 •1.682 PL 6.00 PF 1.3 11 10.5 5.0 22.2 23.3 13.2 120 FTG - - -- PE 0.0 12 10.5 5.0 23.5 24.0 0.216 TL 6.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \CLEAN ROOM.SDF JOB TITLE: Apex Industries, Clean Room 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 -115.1 1.682 PL 10.00 PF 3.3 12 10.5 5.0 23.5 24.0 16.6 120 FTG - - -- PE 0.0 13 10.5 5.0 26.8 25.6 0.333 TL 10.00 PV Pipe: 14 -140.8 1.682 PL 7.00 PF 3.4 13 10.5 5.0 26.8 25.6 20.3 120 FTG - - -- PE 0.0 14 10.5 5.0 30.2 27.2 0.483 TL 7.00 PV Pipe: 15 -168.0 1.682 PL 0.50 PF 7.0 14 10.5 5.0 30.2 27.2 24.3 120 FTG T PE -2.1 B1 15.4 0.0 35.1 0.0 0.669 TL 10.50 PV Pipe: 16 -336.5 6.065 PL 10.67 PF 0.1 B1 15.4 0.0 35.1 0.0 3.7 120 FTG - - -- PE 0.0 Cl 15.4 0.0 35.2 0.0 0.005 TL 10.67 PV Pipe: 17 -22.5 1.682 PL 8.00 PF 0.1 15 10.5 5.0 20.6 22.5 3.2 120 FTG - - -- PE 0.0 16 10.5 5.0 20.8 22.6 0.016 TL 8.00 PV Pipe: 18 -45.1 1.682 PL 8.00 PF 0.5 16 10.5 5.0 20.8 22.6 6.5 120 FTG - - -- PE 0.0 17 10.5 5.0 21.2 22.8 0.059 TL 8.00 PV Pipe: 19 -67.9 1.682 PL 8.00 PF 1.0 17 10.5 5.0 21.2 22.8 9.8 120 FTG - - -- PE 0.0 18 10.5 5.0 22.2 23.3 0.125 TL 8.00 PV Pipe: 20 -91.2 1.682 PL 6.00 PF 1.3 18 10.5 5.0 22.2 23.3 13.2 120 FTG - - -- PE 0.0 19 10.5 5.0 23.5 24.0 0.216 TL 6.00 PV Pipe: 21 -115.2 1.682 PL 10.00 PF 3.3 19 10.5 5.0 23.5 24.0 16.6 120 FTG - - -- PE 0.0 20 10.5 5.0 26.9 25.7 0.333 TL 10.00 PV Pipe: 22 -140.9 1.682 PL 7.00 PF 3.4 20 10.5 5.0 26.9 25.7 20.3 120 FTG - - -- PE 0.0 21 10.5 5.0 30.3 27.2 0.483 TL 7.00 PV Pipe: 23 -168.1 1.682 PL 0.50 PF 7.0 21 10.5 5.0 30.3 27.2 24.3 120 FTG T PE -2.1 Cl 15.4 0.0 35.2 0.0 0.670 TL 10.50 PV - Pipe: 24 -504.6 6.065 PL 11.33 PF 0.1 Cl 15.4 0.0 35.2 0.0 5.6 120 FTG - - -- PE 0.0 - D1 15.4 0.0 35.3 0.0 0.010 TL 11.33 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \CLEAN ROOM.SDF JOB TITLE: Apex Industries, Clean Room 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: 25 -22.6 1.682 PL 8.00 PF 0.1 22 10.5 5.0 20.8 22.6 3.3 120 FTG - - -- PE 0.0 23 10.5 5.0 21.0 22.7 0.016 TL 8.00 PV Pipe: 26 -45.3 1.682 PL 8.00 PF 0.5 23 10.5 5.0 21.0 22.7 6.5 120 FTG - - -- PE 0.0 24 10.5 5.0 21.4 22.9 0.059 TL 8.00 PV Pipe: 27 -68.2 1.682 PL 8.00 PF 1.0 24 10.5 5.0 21.4 22.9 9.8 120 FTG - - -- PE 0.0 25 10.5 5.0 22.4 23.5 0.126 TL 8.00 PV Pipe: 28 -91.6 1.682 PL 8.00 PF 1.7 25 10.5 5.0 22.4 23.5 13.2 120 FTG - - -- PE 0.0 26 10.5 5.0 24.2 24.3 0.218 TL 8.00 PV Pipe: 29 -116.0 1.682 PL 8.00 PF 2.7 26 10.5 5.0 24.2 24.3 16.7 120 FTG - - -- PE 0.0 27 10.5 5.0 26.9 25.7 0.337 TL 8.00 PV Pipe: 30 -141.6 1.682 PL 7.00 PF 3.4 27 10.5 5.0 26.9 25.7 20.5 120 FTG - - -- PE 0.0 28 10.5 5.0 30.3 27.3 0.488 TL 7.00 PV Pipe: 31 -168.9 1.682 PL 0.50 PF 7.1 28 10.5 5.0 30.3 27.3 24.4 120 FTG T PE -2.1 D1 15.4 0.0 35.3 0.0 0.676 TL 10.50 PV Pipe: 32 -673.5 6.065 PL 15.67 PF 0.8 D1 15.4 0.0 35.3 0.0 7.5 120 FTG T PE 0.0 N 15.4 0.0 36.1 0.0 0.017 TL 45.67 PV Pipe: 33 -673.5 6.065 PL 4.67 PF 0.7 N 15.4 0.0 36.1 0.0 7.5 120 FTG TL PE 0.0 M 15.4 0.0 36.8 0.0 0.017 TL 43.67 PV Pipe: 34 -673.5 6.065 PL 25.75 PF 1.1 M 15.4 0.0 36.8 0.0 7.5 120 FTG EA PE 6.0 P 1.5 0.0 44.0 0.0 0.017 TL 67.75 PV Pipe: 35 -673.5 6.280 PL 138.00 PF 1.8 P 1.5 0.0 44.0 0.0 7.0 140 FTG EG PE 0.6 X 0.0 0.0 46.4 0.0 0.011 TL 165.00 PV Pipe: 36 FIXED PRESSURE LOSS DEVICE Y 0.0 0.0 50.4 0.0 4.0 psi, 673.5 gpm X 0.0 0.0 46.4 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \CLEAN ROOM.SDF JOB TITLE: Apex Industries, Clean Room 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: 37 -673.5 6.280 PL 16.00 PF 0.2 Y 0.0 0.0 50.4 0.0 7.0 140 FTG - - -- PE -1.3 Z 3.0 SRCE 49.3 (N /A) 0.011 TL 16.