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HomeMy WebLinkAbout2966 Orlando Dr 20010 Sign Ace Beauty SupplyH or( a* Ow ry a 3 i i D D D FI 3= L L L l 5 flux c n T o 3.4 c /-r o I= s i 6 N Tm Ijc CPT t cL7 7 13,4Ck of s GN 1-U NMI All /Y1_XZ9?:15 0 RA i1L 1Jd4' D'G.95"IC^F'9CL—'S f(.O. L Am PS d P,4 L L A STS 36 1. F(II 7V ' >= II 1J i L. b1NG-- J tia,l ISOM OZ, 4q64, 77 WEST FL0RJDA PI N G CO,, INC. P. O. DRAWER 1563 MARIANN,^' L 32446 HYDRAULIC CALCULATIONS FOR RUSH HAMPT0N — SYSTEM #7 / AREA D (GRID) sANF0RD. FLORIDA ` FILE NUMBER:82084 Nov 24. 1982 WFPC m. ED: ECDESIGN DATA—M31987 TAMPA OCCUPANCY CLASSIFICATION: ORDINARY HAZARD — GP' 3 DENSITY: 20 grm/sn. ft. AREA OF APPLICATION: 3000 S&. FT. COVERAGE PER SPRINKLER: 125 sp. ft. NUMBER OF SPRINKLERS CALCULATED: 24 HEADS TOTAL SPRINKLER WATER FLOW REQUIRED: 628.4 GPM TOTAL WATER REQUIRED (INCLUDING HOSE): 1128.4 GPM FLOW & PRESSURE (AT SOURCE): 1128.4 GPM @ 108.1 PSI SPRINKLER ORIFICE SIZE: 1/2 INCH CALCULATIONS BY HASS COMPUTER PROGRAM HRS SYSTEMS. INC. ATLANTA. GA' 14 SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: RUSH HAMPT0N - SYSTEM #7 / AREA D (GRID) WATER SUPPLY DATA NODE # AT STATIC RESIDUAL FLOW HOSE STREAM SOURCE PRESSURE PRESSURE @ ALLOWANCE PSI) (PSI) (GPM) (GPM) 45 125.0 81.3 3000.0 0'0 AGGREGATE FLOW ANALYSIS: TOTAL FL0W AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA Page z HAM ACTUAL T0T/ PRESSURE @ DEMAr, PSI) (GPt- 108.1 1128. NODE # ELEVATION NODE TYPE PRESSURE DISCHARGE FT) PSI) GPM) z 19'7 79'9 2 21.4 K= 5.60 25'2 28.1 3 21.4 K= 5.60 21.9 26.2 4 21.4 K= 5.60 20.4 25.3 5 21.4 K= 5.60 19.9 25'0 6 21.4 K= 5.60 19.9 25.0 7 21'4 K- 5.60 20'3 25'3 8 21.4 K= 5'60 21.8 26.2 9 21.4 K= 5-60 25.1 28'1 10 19.7 56.9 11 19.7 80.0 12 21.4 K= 5.60 25'3 28.1 13 21.4 K= 5.60 21.9 26.2 14 21.4 K= 5'60 20'4 25.3 15 21.4 K= 5.60 20.0 25'0 16 21.4 K= 5.60 20'0 25.0 17 21'4 K= 5.60 20.4 25.3 18 21'4 K= 5.60 21.9 26'2 19 21'4 K= 5'60 25.2 28.1 20 19.7 57'0 21 19.7 80.5 22 21.4 K= 5.60 25.5 28.3 23 21.4 K= 5.60 22.1 26.3 24 21.4 K= 5.60 20.6 25.4 25 21.,(1. K= 5'60 20.1 25.1 26 21'4 K= 5.60 20'1 25'1 27 21.4 m= 5'60 20.6 25'4 28 21'4 K= 5'60 22.1 26.3 29 21.4 K= 5'60 25.4 28.2 30 19.7 57.5 31 19.7 81.6 32 19.7 58.6 33 19.7 82.9 34 19.7 59.4 1128.4 GPI- 0.0 GO 500.0 GO 628.4 GPI SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: RUSH HAMPTON - SYSTEM #7 / AREA D (GRID) NODE ANALYSIS DATA (c o rt t' ,j ) NODE # ELFVAT Ic>N NODE TYPE PRESSURE DISCHARGE FT) PSI) GPM) 35 19.7 - - - - 84.6 36 19.7 - - - - 60.0 37 19.7 - - - - 86.6 38 19.7 - - - - 60.4 39 19.7 - - - - 88.9 40 19.7 - - - - 60.6 41 19.7 - - - - 89.7 42 19.7 - - - - 60.8 43 19.7 - - - - 90.6 44 19.7 - - - - 60.8 45 0.0 SOURCE 108.1 112H.4 46 17.0 - - - - 93.3 47 17.0 - - - - 97.7 48 1.0 HOSE STREAM 105.3 500.0 49 0.0 - - - - 106.5 Page 2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS page 3 JOB TITLE: RUSH HAMPTON SYSTEM 7 / AREA D GRID) PIPE DATA PIPE FLOW(GPM) D I A (I N) H-W COEF LENGTH FRICTIONENDNODESVEL(FPS) FT) LOSS PSI/FT) 1 104.9 1.442 120 PL 82.0 0.592 PF 53.9120.6 FL 9.0 PE 0.7 TL 91.0 PV 2.9 2 76.7 1.442 120 PL 10.0 0.332 PF 3.32315. 