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HomeMy WebLinkAbout3717 Orlando Dr 21025 Plans Sprinklers LuriasVESTA TRANSMITTAL LETTER FIRE PROTECTION 1870 N. Rio Grande Ave. Orlando, Florida 32804 DATE: July 7, 1986 305-425-2548 PROJECT: Luria's @eminole Center Sanford Fire Prevention Bureau 3717 Orlando Ave. 1303 S. French Ave. Sanford, Florida Sanford, FL 32771 ATTN: Michael Hoening Our Contract No. 8632 WE TRANSMIT HEREWITH FOR YOUR — INFORMATION CORRECTION APPROVAL RETURN QUOTATION 6 - Prints of drawing no. 1 of 1: ith P.E. stamp of review. 6 - Sets of hydraulic calculations each floor. SINCERELY, U Louis H. Mirenda z HYDRAULIC SUMMARY SHEET NAME I ALS DATE - T' 3 LOCAT ION -58 N FOWD.,L.o BUILDING SYSTEM NO. 2AJA, FG, CONTRACTOR CONTRACT NO. 3Z CALCULATED BY o11 DRAWING NO. CONSTRUCTION: COMBUSTIBLE -COMBUSTIBLE CEILING HEIGHT /0 LO FT. OCCI PANCY I 5KNFPA 13: LT. HAZ. ORD. HAZ. GP. 1 2/2 3 EX. HAZ. Z NFPA 231 NFPA231C: FIGURE CURVE C7 OTHER (Specify) w SPECIFIC RULING MADE BY DATE 0 w w AREA OF SPRINKLER OPERATION O 3xSTFM TYPE DENSITY a WET DRY DELUGE PRE -ACTION AREA PER SPRINKLER ZD 40 HOSE ALLOWANCE GPM: INSIDE MAKE V1 ING' —MODEL HOSE ALLOWANCE GPM: OUTSIDE ZSD SIZE 1 "' K-FACTOR s• RACK -SPRINKLER ALLOWANCE TEMPERATURE RATING /5"5° CALCULATION GPM REQUIRED 3 00m 9 PSI REQUIRED 35115 AT BASE OF RISER . SUMMARY C" FACTOR USED: OVERHEAD ZZ-0 UNDERGROUND /4'0 J WATER FLOW TEST DATE & TIME 7'2-8(o•'30P/1 PUMP DATA RATED CAPACITY TANK OR RF ERVOIR CAPACITY a STATIC PSI SO AT PSI ELEVATION j RESIDUAL PSI 30 ELEVATION co GPM, FLOWING 770 WELLCr ELEVATION Z L&I, PROOF F LOW GPM Q LOCATION D N DN mop SOURCE OF INFORMATION COMMODITY CLASS LOCATION w STORAGE HEIGHT AREA AISLE WIDTH O Q STORAGE METHOD: SOLID PILED % PALLETIZED 96 RACK 96 0 I- SINGLE ROW CONVENTIONAL PALLET AUTOMATIC STORAGE ENCAPSULATED DOUBLE ROW SLAVE PALLET SOLID SHELVING NON- MULTIPLE ROW OPEN ENCAPSULATED 0 Y FLUE SPACING IN INCHES CLEARANCE FROM TOP OF STORAGE TOCEILINO LONGITUDINAL TRANSVERSE FT. IN. v HORIZONTAL BARRIERS PROVIDED ABBREVIATIONS USED IN CALCULATIONS O . PLOW INCRKMMNT AT SPECIFIC LOCATION - T . TEE -FLOW TURNED SO' O . PLOW AT A SPECIFIC LOCATION- C - CROSS -FLOW TURNED 600 O.P.M.. GALLONS PIER MINUTE 0ILL.V. • DELUGE VALVE P.O.[.. POUND PER OOUARE INCH O.P.V.. DRY PIPE VALVE PT TOTAL PRCOSURE IN P.O.I. AL.V. - ALARM VALVE PP . PRESSURE LOOS OUR TO FRICTION OV GATE VALVE PE . PRESSURE CHANGE OUR TO ELEVATION CV SWING CHECK VALVE PN . PRESSURE NORMAL AV - ANGLE VALVE PV . PRESSURE VELOCITY GLV GLOOM VALVE EE 41DO ELBOW - ST . STRAINER E . 90' ELBOW - OPP . BACKFLOW PRKVBNTER L.T.E.. LONG TURN ELBOW - DCV DETECTOR CHECK VALVE TW - THIN.WALL PIPE - - BY . BUTTERFLY VALVE MULTIPLY SCALE BY D Z o D O O 3 Z m-4 n co"- a 0 tY to Y 1 t y- fi i0 T. a s i1 W NI Ul co o a oco w GPM 43 F I RENET HYDRAULIC ANALYSIS OF A FIRE PROTECTION SPRINFLER SYf VERSION i - JULY 1984 I DATE FOR THIS COMPUTER RUN = 7-5-86 ID FOR' THIS COMPUTER RUN = LURIA2 INPUT DATA FILE NAME = LUR I A2 OUTPUT DATA FILE NAME = 8632 I SPRINKLER SYSTEM DATA SUMMARY WATER SUPPLY CHARACTERISTICS: STATIC PRESSURE = 50 PSI RESIDUAL PRESSURE = 30 PSI RESIDUAL FLOW = 790 GPM ELEVATION OF PRESSURE GAGE ,.