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 7.9 computer program under license no. 16061181 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 (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 0.063 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 24.4 ft /sec at pipe 31. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVly BfyVly GatV1v AlmChk DPV1v NPTee 6.065 14.00 30.00 9.00 32.00 11.00 3.00 28.00 28.00 30.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVly BfyVly GatVly AlmChk DPV1v NPTee 1.682 5.00 10.00 3.00 11.00 8.00 1.00 12.00 12.00 10.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVly BfyVly GatVly NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 � t7 o > W C+] WATER SUPPLY ANALYSIS y •• 120.0 Static: 106.00 psi Resid: 96.00 psi Flow: 2500.0 gpm y A LEGEND r Available pressure 1 104.42 psi @ 923.5 gpm o l� 1 Required pressure m ko 2 49.26 psi @ 923.5 gpm k 100.0 A. Source Supply Curve H G B. System Demand Curve A cr) W U rt ' G N H M •• z E80.0 -n 7or p 0 0 m x R m - O W 1-C E W S x > m 5 60.0 o r U x R 2 r m E m > W C r ( 40.0 roc p x > S H z i z r K C W W H 20.0 W H C+7 W 0 0.0 B z 0 o ro 3 a • w -14.7 I I I I W `° 600 900 1200 1500 1800 2100 2400 2700 3000 "I FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \CLEAN ROOM.SDF JOB TITLE: Apex Industries, Clean Room WATER SUPPLY CURVE 108+ * \ \ \ \ \\ I 0 \ \ \ \ \ \\ I \ \ \ \ \ \\ 99+ \ \ \ \ \\ I * < -96.0 psi @ 2500 gpm Flow Test Point 90+ 81+ 1 1 P 72+ R I E 1 S I S 63+ U I R 1 E I 54+ ( 1 P I X S I I 45+ • ) I 36+ 1 27+ 1 18+ LEGEND I " I X = Required Water Supply I 49.26 psi @ 923.5 gpm 9+ I 0 = Available Water Supply " • I 104.42 psi @ 923.5 gpm " 1 0 + +- +--- + - - - -+ + + + + + + 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 4/9/2009 C: \RICK'S CALC FILES \APEX INDUSTRIES \CLEAN ROOM.SDF JOB TITLE: Apex Industries, Clean Room Utility Report: • Equivalent K- Factor Calculator Node Sprinkler Pres. Dia. Pipe Ftgs. Total H -W Equivalent Name K- Factor (psi) (in) Len.(ft) Len.(ft) coef. K- factor Flowing 5.60 11.76 1.049 20.42 ET 27.42 120.00 4.95 , . . +� ::.::::::.:::.:::.:::: PREMIER FLEX BLE STAINLESS TUBING ;: :..,::::: ' >; .:: ;;: »: :; SIDENiNDER ::: :::::;1:::. : s: .. OGATEWAr :::::::::i!:i:::::::::::,g::::::::::u::::::0)„,)„,:,,,-0„::::::,,,,,,:::.:::,;:i,:::i,i,i,i,,i,: : :: :. : :i:; :: SPRINKLER DROP P.O. Box G40 >:.. :::::::::::;�;:. >:: ;;:.:.:;.:<.:<.; ::. <.::.;::;:.::.;:.: Rolla, Missouri 65402 ::::::�j :: il;Ili;:::N :s. ;:.16 :1:: %; 1- 800 -554 -3539 • 573- 364 -2930 (facsimile) e `o @evaytubing.com • www.gatewaytubing.com • Introduction Model' :` :Tubing Length : ed m ucer Dia IP Gateway Tubing's SidewinderTM 230 (DASPNO1A) 30" %z sprinkler drop connects the "Fs 248 (DASPNO2A) 48" 1 /z" branch line to the sprinkler head 260 (DASPNO3A) 60" 1/2" using a flexible stainless steel. 