1• FL 0.0 PE 0.0 TL 10.0 PV 1.5 3 50.5 1.442 120 PL 10.0 0.153 PF 1.5349.9 FL. 0.0 PE 0.0 TL 10.0 PV 0.7 4 25.2 1.442 120 PL 10.0 0.043 PF 0.4455.0 FL_ 0.0 PE 0.0 TL 10.0 PV 0.2 5 0.3 1.442 120 PI_ 10.0 0.000 PF 0.0560.1 FL_ 0.0 PE 0.0 TL 10.0 PV 0.0 6 24.7 1.442 120 PL 10.0 0.041 PF 0.4 6 7 4.9 Ft- 0.0 PE 0.0 TL 10.0 PV 0.2 7 50.0 1.442 120 PL 10.0 0.150 PF 1.5 7 8 9.8 FL 0.0 PE 0.0 TL 10.0 PV 0. f, 8 76.2 t.442 120 PL 10.0 0.328 PF 3.3 8- 9 15.0 FL 0.0 PE 0.11) TL 10.0• PV 1.1-5 9 104.2 1.442 120 PI_ 44.0 0.585 PF 31.0 9 10 20.5 FL 9.0 PE 0.7 TL 53. 0 PV 2. e3 10 104.9 3.260 120 PL 12.5 0.011 PF 0.1 1 11 4.0 FL 0.0 PE- 0.0 TL 12.5 PV 0.1 11 105.0 1.442 120 PL 82.0 0.593 PF 54.0 11 12 20.6 FL 9.0 PE 0.7 TL 91.0 PV 2.9 12 76.8 1.442 120 PL 10.0 0.333 PF 3.3 12 13 15.1 FL 0.0 PE 0.0 TL 10.0 PV 1.5 13 50.6 1.442 120 PL 10.0 0.154 PF 1.5 13 14 9.9 FL 0.0 PE 0.0 TL 10.0 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: RUSH HAMPTON SYSTEM 7 / AREA D GRID) s PIPE DATA cont'd) PIPE FLOW(GPM) DIA(IN) H-W COEF LENGTH FRICTIONENDNODESVEL ( FPS) FT) LOSS PSI/FT) 14 25.3 1.442 120 PL 10.0 0.043 PF 0.414155.0 FL 0.0 PE 0.0 TL 10.0 PV 0.2 15 0.3 1.442 120 PL 10.0 0.000 PF 0.015160.1 FL 0.0 PE 0.0 TL 10.0 PV 0.0 16 24.8 1.442 120 PL 10.0 0.041 PF 0.416174.9 FL 0.0 PE. 0.0 TL 10.0 PV 0.2 17 50.1 1.442 120 PL 10.0 0.151 PF 1.5 17 18 9.8 FL 0.0 PE 0.0 TL 10.0 PV 0.7 18 76.3 1.442 120 PL 10.0 0.329 PF 3.3 is 19 15.0 FL 0.0 PE 0.0 TL 10.0 PV 1.5 19 104.3 1.442 120 PL 44.0 0.587 PF i 31.1. ' 19 20 20.5 FL 9.0 PE 0.7 TL 53.0 PV 2.8 20 104. 3 3.260 120 PL 12.5 0.011 PF 0.1 10 20 4.0 FL 0.0 PE 0.0 TL 12.5 PV 0.1 21 209.8 3.260 120 PI_ 12.5 0.040 PF 0.5 1. 1 21 8.1 FL 0.0 PE 0.0 TL- 12.5 PV 0.4 22 105.3 1.442 120 PL 82.0 0.597 PF 54.3 21 22 20.7 FL. 9.0 PEA 0.7 TL 91.0 PV 2.9 23 77.0 1.442 120 PL 10.0 0.335 PF 3.3 22 23 15.1 FL 0.0 PE 0.0 TL 10.0 PV 1.5 24 50.7 1.442 120 PL 10.0 0.154 PF 1..5 23 24 10.0 FL 0.0 PE 0.0 TL 10.0 PV 0.7 25 25.3 1.442 120 PL 10.0 0.043 PF 0.4 24 25 5.0 FL_ 0.0 PE 0.0 TL- 10.0 PV 0.2 26 0.3 1.442 120 PL 10.0 0.000 PF 0.0 25 26 0.1. FL_ 0.0 PE 0.0 TL 10.0 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE: RUSH HAMPT0N SYSTEM 7 / AREA D (GRID) PIPE DATA cont`d) PIPE FLOW(GPM) DIA(IN) H-W C0EF LENGTH FRICTION END NODES VEL(FPS) FT) LOSS PSI/FT) 27 725.0 1.442 120 PL 10.0 0.042 PF 0'4 26 27 4.9 FL 0.0 PE 0.0 TL 10.0 PV 0'2 28 50.4 1.442 120 PL 10.0 0.153 PF 1.5 27 28 9.9 FL 0.0 PE 0'0 TL 10.0 PV 0'7 29 78'7 1'442 120 PL 10'0 0'332 PF 3'3 28 29 15'1 FL 0.0 PE 0.0 TL 10.0 pV 1-5 30 104.9 1.442 120 PL 44'0 0'592 PF 31'4 29 30 20'6 FL 9.0 PE 0-7 TL 53.0 PV 2.9 31 208'6 3.260 120 PL 12.5 0.040 PF 0.5 20 30 8'0 FL 0.0 PE 0.0 TL 12.5 PV 0.4 32 315.0 3.260 120 PL 12.5 0.085 PF 1'1 21 31 12.1 FL 0.0 PE 0.0 TL 12.5 PV 1'0 33 41.7 1.442 120 PL 196.0 0.107 PF 23'0 31 32 8'2 FL 18'0 PE 0'0 TL 214.0 PV 0.5 34 313'5 3'260 120 PL 12.5 0.085 PF 1.1 30 32 12.1 FL 0'0 PE 0'0 TL 12.5 PV 1.0 35 356.7 3'260 120 PL 12'5 0.107 PF 1'3 31 33 13'7 FL 0'0 PE 0'0 TL 12.5 PV 1'3 36 42.2 1'442 120 PL 196.0 0.110 PF 23-5 33 34 8.3 FL 18'0 PE 0'0 TL 214'0 PV 0'5 37 271.9 3'260 120 PL 12'5 0-065 PF 0'8 32 34 10.4 FL 0'0 PE 0'0 TL 12.5 PV 0'7 38 398.9 3'260 120 PL 12'5 0.132 PF 1'7 33 35 15.3 FL 0'0 PE 0'0 TL 12.5 PV 1.6 39 43.2 1'442 120 PL 196.0 0.115 PF 24'6 35 36 8.5 FL 18.0 PE 0.0 TL 214'0 PV 0'5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 JOB TITLE: RUSH HAMPTON - SYSTEM 07 / AREA D (GRID) PIPE DATA cont'd) PIPE END NODES FLOW(GPM) DIA(IN) H-W CiREF LENGTH FRICTIONVEL ( FPS ) FT) LOSS PSI/FT) 40 34 36 229.7 3.260 120 PL 12.5 0.048 PF 0.6e.8 FL. 0.0 PE 0.0 TL 12.5 PV 0,5 41 35 - 37 442.1 3.260 120 PL 12.5 0.160 PF 017.0 FL 0.0 PF_ 0.0 TL 12.5 PV 1.9 42 37 - 38 44.7 1.442 120 PL 196.0 0.122 PF 26.28.6 FL 18.0PE 0.0 TL 214.0 PV 0.5 43 36 - 38 186.5 3.260 120 PL 12.E 0.032 PF 0.47 FL 0.0 PE 0.0 TL 12.5 PV 0.3 44 37 - 39 486. 