= 2.5 FT. FLOW REQUIREMENTS: OUTSIDE HOSE FLOW REQUIREMENT CAT SUPPLY) _ 250 GPM INSIDE HOSE FLOW REQUIREMENT CAT LOCATION U o GPM TOTAL SPRINKLER SYSTEM FLOW REQUIRED (BASE OF RISER) _ 0 GPM SPRINKLER INFORMATION MAXIMUM SPACING OF SPRINKLER HEADS 10 F•"f . MAXIMUM SPACING OF BRANCH LINES = 12 FT. REQUIRED MINIMUM FLOW (PER SPRINKLER) _ 22.8 GPM REQUIRED MINIMUM FLOW DENSITY = .19 GPM/SQ. FT. OTHER SPRINKLER SYSTEM DATA. - DEFAULT VALUE FOR C-FACTOR = 120 NUMBER OF BOOSTER PUMPS ,= U SUMMARY OF SPRINKLER OPERATION: SPRINKLER CONSTANT.- 5.6 LOCATION OF OPERATING SPRINKLERS: 65 66 67 LOCATION OF OPERATING SPRINKLERS: 73 74 75 76 77 LOCATION OF OPERATING SPRINKLERS 83 - 84 85 86 87 i yy y ,y ,y y.y y ,l..!' ,y.y y. ,!y, ,y.y .,y y y y ,I• ,y .,y y yy y f - 1'•••T+F•+r•?••1•:.#.::$.:*.:#:r{,:..#.ry:::#..%:.#:'....y.•?••#•••Y•••r.•#••T••T••T•T•7•:'.#:.#:••?•••r•ri+FTMR••T••7L•:.•••••••t• .. I HYDRAULIC ANALYSIS WITH REQUIRED FLOW AT REMOTE HEAD *4:4.3 34-:#:SUMMARY OF SPRINKLER SYSTEM OPERATION**** o THE F"OLLOW I NG SPRINKLERS ARE OPERATING LOCATION SPRINKLER K' ELEVATION FLOW PRESSURE. i 65 5.60 26.50 23.87 18.17 Le 5.60 26.50 23.84 18.13 67 5.60 26.50 23. 88 l e. 19 i 73 5.60 26.5U 23.12 17.05 7.4 5.60 26.50 22.87 16.67 75 5.60 26.5o 22.83 16.61 76 5.60 26.50 22.85 16.65 77 5.60 26.50 213.06 16.95 f 83 5.60 26.50 23.10 17.'01 84 5.6U 26.50 22.84 16.64 85 5.60 26.50 22.80 16.58 i uC5.60 26.50 "2'2.82 16.61 . 8 7 5.60 26.50 23.03 116.912 THE TOTAL SPRINKLER FLOW DELIVERED = 300.9 GPM 1+ iE OUTSIDE HOSESTREAM FLOW OF 250 GPM OPERATES.AT 39.74 PSI i s THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.150 GPM/SO FT i WATER SUPPLY CHARACTERISTICS LOCATION Al" PIPE NO 1 Sl" ATIC PRESSURE _ 50 PSI RESIDUAL PRESSURE = 30 PSI AT 790 GPM OPERATING PRESSURE _ 34.5 PST 1 AVAILABLE PRESSURE = 3-3.74 PSI AT 550.88 GPM i EXCESSIVE ( OR REQUIRED) SUPPLY PRESSURE _ 5.23 PSI 7'• m•'%IY.t•I•1••••i•fi••i'i•i•i••iT•T•T•i•i%•i•T!h•i••!'!Tm7'!•.+i4•'h••*••i•i•7'•/. •i'•i•Jii••T!m 1 y..#..• t..}.T•+t••T•7+T•7•T•.'r.•T••N.1•T•T•T•#•.?•T•TAT••TTT?•+h•.1'•.T.#..•ri•T•(T TT`F AT T+f`•T•.#. .•.#..#..... 1 SUMMARY OF HYDRAULIC CALCULATIONS i y NODES FLOW P IPE EOV ., H-W : D IA. PSI / ELEV . START VEND FROM -TO GPM) FT.) FT G- IN. 100-FT PSI.- PSI. PSI. . PSI. 1 10 3cJU . 88 U-, c JU 48. 38- 15cJ-- 7. '8- c0.07 J . VcJ. 3J . 59--..,5. 5---.^ J. 1` 10 11 300.88 12.50 22t. UU 1.:.0 4..=6 2 14 Gv. '' C. AAA) t.:33 6. 1S 11 21 00. 88 14.00 0.00 120 4.26 2.14 6. 07 29.39 23.02 6.37 21 22 300.88 2.17 10.00 120 4.26 2.14 0.00 23.02 22.76 0.26 22 31 58.55 5 15.00 120 3.26 0.38 0.00 22.76 22.68 0.08 22 32 242.33 4.50 15.00 120 3. L6 5.27 0.00 22.76 21.74 1.03 30 31 28.19 7.00 0.00 120 3.26 0.10 0.00 22.68 22.68 0.01 32 33 218.31 12.00 0.00 120 3.26 4.34 0.00 21.74 21.22 0.52 33 34 197.92 12.00 0.00 120 3.26 3.62 0.00 21.22 10.73 0.43 34 35 180.46 12.00 0.06 120 3.26 3405 0.00 20.70 20. 