330 (DASPNOIB) 30" 3 /4 " tube and reducer. Each 348 (DASPNO2B) 48" 3 /4 " SidewinderrM assembly installs quickly and is designed to save 360 (DASPNO3B) 60" 3 /4" costs and speed project Table 1 - SidewinderTM Model Numbers completion. It is particularly Parts Included codes. Any failure to comply with suited for use with suspended Each SidewinclerTM assembly any such requirement or ceilings, as the flexible tube bends consists of the following parts: standard, or any failure to comply by hand for placement of every one-piece stainless steel flexible with the instructions and sprinkler head in the precise tube and reducer ready to mount recommendations contained in center-of-tile of the suspended to branch line; one square tube this document will void any ceiling. c. 52" in length; two ceiling grid warranty made by Gateway SidewinderTm drops are available clamps which suspend the square Tubing, Inc. in three different lengths: 30 ", 48" tube above the ceiling grid; one and 60 ". Each length is available reducer clamp which connects the Step 1: Connect the nipple to the in two different sizes for reducer reducer to the square tube; and branch line using the wide, NP' threading: Y2" and 3 /" NPT one nipple which connects the threads of the nipple. Figure 1. thread. Each SidewinderTM drop is branch line to the flexible tubing. Apply a nonharclening pipe joint UL listed and approved by the compound or Teflon tape to the New York City MEA Department Friction Loss Data NPT male threads of the nipple. of Buildings. Table 2 (below) shows the Tighten firmly with pipe wrench hydraulic friction loss expressed for leak proof connection. in terms of the average equivalent Technical Data length of Schedule 40 steel pipe. ' Product Identification Installation Gateway's SidewinderTM drops are •t available in 6 different models, Each SiclewinderrM assembly must "mismo" ' T• — C- depending on the length of the be installed according to NFPA 13 ��' ' ` ` sprinkler drop and diameter of the reducer needed. See Table 1. standards and local government Figure 1 requirements, standards and Maximum Working Pressure: 175 PSI Average Equivalent Length (in feet) of Temperature Rating: 225 °F Model 1" Schedule 40 Pipe IP Connection to Branch Line: 230 16.5 1 "NPT 248 30.7 Minimum Bend Radius of 260 39.2 Flexible Tube: 3 inches. Do not 330 19.7 bend within 21/2 inches of 348 31.0 connection nut or reducer. 360 35.0 Maximum number of bends in Table 2 - Friction loss data one flexible tube: 3 tqct3 Fire & Building Products Technical Services: Tel: (800) 381 -9312 / Fax: (800) 791 -5500 Series TY -FRB — 2 . 8 , 4.2, 5 and 8.0 K- factor Upright, Pendent, and Recessed Pendent Sprinklers Quick Response, Standard Coverage tained when exposed to corrosive at- G eneral mospheres. Although corrosion resis- tant coated sprinklers have passed the D escription standard corrosion tests of the appli- =a ;`�'; " cable approval agencies, the testing is -s _ The Tyco® Series TY -FRB, 2.8, 4.2, not representative of all possible cor- 5.6, and 8.0 K- factor, Upright and Pen- rosive atmospheres. Consequently, it Mt I dent Sprinklers described in this data is recommended that the end user be ' sheet are quick response - standard consulted with respect to the suitability 1 coverage, decorative 3 mm glass bulb of these coatings for any given corro- ` type spray sprinklers designed for use sive environment. The effects of ambi- in light or ordinary hazard, commercial ent temperature, concentration of .