8 1.8. 7 3.260 120 PI_ 12. 5 0. 191 PF 2.4 FL 0.0 PE 0.0 TL 12.5 PV 2.4 45 39 - 40 46.6 1.442 120 PL 196.0 0.132 PF 28.39.2 FL 18.0 PE 0.0 TL 214.0 PV 0.6 46 38 - 40 141.8 3.260 120 PL 12.5 0.019 PF 0.: 5.5 FL 0,0 PE 0.0 TL 12.5 PV 0. 47 39 - 41 533.4 4.260 120 PL 12.5 0.061 PF 0.812.0 FL 0.0 PE 0.0 TL 12.5 PV 1.0 48 41 - 47.2 1.442 120 PL 196.0 0.135 PF 29.0429.3 Ft_ 18.0 PE 0.0 TL 214.0 PV 0,6 49 40 - 42 95.2 3.260 120 PL 12. `i 0. 009 PF 0 , 13, 7 FL 0.0 PE 0.0 TL 12.5 PV 0.1 50 41 580.6 4.260 120 PL 12.5 0.072 PF 0.94313.1 FL 0. 0 PE 0.0 TL 12.5 PV 1.1 51 43 - 48.0 1.442 120 PI_ 196.0 0.139 PF 29.8449.4 FL 18.0 PE 0.0 TL 214.0 PV 0.6 52 42 - 48.0 3.260 120 PL 12.5 0.003 PF 0.0441.8 FL 0.0 PF_ 0.0 TL 12.5 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 JOB TITLE! RUSH HAMPT0N - SYSTEM #7 / AREA D (GRID) PIPE DATA (cont`d) PIPE FLOW(GPM) DIA(IN) H-W C0EF LENGTH FRICTION END NODES VEL(FPS) (FT) LOSS PSI/FT) 53 628.6 4.260 120 PL 6.3 0.083 PF 1.5 43 46 14.1 FL 12.0 PE 1.2 TL 18.3 PV 1'3 54 628'6 4.260 120 PL 47'0 0.083 PF 4.4 6 47 14'1 FL 6'0 PE 0'0 TL 53.0 PV 1'3 55 628.7 6.360 120 PL 18.9 0.012 PF 0'6 47 48 6.3 FL 35.0 PE 6'9 TL 53.9 PV 0'3 56 1128.6 8.040 150 PL 30.0 0.007 PF 0'8 48 49 7'1 FL 73.0 PE 0.4 TL 103.0 PV 0.3 57 1128.4 9.870 150 PL 450.0 0.003 PF 1.6 49 45 4'7 FL 142.0 PE 0'0 TL 592.0 PV 0'2 NOTES: 1) Calculations were Performed by the HASS 3.3 computer program under license no. 8101F40 granted by HRS Systems, Inc' 2193 Ranchyood Dr.. N.E. Atlanta, Georgia 30345 2) The system has been balanced to provide an average imbalance at each node of 0.133 spm and a maximum imbalance at any node of 0.844 srm. 3) Velocity Pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 20'7 ft/sec. 4) a' System remote area HAS been nroven or 'peaked'. b. Minimum pressure at any sprinklery 19.931 psi c. Minimum pressure with remote area shifted one sprinkler space toward near cross main: 20.009 psi d. Minimum pressure with remote area shifted one sprinkler space toward far cross main: 19'987 psi FLOW DIAGRAM JOB TITLE: RUSH HAMPTON - SYSTEM #k7 / AREA D (GRID) T 106.0 77.7 51.5 26.2 1.3 23.8 49.0 75.2 103.0 ? 106.0 103.2 C 11 ]*--:>---*--' T 106.1 77.8 51.5 26.2 1.3 23.8 49.1 '75.3 103.1 T 212.0 206.4 t C21]*-->---*--:>---*-->---•*-->---w-->---x--<:-----<:---*--!---*--<:--- *[ :30 ] 106.5 78.0 51.6 26.2 1.2 24.0 49.4 75.6 103.6 v 318.4 44.2 T v 131]*------------------------------ 41.1 T 359.5 269.0 T ? C.33]*------------------------------- >------------------------------- * C34] T 41.7 T 401.2 227.3 C353*------------------------------>--------------------------------*C 36 1 T 42.7 T 443. 9 184.6 T T C37_ 1*------------------------------ ;>------- =----------------------*C381 T 44.2 488. 2 140. 4• T T C. 39 ]*------------------------------'--•--- ----------------------------*C40:I T 46.2 f 534.:. 