4'2 0.37 36 37 152.83 12.00 ovoo 120 3.26 2.24 0.00 20.07 19.8 i 0.27 37 38 118.52 12.00 0.00 120 3. 26 1.40 0.00 19. 80 19.64 0 A 7 38 39 59.22 12.00 0.00 126 3.26 0.39 0.00 19.64 19.59 0.05 35 36 166. 86 13.00 0.00 120 3.16 2.64 0.00 20; 42 20107 0.34 4o 41 28. 19 1 1 .00 0.00 120 3.26 0.10 0.00 20.13 20.12 0.01 41 42 58.55 11.00 0.00 120 3.26 0.30 0.06 20.12 20.08 0.04 42 43. 82.57 12.00 0.00 120 3.26 0.72 0.00 20.08 19.99 0.09 43 44 102.96 12.00 0.00 120 3.26 1.08 0.00 19.99 19.86 0.13 44 45 120.43 12.00 0.00 120 3.26 1.44 0.06 19.86 19.69 0.17 46 47 148. o3 12.00 0.00 120 3.26 2.11 0.00 19.46 Q. 21 0. 2 S 17 48 110.79 12VOO 0.00 120 3.26 1.24 0.00 19.21 19.06 0.15 48 49 55.37 12.00 0.00 120 3.26 0.34 0.00 19.06 19.02 0.04 45 46 134.02 13.00 0.00 120 3.26 1.76 0,00 19. 69 19.46 0.23 3U 4o 28..19 85.00 21.00 120 1.69 40 0.00 22.68 20.13 2.55 3.1 41 00.37 81.00 12.00 120. 1.69 0.76 0.00 22.68 20.12 2.56 32 42 24.02 81.00 12.00 120 1.69 1.79 0.00 21..74 20.08 1.66 33 43 20.39 81.00 12.00 120 1 .6 9 1.32 0.00 21.22 19.99 1.23 34 44 17.47 81.00 12.00 120 1.69 0.99 0.00 20.78 19.86 0.92 36 46 14.03 81.00 12.00 120 1.69 0.66 0.00 20.07 19.46 0.61_ 35 45 13.59 85.00 32.00 120 1.69• 0.E2 0.00 20.42 19.69 0.73 37 61 34.31 1.08 6.00 120 1.69 3.46 6.00 19. BO 19.56 0.04 30 71 59.31 1.08 6.00 120 1.69 9.53 0.00 19.64 18.96 0.67 39 81 59.2 1-08 6.00 110 1.69 9.50 0.00 19.59 18.92 0.67 47 69 37.26 1.00 6.00 120 1.69 4.03 0.00 AM, 18. 92 0. 28 48 79 55.41 1.0p 6.00 120 1.69 8.40. 0.00 19.06 18.47 0.59 49 89 55.37 1.00 6.00 120 1.69 8.39 0.00 19.02 18.43 0.59 i 61 62 34.31 10.00 0.00 120 1.69 3.46 0.00 19.56 19.21 0.35 62 63 34.31 10.00 0.00 120 1.69 3.46 0.00 19.21 18.87 0.35 63 64 34.31 10.00 0.00 120 1.69 3.46 0.00 18.87 18.52 0.35 64 65 34.31 10.00 0.00 120 1.69 3.46 0.00. 18.52 i8.i8 0.35 65 66 10.45. 10.00 0.00 120 1.69 U.38 0.00 18.18 Q.14 0.04 66 67 13.39 10.00 0.00 120 1.69 0.61 0.00 16.14 18.20 0.06 67 68 37. 26 10.00 0.00 120 1069 4.03 0.00 18.20 18. 60 . 0. 40 71 72 59.31 10.00 0.00 120 1.69 9.53 0.00 18.96 18.01 0.95 72 73 59.31 10.00 0.00 120 1.69 9.53 0.00 18.01 17.06 0.95 73 74 36.18 10.00 0.00 120 1.69 3.81 0.00 17.06 16.67 0.38 74 75 13.32 10. 00 0- 0Q 120 1. 60 0.60 6.00 16.67 16.61 0.06 75 76 9.5i 10.00 0;00 120 1.69 0.32 0.00 16.61 16.65 0.03 76 77 32.36 10.00 0.00 120 1.69 3.10 0.00 16.65 16.96, 0.31 ` 77 78 55.41 10.00 0.00 120 1.69 8.40 0.00 16.96 17.80 0.84 81 82 59.22 10.00 0.00 12/ - 1.69 9~50 0.00 18.92 1/.97 A 95 82 83 59.~2 10.00 0.00 120 1.69 9.50 00` 17.97 1'.02 0.95 ' 83 84 36.12 10.00 0.V0 120 1.69 3~80 0.00 17.02 16.64 0.38 84 85 13.28 10.00 0.00 120 1,69 8.60 0.00 16.64 16.58 0.O6 85 86 9.52 10.00 0.00 120 1~69 0.32 0.00 16.58 16.61 0.03 86 87 32.34 10.00 0,00 120' 1.69 3,10 0.0() 16~61 16.92 0.31 87 88 55,37 10.80 0.00 120 1.69 8.39 0.00 16.92 17.76 0.84 68 69 37.26 8.00 ` 0.00 120 1.69 4.n3 0. 