� occupancies such as banks, hotels, chemicals, and gas /chemical velocity, -- shopping malls, etc. should be considered, as a minimum, The recessed version of the Series along with the corrosive nature of the TY -FRB Pendent Sprinkler, where ap- chemical to which the sprinklers will be plicable, is intended for use in areas exposed. �� with a finished ceiling. It uses either a An intermediate level versions of the two -piece Style 10 (1/2 inch NPT) or Series TY -FRB Pendent Sprinklers Style 40 (3/4 inch NPT) Recessed Es- are detailed in Technical Data Sheet ( I N cutcheon with 1/2 inch (12,7 mm) of TFP356, and Sprinkler Guards are de-{ ; 40 , i recessed adjustment or up to 3/4 inch tailed in Technical Data Sheet TFP780 (19,1 mm) of total adjustment from the flush pendent position, or a two -piece WARNINGS r Style 20 (1/2 inch NPT) or Style 30 (3/4 The Series TY -FRB Sprinklers de- .. ', inch NPT) Recessed Escutcheon with scribed herein must be installed and '...r9.1" 1/4 inch (6,4 mm) of recessed adjust- maintained in compliance with this ment or up to 1/2 inch (12,7 mm) of document, as well as with the applica- total adjustment from the flush pen- ble standards of the National Fire Pro - dent position. The adjustment pro- tection Association, in addition to the vided by the Recessed Escutcheon re- standards of any other authorities hav- Model /Sprinkler duces the accuracy to which the fixed ing jurisdiction. Failure to do so may pipe drops to the sprinklers must be impair the performance of these de- Identification cut. vices. Corrosion resistant coatings, where The owner is responsible for maintain- Numbers applicable, are utilized to extend the ing their fire protection system and de- life of copper alloy sprinklers beyond vices in proper operating condition. TY1131 - Upright 2.8K, 1/2 "NPT that which would otherwise be ob- The installing contractor or sprinkler TY1231 - Pendent 2.8K, 1/2 "NPT manufacturer should be contacted TY2131 - Upright 4.2K, 1/2 "NPT IMPORTANT with any questions. TY2231 - Pendent 4.2K, 1/2 "NPT TY3131 - Upright 5.6K, 1/2 "NPT Always refer to Technical Data TY3231 - Pendent 5.6K, 1/2 "NPT Sheet TFP700 for the "INSTALLER TY4131 - Upright 8.0K, 3/4 "NPT WARNING" that provides cautions TY4231 - Pendent 8.0K, 3/4 "NPT with respect to handling and instal- TY4831- Upright 8.0K, 1/2 "NPT lafion of sprinkler systems and com- TY4931- Pendent 8.0K, 1/2 "NPT ponents. Improper handling and in- stallation can permanently damage a sprinkler system or its compo- nents and cause the sprinkler to fail to operate in a fire situation or cause it to operate prematurely. tL,CO IFire & Building Products Technical Services: Tel: (800) 381 -9312 / Fax: (800) 791 -5500 Series T -L — 5.6 and 8.0 K- factor Uprigh Pendent, and Recessed Pendent Sprinklers Standard Response, Standard Coverage General rosive atmospheres. Consequently, it is recommended that the end user be . , VW consulted with respect