3 94. T T l*------------------------------ >---------------------------------- -* C 4 ' :I T 46.7 T 581. 1 47.5 T T C43 ]*------------------------------''-•------------- WEST FLORIDA PIPING CO., INC. P.O. DRAWER 1563 MAR I ANNA, FL. 32446 HYDRAULIC CALCULATIONS FOR RUSH HAMPTON - SYSTEM #7 / AREA D (GRID) SANFORD, FLORIDA FILE NUMBER : 92094 Nov 24, 1992 DESIGN DATA-- WFPC rD inn .:, c NA FET uL. , " I TAMPA OCCUPANCY CLASSIFICATION: ORDINARY HAZARD - GP. 3 DENSITY: . 20 gpm/sq. ft. AREA OF APPLICATION: 3000 SO. FT. COVERAGE PER SPRINKLER: 125 5q. ft. NUMBER i F SPRINKLERS CALCULATED: 24 HEADS TOTAL SPRINKLER WATER FLOW REOU I RED : 628.4 GPM TOTAL WATER REOU I RED (INCLUDING HOSE) : 1128.4 GPM FLOW & PRESSURE (AT SOURCE): 1128.4 GPM a 108.1 PSI SPRINKLER ORIFICE SIZE: 1/2 INCH CALCULATIONS BY HASS COMPUTER PROGRAt HRS SYSTEMS, INC. ATLANTA, GA. 14 SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOBi TITLE! RUSH HAMPT0N - SYSTEM #7 / AREA D (GRID) WATER SUPPLY DATA NODE # AT STATIC RESIDUAL FLOW HOSE STREAM SOURCE PRESSURE PRESSURE @ ALLOWANCE PSI) (PSI) (GPM) (GPM) 45 125.0 81.3 3000.0 0'0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA Page 1 HAM ACTUAL TOT( PRESSURE @ DEMAr PSI) (GPr 10B.1 1128. NODE # ELEVATION NODE TYPE PRESSURE DISCHARGE FT) PSI) GPM) 1 19'7 79'9 2 21.4 K= 5.60 25.2 28.1 3 21.4 K= 5.60 21.9 26.2 4 21'4 K= 5.60 20'4 25.3 5 21'4 K= 5.60 19.9 25'0 6 21.4 K= 5.60 19.9 25.0 7 21'4 K= 5'60 20.3 25.3 8 21.4 K= 5.60 21-8 26.2 9 21.4 K= 5.60 25.1 28'1 10 19.7 56'9 11 19.7 e0.0 12 21'4 K= 5.60 25'3 28.1 13 21'4 K= 5.60 21.9 26-2 14 21.4 K= 5.60 20.4 25.3 15 21.4 K= 5.60 20.0 25'0 16 21.4 K= 5.60 20'0 25.0 17 21.4 K= 5'60 20'4 25.3 18 21.4 K= 5.60 21.9 26.2 19 21'4 K= 5'60 25.2 28'1 20 19.7 57'0 21 19'7 80.5 22 21-4 K= 5.60 25'5 28'3 23 21'4 K= 5'60 22.1 26,3 24 21.4 K= 5.60 20'6 25'4 25 21.4 K~ 5'60 20'1 25.1 26 21.4 K=,5'60 20'1 25.1 27 21'4 w= 5'60 20-6 25-4 28 21'4 K= 5'60 22.1 26.3 29 21.4 K= 5'60 25'4 28.2 30 19.7 57'5 31 19'7 81'6 32 19.7 58'6 33 19'7 82'9 34 19'7 59'4 1128.4 GPI 0'0 GPr 500.0 GPt- 628'4 GPr SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: RUSH HAMPTO>N - SYSTEM #7 / AREA D (GRID) NODE ANALYSIS DATA (c o n t' ,j ) NODE # ELFVAT I O N NODE TYPE PRESSURE DISCHARGE FT) PSI) GPM) 35 19.7 - - - - 84.6 36 19.7 - - - - 60.0 37 19.7 - - - - 86.6 38 19.7 - - - - 60.4 39 19.7 - - - - 88.9 40 19.7 - - - - 60.6 41 19.7 - - - - 89.7 42 19.7 - - - - 60.8 43 19.7 - - - - W.6 44 19.7 - - - - 60.8 45 0.0 SOURCE 108.1 1128.4 46 17.0 - - - - 93.3 47 17.0 - - - - 97.7 48 1.0 HOSE STREAM 1.05.3 500.0 49 0.0 - - - - 106.5 Page 2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE! RUSH HAMPTON SYSTEM 7 / AREA D GRID) PIPE DATA PIPE FLU )W ( GPM) D I A (I N) H-W COEF LENGTH FRICTION END NODES VEL (FPS) FT) LOSS PSI/FT) 1 104.9 1.442 120 PL 82.0 0.592 PF 53.9 1 2 20.6 FL 9.0 PF_ 0.7 TL 91.0 PV 2.9 2 76.7 1.442 120 PL 10.0 0.332 PF 3.3 2 3 15.1 FL 0.0 PE 0.0 TL 10.0 PV 1.5 3 50.5 1.442 120 PL 10.0 0.153 PF 1.5 3 4 9.9 FL- 0.0 PE 0.0 TL 10.0 PV 0.7 4 25.2 1.442 120 PL 10.0 0.043 PF 0.4 4 5 5.0 FL 0.0 PE-. 