'O 18.0 18.92 0.32 78 79 55.41 8.0o 0.00 120 1.69 8.40 0.00 17.80 18.47 0.67 88 89 55.37 8.00 0.00 120 1.69 8.39 0.00 17,,76 18.43 0.67 THE MAXIMUM VELOCITY OF 9.31 FT/8 OCCURS BETWEEN NODES 22 AND 32 HYDRAULIC CALCULATIONS ACCURACY CHECKS (UNBALANCEDPRESSURE IN LOOPS): LOOP # 1 - NODES: 32 42 41 31 22 32 UNBALANCED PRESSURE = 0.0004 PSI LOOP # 2 - NODES: 40 41 31 30 40 UNBALANCED PRESSURE = 0°00V0 PSI LOOP # 3 - NODES: 42 43 33 32 42 UNBALANCED PRESSURE = 0.0002 PSI LOOP # 4 - NODES: 43 44 34 33 43 UNBALANCED PRESSURE = 0.0002 PSI LOOP # 5 - NODES: 44 4535 34 44 UNBALANCED PRESSURE = 0.0002 PSI LOOP # 6 - NODES: 46 47 69 68 67 66 65 64 63 62 61 37 36 46 UNBALANCED PRESSURE 0.0029PSI LOOP # 7 - NODES: E.1 62 63 64 65 66 67 68 69 47 48 79 78 77 76 75 74 73 72 71 38 37 61 UNBALANCED PRESSURE = 0.0004 PSI i LOOP # 8 - NODES: 71 72 73 74 75 76 77 78 79 48 . 49 89 Be 87 ' 8G, 85 84 83 82 81 39 38 71 ! UNBALANCED PRESSURE = 0,0000 PSI LOOP # 9 - NODES: 45 46. 36 35 45 UNBALANCED PRESSURE = 0.0028 PSI SPRINKLERCONSTANT = 5. 6 LOCATION OF OPERATING SPRINKLERS: - 64 65 66 ' LOCATION OF OPERATING SPRINKLERS: 72 7374 75 76 LOCATION OF OPERATING SPRINKLERS: 82 83 84 85 86 HYDRAULIC ANALYSIS WITH REQUIRED..FLOW AT..REMOTE HEAD SUMMARY OF SPRINKLER SYSTEM OPERATION**** THE FOLLOWING SPRINKLERS ARE OPERATING LOCATION SPRINKLER K ELEVATION FLOW PRESSURE G4 5. 60 26.50 23.77 18.02 65 5. GU 26.50 23. 73 17.96 GG 5.6o 26.5U. 23.76 18.01 7: 5.60 26.50. 23.26 17.25 73 5.6U 26. 5U 22.91 1E.74 74 5.60 26.50 2.83 16.62 75 5.60 26. 5o 22.83 16.62 76 5.60 26.50 22.97 1E.82 821 5.60 26.5U 3.:_3 17.21 83 5.60 26.50 . 22. 88 16.701 84 5.60 26.50 22.8o 16.58 85 5.60 26.50 22. E30 16.58 86 5. 6U 26.50 22.9494 16.79 THE TOTAL SPRINKLER FLOW DELIVERED = 300.72 GPM THE OUTSIDE HOSESTREAM FLOW OF 250 GPM OPERATES AT 39.74 PSI THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.190 GPM/SO FT WATER' SUPPLY CHARACTERISTICS LOCATION AT PIPE NO 1 STATIC PRESSURE = 50 PSI RESIDUAL PRESSURE = 30 PSI AT 790 OPERATING PRESSURE = 34.3 PSI AVAILABLE PRESSURE = 39.74 PSI AT GPM 550.6.9 GPM 434-4.4444* EXCESSIVE (OR REQUIRED) SUPPLY PRESSURE = 5.44 PSI :#:*:#::#::#::#::#.4.3: HYDRAULIC ANALYSIS WITH REQUIRED FLOW AT REMOTE HEAD -*** SUMMARY OF SPRINKLER SYSTEM O TION**. THE FOLLOWING SPRINKLERS ARE OPERATING nr ATION SPRINKLER K ELEVATION FLOW PRESSURE 66 5 G0 26 50 2 3.84 18.13 67 5.60 26.50 23.82 18.10 68 5.60 26.50 23.87 18,18 74 . 5~60 ' 26.50 23.02 16.90 75' 5.60 26.50 22.84 16.63 76 5,60 26.50 22.83 16.62 77 5.60 26.50 22.88 1 70 78 5.60 26 50 23^17 1=^12 84 5.60 26.50 23.00 16.86 85 5-60 ` 26.50 .22,81 16.60 86 5.60 26.50 ` 22.80 16.58 87 5,60 26.50 22.85 16.66 88 5.60 26,50 23.14 17,08 THE TOTAL SPRINKLER FLOW DELIVERED 300.89 GPM THE OUTSIDE HOSESTREAM FLOW OF 250 GPM OPERATES AT 39,74 PSI THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.190 GPM/SQ T WATER SUPPLY CHARACTERISTICS LOCATION AT PIPE NO 1 STATIC PRESSURE = 50 PSI RESIDUAL PRESSURE = 30 PSI AT j90 GPM OPERATING PRESSURE = 34.44 PSI . ' AVAILABLE PRESSURE 39 4 PSI AT 550.86 GPM EXCESSIVE (OR REQUIRED) SUPPLY E = 5.29 PSI Jr Y/NFPA 13: LT. HAZ. ORO. HAZ. GP. 1 [jj(2 3 EX. HAZ. Z NFPA 231 NFPA 231C: FIGURE CURVE t7 OTHER (Specify) W SPECIFIC RULING MADE BY DATE 0 W AREA OF SPRINKLER OPERATION 0 SYSTEM TYPE N ai DENSITY _/9 -' AREA PER SPRINKLER t ZO > WET DRY DELUGE PRE -ACTION SPRINKLER HOSE ALLOWANCE GPM: INSIDE OR NOZZLE MAKE VJ MLN.