to the suitability Description of these coatings for any given corro- ` • ` .ti: -' sive environment. The effects of ambi- The Series TY L, 5.6 and 8.0 K- factor, ent temperature, concentration of .2-__.; Upright and Pendent Sprinklers de- chemicals, and gas /chemical velocity, : 1 , scribed in this data sheet are standard should be considered, as a minimum, Vii ' . response - standard coverage, solder along with the corrosive nature of the , type spray sprinklers designed for use chemical to which the sprinklers will be _ - ' in light, ordinary, and extra hazard, exposed. .— -, commercial occupancies such as banks, hotels, shopping malls, facto- An intermediate level version of the ries, refineries, chemical plants, etc. Series TY L Pendent Sprinkler can be obtained by utilizing the Series TY L The recessed version of the Series Pendent Sprinkler in combination with TY -L Pendent Sprinkler, where appli- the Model S Shield. cable, is intended for use in areas with a finished ceiling. It uses a two -piece WARNINGS Style 20 (1/2 inch NPT) or Style 30 (3/4 The Series TY -L Sprinklers described inch NPT) Recessed Escutcheon. The herein must be installed and main - Recessed Escutcheon provides 1/4 tained in compliance with this docu- ' inch (6,4 mm) of recessed adjustment ment, as well as with the applicable t- r or up to 1/2 inch (12,7 mm) of total standards of the National Fire Protec- 1 adjustment from the flush pendent po- tion Association, in addition to the sition. The adjustment provided by the standards of any other authorities hay- N. Recessed Escutcheon reduces the ac- ing jurisdiction. Failure to do so may curacy to which the fixed pipe drops to impair the performance of these de- ' t_ the sprinklers must be cut. vices. Corrosion resistant coatings, where The owner is responsible for maintain - applicable, are utilized to extend the ing their fire protection system and de- life of copper alloy sprinklers beyond vices in proper operating condition. that which would otherwise be ob- The installing contractor or sprinkler tained when exposed to corrosive at- manufacturer should be contacted TY4811 - Upright 8.0K, 1/2 "NPT mospheres. Although corrosion resis- with any questions. TY4911 - Pendent 8.0K, 1/2 "NPT tant coated sprinklers have passed the standard corrosion tests of the appli- TY3111 is a redesignation for S1800 cable approval agencies, the testing is and G3111. not representative of all possible cor- Model /Sprinkler TY3211 is a redesignation for S1801 and G3112. IMPORTANT Identification TY4111 is a redesignation for S1810 Always refer to Technical Data Numbers and G3101.. Sheet TFP700 for the "INSTALLER TY4211 is a redesignation for S1811 WARNING" that provides cautions TY3111 - Upright 5.6K, 1/2 "NPT and G3102. with respect to handling and instal - TY3211 - Pendent 5.6K, 1/2 "NPT ' lation of sprinkler systems and corn- TY4111 - Upright 8.0K, 3/4 "NPT TY4811 is a redesignation for S1805. ponents. Improper handling and in- TY4211 - Pendent 8.0K, 3/4 "NPT TY4911 is a redesignation for S1806 stallation can permanently damage . a sprinkler system or its compo- nents and cause the sprinkler to fail to operate in a fire situation or cause it to operate prematurely.