0.0 TL 10.0 PV 0.2 5 0.3 1.442 120 PL 10.0 0.000 PF 0.0 5 6 0.1 FL_ 0.0 PE 0.0 TL 10.0 PV 0.0 6 24.7 1.442 120 PL 10.0 0.041 PF 0.4 6 7 4.9 FL 0.0 PE 0.0 TL 10.0 PV 0.2 7 50.0 1.442 120 PL 10.0 0.150 PF 1.5 7 -- 8 9.8 FL 0.0 PE 0.0 TL 10.0 PV 0.6 8 76.2 1.442 120 PL 10.0 0.328 PF 3.3 8 9 15.0 FL 0.0 PE 0.0 TL 10.0 PV 1 . `_5 9 104.2 1.442 120 PI_ 44.0 0.585 PF 31.0 9 10 20.5 FL_ 9.0 PE 0.7 TL 53.0 PV 2.0 10 104.9 3.260 120 PL 12.5 0.011 PF 0.1 1 11 4.0 FL 0.0 PE 0.0 TL 12.5 PV 0.1. 11 105.0 1.442 120 PL 82.0 0.593 PF 54.0 1.1 12 20.6 FL. 9.0 PF_ 0.7 TL 91.0 PV 2.9 12 76.8 1.442 120 PL 10.0 0.333 PF 3.3 12 13 15.1 Fl- 0.0 PF_ 0.0 TL 10.0 PV 1.5 13 50.6 1.442 120 PL 10.0 0.154 PF 1.5 13 14 9.9 FL 0.0 PE 0.0 TL 10.0 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: RUSH HAMPTON SYSTEM 7 / AREA D GRID) PIPE i DATA cont'd) PIPE FLOW(GPM) DIA(IN) H-W COEF LENGTH FRICTIONENDNODESVEL_(FPS) FT) LOSS PSI/FT) 14 25.3 1.442 120 PL 10.0 0.043 PF 0.414155.0 FL 0.0 PF_. 0.0 TL 10.0 PV 0.2 15 0.3 1.442 120 PL 10.0 0.000 PF 0.0151.6 0.1 Fl_ 0.0 PE 0.0 TL 10.0 PV 0.0 16 24.8 1.442 120 PL 10.0 0.041 PF 0.4 16 17 4.9 FL 0.0 PE. 0.0 TL 10.0 PV 0.2 17 50.1 1.442 120 PL 10.0 0.151 PF 1.517189.8 FL 0.0 PE 0.0 TL 10.0 PV 0.7 18 76.3 1.442 120 PL 10.0 0.329 PF 3.3 18 19 15.0 FL 0.0 PE 0.0 TL_ 10.0 PV 1.5 19 104.3 1.442 120 PL 44.0 0.587 PF 31.1 19 20 20.5 FL 9.0 PE 0.7 TL 53.0 PV 2.8 20 104.3 3.60 120 PL 12.5 0.011 PF 0.1 10 20 4.0 FL 0.0 PE 0.0 TL 12.5 PV 0.1 21 209.8 3.260 120 PL 12.5 0.040 PF 0.5 1.1 21 8.1 FL 0.0 PE 0.0 TL 12.5 PV 0.4 22 105.3 1.442 120 PI_ 82.0 0.597 PF 54.3 21 22 20.7 FL 9.0 PE 0.7 TL 91.0 PV 2.9 23 77.0 1.442 120 PL. 10.0 0.335 PF 3.3 22 23 15.1. Ft- 0.0 PE 0.0 TL 10.0 PV 1..5 24 50.7 1.442 120 PL 10.0 0.154 PF 1.5 23 24 10.0 FL 0.0 PE 0.0 TL 10.0 PV 0.7 25 25.3 1.442 120 PL_ 10.0 0.043 PF 0.4 24 25 5.0 FL 0.0 PF_. 0.0 TL 10.0 PV 0.2 26 0.3 1.442 120 PL 10.0 0.000 PF 0.0 25 26 0.1 FL 0.0 PE 0.0 TL 10.0 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: RUSH HAMPTON SYSTEM 17 / AREA D GRID) PIPE DATA cont'd) PIPE FLOW(GPM) D I A (I N) H-W COE:.F LENGTH FRICTION END NODES VF_L(FPS) FT) LOSS PSI/FT) 27 725.0 1.442 120 PL 10.0 0.042 26 - 27 4.9 FL 0.0 TL 10.0 28 50.4 1.442 120 PL 10.0 0.153 27 - 28 9.9 FL. 0.0 TL 10.0 29 76. 7 1.442 120 PL 10.0 0. 332 28 - 29 15.1 Fl-. 0.0 TL 10.0 30 104.9 1.442 120 PL 44'O 0.592 29 - 30 20.6 FL 9.0 TL 53.0 31 208.6 3.260 120 PL 12.5 0.040 20 - 30 8.0 FL 0.0 TL 12.5 32 315.0 3.260 120 PL 12.5 0.085 21 - 31 12.1 FL. 0.0 TL 12.5 33 41.7 1.442 120 PL 196.0 0.107 31 - 32 8.2 Fl_ 18.0 TL 214.0 34 313.5 3.260 120 PL 12.5 0.085 30 - 32 12. 1 FL 0.0 TL 12.5 35 356.7 3.260 120 PL 12.5 0.107 31 33 13.7 FL 0.0 TL 12.5 36 42.2 1.442 120 PL 196.0 0.110 33 34 8.3 FL 18.0 TL 214.0 37 271.9 3.260 120 PL. 12.5 0.045 32 34 10.4 FL 0.0 TL 12.5 38 398.9 3.260 120 PL 12.5 0.132 33 35 15.3 FL 0.0 TL 12.5 39 43.2 1.442 120 PL_ 196.0 0.115 35 36 8.5 FL 16.0 TL 214.0 Page 5 PF 0.4 PE 0.0 PV 0. PF 1.5 PE 0.0 PV 0.7 PF 3.3 PE 0.0 P V 1. 1_3 PF 31.4 PE 0.7 PV 2.9 PF 0.5 PE 0.0 PV 0.4 PF 1. 1 PE 0.0 PV 1.0 PF 23.0 PE 0.0 PV 0.5 PF 1.1 PE 0.0 PV 1.0 PF 1.3 PE 0.0 PV 1.3 PF 23.5 PE 0.0 PV 0.5 PF 0. %3 PE 0.0 PV 0.7 PF 1.7 PE 0.0 PV 1.6 PF 24.6 PE 0.0 PV 0.