-6r MODEL 4^9T1C- HOSE ALLOWANCE GPM: OUTSIDE 150 SIZE Vz. K-FA TOR RACK SPRINKLER ALLOWANCE JEMPERATURE RATING CALCULATION GPM REQUIRED. 9 PSI REQUIRED 32, % AT BASE OF RISER. SUMMARY C" FACTOR USED: OVERHEAD / Z C) ' UNDERGROUND / O J WATER FLOW TEST DATE & TIME 7-Z-86 S—som PUMP DATA RATED CAPACITY TANK OR RESERVOIR CAPACITY as STATIC PSI 5'0 AT PSI ELEVATION RESIDUAL PSI 30 m ELEVATION N GPM FLOWING ?q0WELL IELEVATION Z'N PROOF FLOW GPM LOCATION o N a cP IvC I - SOURCE OF INFORMATION COMMODITY CLASS LOCATION W. STORAGE HEIGHT AREA AISLE WIDTH Q STORAGE METHOD: SOLID PILED 96 PALLETIZED % RACK % 0 1- SINGLE ROW CONVENTIONAL PALLET AUTOMATIC STORAGE Cl ENCAPSULATED DOUBLE ROW SLAVE PALLET SOLID SHELVING NON- MULTIPLE ROW" OPEN ENCAPSULATED Y U - FLUE SPACING IN INCHES CLEARANCE FROM JOP OF STORAGE TO CEILING U LONGITUDINAL TRANSVERSE FT. IN. HORIZONTAL BARRIERS PROVI,DEO A®®RIKVIATIONS USIKO IN CALCULATIONS O . PLOW INCREMENT AT SPECIFIC LOCATION - T . TEE.FLOW TURNED 90* •- j O • PLOW AT A SPECIFIC LOCATION. _ C . CROSS.FLOW TURNED-90 I O.P,M. • GALLONS PER'MINVTE , _ DEL.V.. DELUGE VALVE - P.5.1 POUND PER SQUARE .INCH D.P.V.. DRY PIPE VALVE PT- TOTAL PRESSURE IN P.0.1.' ` -, - AL.V.. ALARM VALVE - .. PP. PRESSURE LOSS OUR TO FRICTION GV-. GATE VALVE I - PE . PRESSURE CHANGE.DUE TO RLFSVATION I CV . OWING CHECK VALVE PN PRESSURE NORMAL AV . ANOLR VALVE PV PRESSURE VRLOCITV' _ GLV . GLOBR VALVE 6E 40# ELBOW T . STRAINER i E . 90' ELBOW - BFP . BACKF LOWPREVENTER L.T.I.. LONO TURN ELBOW DCV . DETECTOR CHECK VALVE I - TW THIN! -WALL PIPE - BV .. BUTTERFLY VALVE MULTIPLY SCALE. BY GPM 0 lot 200 300 400 500 600 700 800 800 to p r. _ - - _ •_ - _. _ ... .. ___ .. i-.. - - - - - - T' 70 tI i' Y r- Y r F I RENE T 1 fYDI ::AUL I C ANALYSISOF OFA . F I RF_ PROTECTION SPRINKLER SYSTEM VERSION 1 = JULY 1984 DATE FOR THIS COMPUTER RUN = 7-3-86 ! ID FOR THIS COMPUTER RUN -:: LURIA INPUT DATA FILE NAME LURIA OUTPUT DATA FILE NAME 8632 SPRINKLER SYSTEM DATA SUMMARY WATER SUPPLY CHARACTERISTICS: STATIC PRESSURE = 50 PSI RESIDUAL PRESSURE _ 30 PSI RESIDUAL FLOW = 790 GPM ELEVATION OF PRESSURE GAGE:=. 2.5 FT. FLOW REQUIREMENTS: OUTSIDE HOSE FLOW REQUIREMENT (AT SUPPLY) = 250 GPM INSIDE HOSE FLOW REQUIREMENT (AT LOCATION 0 ) 0 GPM TOTAL SPRINKLER SYSTEM FLOW REQUIRED (BASE OF RISES`:) = 0 GPM SPRINKLER INFORMATION: MAXIMUM SPACING OF SPRINKLER.HEADS 10 FT MAXIMUM SPACING OF BRANCH LINES = 12 FT. REQUIRED MINIMUM FLOW (PER SPRINKLER) = 22.8 GPM REQUIRED MINIMUM FLOW DENSITY = .19 GPM/SCE. F.T. OTHER SPRINKLER SYSTEM DATA: DEFAULT VALUE FOR C-FACTOR = 12cj NUMBER Of" BOOSTER PUMPS = u SUMMARY OF SPRINKLER OPERATION: SPRINKLER CONSTANT = 5.6 ! LOCATION OF OPERATING SPRINKLER'S 66 67 68 6 LOCATION OF OPERATING, SPRINKLERS: 75 76 77' 78 LOCATION OF OPERATING SPRINKLERS: 84 85 86 87 8B i f.#..#•.. T•r••••i\•T'i\.'(.•..••.i•.P•••T••'i•i.••T•%•r•'(1 .1Y...••#••#. •j'••••••.#.•T..•#•i••••i•T•.i•i.•#..*+i•• ! 3- 3: HYDRAUL.I C ANALYSIS WITH REQUIRED FLOW AT REMOTE HEAD 11 i 1 SUMMARY OF SPRINKLER SYSTEM OPERATION::#:* s THE FOLLOWING SPRINKLERS ARE OPERATING i 1 LOCATION SPRINKLER K ELEVATION FLOW PRESSURE 66 5.60 12.50 23.02 16.90 67 5.60 12.50 22.82 16.61 68 5.60 12.50 22.Oo 16.50 613 5.60 12.50 22.e5 16.65 75 5.60 12.5U 23.02 16.90 76 5.60 12.50 22.82 16.60 77 5.60 12.50 2.80 16.58 78 5.60 12.50 22.83 16.62 84 5.60 12.50 25.00 1'9.93 j 85 5. Eu 12. 50 24.96 19 86 86 5. 60, 12.50 25. 00 19. °J2 87 5.6012.50 23.ol 16.88 88 5.60 . 12. 50 117.01 , i THE TOTAL SPRINKLER FLOW DELIVERED 304.01 GPM THE OUTSIDE HOSESTREAM FLOW OF 250 GPM OPERATES AT 39.63 PSI THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS o..190 GPM/SO FT WATER SUPPLY CHARACTERISTICS LOCATION AT PIPE NO .1 STATIC PRESSURE 50 PSI RESIDUAL PRESSURE = 30 PSI AT 790 GPM OPERATING PRESSURE = 31.63 PSI AVAILABLE PRESSURE = 39.63 PSI AT 553.97 GPM EXCESSIVE (OR REQUIRED) SUPPLY PRESSURE _ 8 PSI i f r SUMMARY OF HYDRAULIC CALCULATIONS I NODES FLOW F' T f='E EL?V .:'H-W. D i A. PSI/ ELEV.-,START END D i F F FROM-1-0 i---1cj- GF'rrl) FT. i FT C- 15cj- IN. 1UU-FT PSI. PSI. 71.... PSI. PSI. cj:.'38-`.::cj, cj J--48. 38 7. 8 cJ. j7-.__j. Qcj3: 2:..; 67 J . 05 1 U q11 303. 98 12. 5_1" 22.00 120 4.26 2.18 5.42 32. 6 26 • JU G • 17 11 12 303.98 1. iJc 20.00 12cj 4.262.18 0. 00 26.56 26.04 o.46 12 37. 67 5.50 0.00 120 4.26 U. 05 0.00 26.04 26.04 0.00 12 23 266.3U 6.UU U.UU 120 4.26 1.7o 0.00 26.U4 25.94 U.10 21 2'2 18.GO 9.00 0.00 120 4.26 0.01 0.00. 26.04. 2E.04 0.00 a. 3 24 248.44 11.50 0.00 12U 4.26 1.50 O. UU 25.94 25.77 0.17 25 26 214.02 11.50 0.cj0 120 4.26 1.14 0.00 25.6o 25.47 0.13 30 31 19. 04 11.50 0.00 120 41. 26 0. 01 0.00 ' 25. 28 25.28 c_i . 00 24 25 231.40 12.50 0.00 120 4{ . '6 1.31 0.100 25.77 25.60 U. 16 3cJ 7'• 1J 12• w t..1, iJ J 12 J 4•.:G 0.18 0.00 25.30 25.26 0.02 26 27 19G-. 15 4.00 0. 00" 120 4.26 0.97 0.00 25.47 25.43 0.04 27 28 177.75 8.50 U.00 120 44.26 0.81 0.00' 25.43 2`,.37 0.07 28 2' 139. 19 12-00 0.00 120 4.2E 0.51 0.00 25. 37 25.30 0.06 41 4z2 18.60 8.00 0.00 120 3.26 o.05 O . oo 23.50 3. 5C) o . t1t ) 4 3 37.67 J. 75 0.00, 12cj 3. 26 0. 17 0. 00 23.50 23.48 U. cJ2 43 44 55.54 11.50 0. 00 120 3.26 cj. 34 0.00 23.48 23.44 0. 04 444, 45 72.57 12.00 0..00 120 3.26 0.56 0.00 23.44 23.37 0.0707 45 46 89. 96. 12.00 0.00,120 3.26 0. 84 0. 00. 23.37 23.27 0. 1 ii 46 47 107682 12.00 0.00 120 3.26 1.18 0.00 23.27 23.13 0. 14 47 48 126.22 12.00 0.00 120 3.2E 1.57 0. 00 23.13 22.94 0. 19 s 48 49 89.86 12.00 0.00 120 3.26 0.84 0.00 22.94 22.84 0.10 49 50 35.37 12.00 0.Oo 120 3.26 0.15 0.Oo 22.84 22.83 o. 0 ' 50 51 19. U4 8.50 0.00 12U 3.26 0.05 0.00 22.83 22.83 0.00 21 41 18. 