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Joe TITLE: RUSH HAMPTON - SYSTEM,#7 / AREA D (GRID) PIPE DATA co n t ' d ) PIPE END NODES FLOW(GPM)DIA(IN) H-W COEF LENGTH FRICTIONVEL (FPS) FT) LOSS PSI/FT) 40 34 36 2:29.7 3.260 120 PL 12.5 0.048 PF 0.68.8 FL 0.0 PE 0.0 TL 12.S PV 0.13 41 35 37 442.1 3.260 120 PL 12.5 0.160 PF 2.017.0 FL 0.0 PE 0.0 TL 12.5 PV 1.9 42 37 38 44.7 1.442 120 PL 196.0 0.122 PF 26.E8.8 FL_ 18.0 PE 0.0 TL 214.0 PV 0.5 43 36 - 38 186.5 3.260 120 PL 12.5 0.032 PF 0.47.2 FL 0.0 PE 0.0 TL 12.5 PV 0.3 44 37 - 39 486.8 3.260 120 PL 12.5 0.191 PF 418.7 FL 0.0 PE 0.0 TL 12.5 PV 2.4 45 39 - 40 46.6 1.442 120 PL 196.0 0.132 PF 28.39.2 FL 18.0 PE 0.0 TL 214.0 PV 0.6 46 38 - 141.8 3.260 120 PL 12.5 0.019 PF 0.2405.5 FL 0.0 PE 0.0 TL 12.5 PV 0.2 47 39 - 41 533.4 4.260 120 PL 12.5 0.061 PF 0.812.0 FL 0.0 PE 0.0 TL 12.5 PV 1.0 48 41- 42 47.2 1.442 120 PL 196.0 0.135 PF 29.0 9.3 FL 18.0 PF_ 0.0 TL 214.0 PV 0.6 49 40 - 95.2 3.260 120 PI_ 12.5 0.009 PF 0.1423.7 FL 0.0 PE 0.0 TL 12.5 PV 0.1 50 580.6 4.260 120 PL 12.5 0.072 PF 0.941 - 43 13.1 FL 0.0 PE 0.0 TL 12.5 PV 1.1 51 48.0 1.442 120 PL 1.96.0 0.139 PF 29.843 - 44 9.14 FL 1.8.0 PE 0.0 TL 214.0 PV 0.6 52 48.0 3.260 120 PL 12.5 0.003 PF- 0.042 - 44 1..8 FL. 0.0 PE 0.0 TL 12.5 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 T0B TITLE: RUSH HAMPT0N — SYSTEM #7 / AREA D GRID) PIPE DATA (cont`d) PIPE FLOW(GPM) DIA(IN) H—W C0EF LENGTH FRICTION END NODES VEL(FPS) (FT) LOSS PSI/FT) 53 628.6 4.260 120 PL A.3 0.083 PF 1.5 43 46 14.1 FL 12.0 PE 1.2 TL 18.3 PV 1.3 54 628.6 4.260 120 PL 47'0 0.083 PF 4.4 46 47 14.1 FL 6'0 PE 0.0 TL 53.0 PV 1.3 55 628.7 6.360 120 P. 18.9 0.012 PF 0.6 47 46 6.3 FL 35.0 PE 6'9 TL 53'9 PV 0'3 56 1128.6 8.040 150 PL 30'0 0.007 PF 0.8 48 49 7.1 FL 73.0 PE 0'4 TL 103.0 PV 0.3 S7 1128.4 9.870 150 PL 450.0 0.003 PF 1.6 49 45 4.7 FL 142.0 PE 0'0 TL 592'0 PV 0'2 NOTES: 1) Calculations were Performed by the HASS 3'3 computer nrouram under license no. 8101F40 granted by HRS Systems, Inc' 2193 Ranchmood Dr.. N.E. Atlanta, Georgia 30345 2) The system has been balanced to Provide an average imbalance at each node of 0'133 spm and a maximum imbalance at any node of 0'844 enm. 3) Velocity pressures are nrinted for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 20'7 ft/sec. 4) a. System remote area HAS been proven or peaked'. b. Minimum pressure at any sprinkler: 19.931 psi c' Minimum pressure with remote area shifted one sprinkler space toward near cross main: 20.009 psi d. Minimum pressure with remote area shifted one sprinkler space toward far cross main: 19.987 nsi FLOW DIAGRAM JOB TITLE: RUSH HAMPTON - SYSTEM #7 / AREA D (GRID) T 106.0 77.7 51.5 26.2 1.3 23.8 49.0 75.2 103.0 T 106.0 103. 2 201 T 106.1 77.8 51.5 26.2 1.3 23.8 212.0 49.1 75.3 103.1 ? T 206.4 C 21 ]*--:>---*-->---*-->---*- T 106.5 79.0 51.6 26.2 1.2 24.0 49.4 75.6 103.6 v 318.4 44." f v C31]*------------------------------::>--------------------------------* C 32] T 41.1 T 359.5 t 269.0 C33_1*------------------------------ 41.7 401.2 7.3 T t C 35 ]*------------------------------ T 42.7 T 443.9 84. 6 T T 44.2 ? 488.2 140. 4. T T 39 ]*------------------------------- '>------------------------------- 46.2 T 534. 3 94. T T C41]*-------------------------------''>-----___------- -_ _-------------* C 4 ' :I T 46.7 T 581.1 47.5 T T C. 43 1*------------------------------ >--------_----•-------- -*1' 44 ] 47.5 49 WEST.FLORIDA PIPING CO., INC. P.O. DRAWER 1563 MAR I ANNA, FL 32446 HYDRAULIC CALCULATIONS FOR RUSH HAMPTON - SYSTEM #7 / AREA D (GRID) SANFORD, FLORIDA FILE NUMBER:82084 Nov 24, 1992 J DESIGN DATA- `" JjcJ%v OCCUPANCY CLASSIFICATION: ORDINARY HAZARD - GP. 3 DENSITY: . 20 gpm/sq. ft. AREA OF APPLICATION: :3000 SO. FT. COVERAGE PER SPRINKLER: 125 s q _ f- t . NUMBER OF SPRINKLERS CALCULATED: 24 HEADS TOTAL SPRINKLER WATER FLOW REQUIRED: 628.4 GPM TOTAL WATER REOU I RED (INCLUDING HOSE) : 1128.4 GPM FLOW & PRESSURE (AT SOURCE) : 1128.4 GPM a 108.1 PSI SPRINKLER ORIFICE SIZE=.: 1/2 INCH CALCULATIONS BY HASS COMPUTER PROGRAM HRH; SYSTE:MSi INC. ATLANTA, GA. 44 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 HAM JOB TITLE: RUSH HAMPTON - SYSTEM #7 / AREA D (GRID) WATER SUPPLY DATA NODE # AT STATIC RESIDUAL FLOW HOSE STREAM ACTUAL TOTr SOURCE PRESSURE PRESSURE a ALLOWANCE PRESSURE @ DEMAr PSI) PSI) (GPM) GPM) PSI) GPI 45 125.0 81.3 3000.0 0.0 108.1 1128. AGGREGATE FLOW ANALYSIS1 TOTAL FLOW AT SOURCE 1128.4 GPt, TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPt- OTHER HOSE STREAM ALLOWANCES 500.0 GPt- TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 628.4 GPI - NODE ANALYSIS DATA NODE # ELEVATION NODE TYPE PRESSURE DISCHARGE FT) PSI) GPM) 1 19.7 79.9 2 21.4 K= 5.60 25.2 28.1 3 21.4 K= 5.60 21.9 26. 4 21.4 K= 5.60 20.4 25.3 5 21.4 K= 5.60 19.9 25.0 i 6 21.4 K- 5.60 19.9 25.0 7 21.4• K= 5.60 20.3 25.3 8 21.4 K= 5.60 21.8 26.2 9 21.4 K== 5.60 25.1 28.1. 10 19.7 56.9 11 19.7 80.0 12 21.4 K= 5.60 25.3 20.1 13 21.4 K= 5.60 21.9 26.2 14 21.4 K= 5.60 20.4 25.3 15 21.4 K= 5.60 20.0 25.0 16 21.4 K= 5.60 20.0 25.0 17 21.4 K= 5.60 20.4 25.3 18 21.4 K= 5.60 21.9 26.2 19 21.4 K- 5.60 25.2 28.1. 20 19.7 57.0 21 19.7 80.5 2 21.4 K= 5.60 25.5 20.3 23 21.4 K==: 5.60 22.1 26. -3 24 21.4 K= 5.60 20.6 25.4 25 i..4 K- 5.60 20.1 25.1. 26 21.4 K- 5.60 20.1 25.1 27 21.4 K= 5.60 20.6 25.4 28 21..4 K= 5.60 22.1 26.3 29 21.4 K==: 5.60 25.4 20.2 30 19.7 7 57.5 31 19.7 81.6 32 19.7 58.6 33 19.7 82.9 34 19.7 59.4 SPRINKLER SYSTEM HYDRAULIC ANAI_.YSIS Paqe 2 JOB TITLE: RUSH HAMPTON - SYSTEM #7 / AREA D (GRID) NODE ANALYSIS DATA (cont'd) NODE # ELEVATIoN NODE TYPE PRESSURE DISCHARGE FT) (PSI) (GPM) 35 19.7 - - - - 84.6 - - - 36 19.7 - - - - 60.0 - - - 37 19.7 - - - - 86.6 38 19.7 _ __ _ 60.4 - - - 39 19.7 - - - - 89.9 - - - 40 19.7 - - - - 60.6 - - - 41 19.7 - - - - 89.7 - - - 42 19.7 - - - - 60.8 - - - 43 19.7 - - - - 90.6 - - 44 19.7 - - - - 60.8 - - - 45 0.0 SOURCE 108.1 1128.4 46 17.0 - - - - 93.3 - - - 47 17.0 - - - - 97.7 - - - 48 1.0 HOSE. STREAM 105.3 -500.0 49 0.0 - - - - 106.5 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE: RUSH HAMPTON SYSTEM 7 / AREA D GRID) PIPE DATA PIPE FL(-)W ( GPM) D I A (I. N) H-W Ct REF LENGTH FRICTION END NODES VF_L(FPS) FT) LOSS PSI/FT) 1 104.9 1.442 120 PL 82.0 0.592 PF 53.9 1- 2 20.6 FL. 9.0 PE 0.7 TL 91.0 PV 2.9 2 76.7 1.442 120 PL 10.0 0.332 PF 3.3 2 3 15.1 FL 0.0 PE 0.0 TL 10.0 PV 1.5 3 50.5 1.442 120 PL 10.0 0.153 PF 1.5 3 4 9.9 FL_ 0.0 PF_ 0.0 TL 10.0 PV 0.7 4 25.2 1.442 120 PL 10.0 0.043 PF 0.4 4 5 5.0 FL 0.0 PE 0.0 TL 10.0 PV 0.2 5 0.3 1.442 120 PL 10.0 0.000 PF 0.0 5 6 0.1 FL_ 0.0 PE 0.0 TL 10.0 PV 0.0 6 24.7 1.442120 PL 10.0 0.041 PF 0.4 6 7 4.9 FL 0.0 PE 0.0 TL 10.0 PV 0.<< 7 50.0 1.442 120 PL 10.0 0.150 PF 1.5 7 8 9.8 FL 0.0 PF_. 