60 196.00 32.00 12U 1.69 1.11 O. oo , 26. U4 23. 5U 2.,54 s 2. 42 I'D. 08 197. 00 21. 00 120 1.69 1. 17 0.100 ' 26.04 23.50i 2.54 i 23 43 17.87 198. oO 40.00 120 1.69 1.03 0. Oo 25.94 23.48 2.46 24 44 17.03 198.00 48.00 120 1.69 0.95 U. UU 25. 77 23.44 2.32 25 4545 17. 39 1.95.00 32. 001201.69 0.88. 0.00 25.6c_i 23.37 2. 23. 6 4G 17.86 195.00 18.00 120 1.69 1.03 0.00 25.47 23.27 2 . cj 27 47 18. 40 193.00 18.00 120 1.69 1.09 O. Oo 25.43 23. ICJ G. 3U p 31 51 19.04 193.00 1fl.0cj 1.-69 1.16 0.00 25.28 22.83 2.45 28 89 38.56 104.50 12.00 120 120 1.69 4.29 0.00. 25.37 20.36 5.0(. 29 91 60. U6 63. UU 12.00 120 1.69 9. 75 0.00 25.30 17.99 P 7. 31 30 90 60.09 G4. 00 12.00 120 1.69 9.76 0.00 - 25.28 17.8E 7.42 48 79 36.36 17.00 6.00 120 1.69 3.85 0.00 22.94 22.06 0.89 49 70 54.49 17.00 6.00, 120 1.69 8.14 0.00 22.84 20.97 1.87 50 61 54.40 17.00 6.00, 120 1.69 8.12 0.00 22.83 20.96 1.87 61 62 54.40 10.00 0.00 12 0 1.69 18.12, 0.00 20.96 20.15 0. 81. 62 63 54.40* 10.00 01.00 120 1.69 8. 12, 0.00 20.15 19.33 0.81 63 64 54.40 10.00 0.00 12U 1.69 8.12 0.00 19.33 18.52 0.81 64 65 54.40 10.00 0.00 120 1.69 8.-12 0.00 18.52 17.71 : 0.81 65 66 54.40 10.00 0.00 120 1.69 8.12 0.00 17.71 16.90 0.81 6G 67 31.39 10.00 0. 0.0 " 120 1.69 2.93. 0.00 16.90 16.61 0.29 67 68 8. 57 10- UU, 0.00 120 1.69 0.26 0.00 16.61 16.58 U. U.".'r . 68 69 14.24 10.00 . O.:UO 120 1.69 0.68 0.00 16.58 16.65 0.07 70 71 54.49 10.00 0.00 120 1.69 8.14 6.00 20.97 20.16 0.81 71 72 54..49 10..00 0'. 0U 120 1.69 8. 14' 0. G0 20. 16 19.34 0.81 72 73 54.49 10- 00 Q.'-00 120 1. 69 .. 8. 14 0.00 19.34 18.53 c j. 8.1 73 74 54.49 10.00 0, 00 120. 1.69 ` 8.14 a. U0 18.53 17.71 0.81 74 75, 54.49 10.00 0.00 120 1.69 8.14 0.00 17.71 16. 90 c . 81 75 76 31.49 10.00'::,0. 00 120 1. 69 2.95 0.00 16. 90. 16. 60 0. 29 76 77 8.66 10.00 0.100 120 1.69 0.27. 0.00 16.60 16.58 0.03 79 80 36.36 10.00 0.00 120 1.69 3.85 0.00 22.06 21.67 0.39 81 82 36.36 10. 00 0. 00 120 1 . 69 3. 85 0 . cjcj 21.10 20.71 0. 3' D 82 83 36.36 10.00 0". 00 120 1.169 3.85 0. 00 20. 71 26.33 0.39 83 84 36.36 10.00 Q. 00 12o 1.69 3.85 o. UU 20.33 19.94 o. 9 8.5 8 13. 7 10. Cu; 0.00 120 1.69 0. 6 cj(-- 19. 87 :.: 19. 84 c.j, 06 78 E30 3E. 97 1o. Oo o. oo 120 1.69 3.97 0.00 16.62 17. 01 0. 40 87 90 60. 09 10. c.u_) c:). (:)0 1::0 1.69 9.76. 0. Oo 16. 89 17.86 0.98 Be 1 60 . c:>6 10 , i o 0. Oo 110 1 . 6'9 9.75 0 . oO 17 .,o i 17.99 0. 98 86 8'g 38.56 10.00 0.00 120 1.69 4.29 0.00 19.94 20.36 0. 43 77.:78 14.14 6.00 0.00 120 1.69 0.67 0.00 16.58 16.62 0.04 69 87 37. o8 6.00 0.00 120 1.69 3.99 0.00 16. 65 16. 89 0. 24 80 81 36.36 9.00 6.00 120 1.69 3.85 0.00 21.67 21.10 0.58 84 85 11.37 9.00 6.00 120 1.69 0.45 0.00 19.94 19.87 0.07 THE MAXIMUM VELOCITY OF i 8.59 FT/S OCCURS BETWEEN NODES 87 AND 90 HYDRAULIC CALCULATIONS ACCURACY CHECKS (UNBALANCED PRESSURE IN LOOPS): i LOOP.# 1 - NODES: 23 43 42 22 12 23 UNBALANCED.PRESSURE 0.0001 PSI LOOP # 2 - NODES: 41 42 2221 41 UNBALANCED PRESSURE = 0.0000 PSI LOOP # 3 - NODES: 43 44 24 23 43 UNBALANCED PRESSURE = 0.0001 PSI LOOP # 4 - NODES: 45 46 26 25 45 UNBALANCED PRESSURE _'-0.0001 PSI LOOP # 5 -.NODES. 29 28 27 47 48 49 50 51 31 30 29 UNBALANCED PRESSURE = 0,0001 PSI LOOP # 6 - NODES: 44 45 25 24 44 UNBALANCED PRESSURE = 0.0001 PSI LOOP # 7 - NODES: 28 27 47 48 49 50 61 62 63 64 65 66 67. 68 69 87 90 30 29 28 UNBALANCED PRESSURE _ 0.Oo23 PSI I LOOP # 8 - NODES: 467 47 27 26 46 UNBALANCED PRESSURE = O. caOoO PSI LOOP # 9 -- NODES: 47 48 79 80 81 82 83 84 85 86 89 28 27 47 UNBALANCED PRESSURE = 0.0187 PSI LOOT' # 10 - NODES: 89 86 85 84 83 82 81 80 79 48 4" 3 70 71 72 73 74 75 76 77 78 Be 91 29 28 8°3 UNBALANCED PRESSURE 0.0162 PSI a i 3 i SPRINKLER CONSTANT 5 6 LOCATION.:OF OPERATING•.SPRINKLERS: 65 66 67.' 68 69 LOCATION OF OPERATING.SPRINKLERS: 74 75 78 77. 78 i LOCATION OF OPERATING SPRINKLERS: 83 841, 85 i i i I' HYDRAULIC ANALYSIS WITH REQUIRED FLOW AT REMOTE HEAD SUMMARY OF SPRINKLER SYSTEM' OPERATION:*:*:#::#: i THE FOLLOWING SPRINKLERS ARE OPERATING LOCATION SPRINKLER K ELEVATION FLOW PRESSURE 65 5.60 12.50 23.07 iG.97 66 5.60 12.50 22.04 16.64 67 5.60 121. 50 22. 83 1116. 5 i 68 5.60 .50 22.84 16.64 I i 69 5.60 12. 50 ::3. 00 16.99 74 5.60 12.50 23.0E 1G.96 75 5.60 12.50 22.83 16.62 76 5.6U 12.50 22.8U 16.58 77 5.60 12.50 22.e3 16.6.E 78 5.60 12.50 22.97 16. 83 . SU 5.60 12.50 24.97 19.88 84 5.60 12.50 24.93 19.8' 85 5.60 12.50 24.98 19.90 THE TOTAL SPRINKLER FLOW DELIVERED = 304,o2'GPM THE OUTSIDE HOSESTREAM FLOW OF 250 GPM OPERATES AT 39.63 PSI i I THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.150 GPM/SQ FT WATER SUPPLY CHARACTERISTICS LOCATION AT PIPE NO 1 STATIC PRESSURE 50 PSI RESIDUAL PRESSURE 30 PSI AT 790 GPM OPERATING PRESSURE =.31.E1 PSI AVAILABLE PRESSURE = 39.63 .PSI AT 553.98 GPM EXCESSIVE ( OR REQUIRED) SUPPLY PRESSURE - 8. 020001 PSI SUMMARY OF HYDRAULIC CALCULATIONS f HYDRAULIC ANALYSIS WITH REQUIRED FLOW AT REMOTE HEAD k::#::#- 4..::::#:;: F::#::#::#::#::#::#::#:: i SUMMARY OF SF,RINI-::LEF: i SYSTEM OPERATION: :: z THE FOLLOWING SPRINKLERS ARE OPERATING LOCATION SPRINKLEF, k; ELEVATION FLOW PRESSURE k. 67 5.60 12.50 22.98 16.84 G9 5. GO 12.50 22.91 16.59 69 GO 12. 5o 22. 8o 16.56 7G 5.60 12.50 20.00 16.87 77 5.60 12.50 22.83 16.62 78 `,. GO 12.50 22.82 16.61 is 85 5.6U 12.50 24.92 19.8o f' 86 5.60 12.50 24.90 19.77 i 87 5.60 12.50 22.84 16.63 88 5.60 1'2. 50 22.89 16.71 5.60 12. JU 2,4. 95 19.84 90 5.60 12.50 23.15 17.08 31 5.60 12.50 23. 20 17.16 THE TOTAL SPRINKLER FLOW DELIVERED i' 304.07 GPM THE OUTSIDE HOSESTREAM j FLOW OF 250 GPM OPERATES AT 39.63 PSI THE MINIMUM DENSITY. PROVIDED BY THIS SYSTEM IS o.190 GPM/SO FT WATER SUPPLY CHARACTERISTICS LOCATION AT PIPE NO 1 SI-AT I C PRESSURE = 5U PSI RESIDUAL PRESSURE.= 30 PSI AT 790 GPM OPERATING PRESSURE =:31.52. PSI AVAILABLE PRESSURE = 39.63 PSI AT 554.03. GPM EXCESSIVE (OR REQUIRED) SUPPLY PRESSURE = 8.1 PSI 43-334343* L r-l'a 5 +,Sov) , ---L- a C- Drl a,nd o D r. a oa s