0.0 TL 10.0 PV 0.6 8 76.2 1.442 120 PL 10.0 0.328 PF 3.3 B 9 15.0 FL 0.0 PF_ 0.0 TL 10.0 PV 1.5 9 104.2 1.442 120 PL 44.0 0.585 PF 31.0 9 10 20.5 FL_ 9.0 PE 0.7 TL 53.0 PV 2.8 10 104.9 3.260 120 PL 12.5 0.011 PF 0.1 1 1 i. 4.0 FL 0.0 PE 0.0 TL 12.5 PV 0.1 11 105.0 1.442 120 PL 82.0 0.593 PF 54.0 1.1 12 20.6 FL 9.0 PE 0.7 TL 91.0 PV 2.9 12 76.8 1.442 120 PL 10.0 0.333 PF 3.3 12 13 15.1 FL 0.0 PF_ 0.0 TL 10.0 PV 1.5 13 50.6 1.442 120 PL 10.0 0.154 PF 1.5 13 14 9.9 FL 0.0 PE 0.0 TL 10.0 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: RUSH HAMPTON SYSTEM 7 / AREA D GRID) PIPE DATA cant' d ) PIPE FLOW(GPM) DIA(IN) H-W COEF LENGTH FRICTIONENDNODESVEL(FPS) FT) LOSS PSI/FT) 14 25.3 1.442 120 PL 10.0 0.043 PF 0.414155.0 FL 0.0 PE 0.0 TL 10.0 PV 0.2 15 0.3 1.442 120 PL 10.0 0.000 PF 0.015I60.1 Ft- 0.0 PF-. 0.0 TL 10.0 PV 0.0 16 24.8 1.442 120 PL 10.0 0.041 PF 0.416174.9 FL 0.0 PE 0.0 TL 10.0 PV 0.2 17 50. 1 1.442 120 PL 10.0 0.151 PF 1.517189.0 FL. 0.0 PE 0.0 TL 10.0 PV 0.7 18 76.3 1.442 120 PL 10.0 0.329 PF 3.318 -- 19 15.0 FL 0.0 PE 0.0 TL_ 10.0 PV 1.5 19 104.3 1.442 120 PL 44.0 0.587 PF 31.1192020.5 FL 9.0 PF.. 0.7 TL 53.0 PV 2.8 0 104.3 3.260 120 PL 12.5 0.011 PF 0.1 10 20 4.0 FL 0.0 PE 0.0 TL 12.5 PV 0.1 21 209.8 3.260 120 Pt_ 12.5 0.040 PF 0.5 11 -- 21 8.1 F L 0.0 PE 0.0 TL 12.5 PV 0.4 22 105.3 1.442 120 PL 82.0 0.597 PF 54.3 21 - 22 20.7 FL. 9.0 PE 0.7 TL 91.0 PV 2.9 23 77.0 1.442 120 PL_ 10.0 0.335 PF 3.3 22 23 15 . 1. FL 0.0 PE=. 0.0 TL 10.0 PV 1.5 24 50.7 1.442 120 PI_ 10.0 0.154 PF 1.15 23 24 10.0 FL. 0.0 PE 0.0 TL 10.0 PV 0. 7 25 25.3 1.442 120 PL_ 10.0 0.043 PF 0.4 24 - 25 5.0 FL 0.0 PF_. 0.16 TL_ 10.0 PV 0.2 26 0.3 1.442 120 PL 10.0 0.000 PF 0.0 25 - 26 0.1. FL 0.0 PE 0.0 TL 10.0 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE: RUSH HAMPT0N SYSTEM 7 / AREA D (GRID) PIPE DATA cont`d) PIPE FLOW(GPM) DIA(IN) H-W C0EF LENGTH FRICTION END NODES VEL(FPS) FT) LOSS PSI/FT) 27 25.0 1.442 120 PL 10.0 0.042 PF 0.4 26 27 4.9 FL 0.0 PE 0^0 TL 10.0 PV 0'2 28 50.4 1.442 120 PL 10.0 0.153 PF 1.5 27 28 9.9 FL 0.0 PE 0.0 TL 10.0 PV 0'7 29 76.7 1.442 120 PL 10'0 0'332 PF 3'3 28 29 15.1 FL 0.0 PE 0.0 TL 10.0 PV 1.5 30 104.9 1.442 120 PL 44'0 0'512 PF 31'4 29 30 20.6 FL 9.0 PE 0'7 TL 53.0 PV 2.9 31 208.6 3'260 120 PL 12.5 0.040 PF 0.5 00 30 8.0 FL 0'0 PE 0.0 TL 12.5 PV 0.4 32 315.0 3.260 120 PL 12.5 0'085 PF I.I. 21 31 12'1 FL 0.0 PE 0.0 TL 12.5 PV 1'0 33 41'7 1.442 120 PL 196.0 0'107 PF 23'0 31 32 8'2 FL 18'0 PE 0.0 TL 214.0 PV 0.5 34 31345 3.280 120 PL 12.5 0.085 PF 1'1 30 32 12.1 FL 0'0 PE 0'0 TL 12.5 PV 1.0 35 356.7 3.260 120 PL 12'5 0'107 PF 1.3 31 33 13'7 FL 0'0 PE 0'0 TL 12.5 PV 1.3 36 42'2 1'442 120 PL 196'0 0'110 PF 23'5 33 34 8'3 FL 18.0 PE 0'0 TL 214.0 PV 0'5 37 271.9 3.260 120 PL 12.5 0.065 PF 0'8 32 34 10'4 FL 0'0 PE 0~0 TL 12'5 PV 0'7 38 398'9 3'260 120 PL 12'5 0'132 PF 1'7 33 35 15.3 FL 0'0 PE 0.0 TL 12.5 PV 1,6 39 43'2 1'442 120 PL 196.0 0'115 PF 24'6 35 36 8.5 FL 18'0 PE 0-0 TL 214'0 PV 0'5 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Pages 6 JOB TITLE: RUSH HAMPTON - SYSTEM 7 / AREA D (GRID) PIPE DATA Wnt'd) PIPE END NODES FLOW(GPM) DIA(IN) H-W COEF LENGTH FRICTIONVEL (FPS ) FT) LOSS PST/FT) 40 34 36 229.7 3.260 120 PL 12.5 0.048 PF 0.68.8 FL 0.0 PE 0.0 TL 12.5 PV 0.5 41 35 37 442.1 3.260 120 PL 12.5 0.160 PF 2 017.0 Ft_ 0.0 PE 0.0 TL 12.5 PV 1.9 42 37 36 44.7 1.442 120 PL 196.0 0.122 PF 26.28.6 FL 18.0 PE 0.0 TL 214.0 PV 0.5 43 36 - 38 186.5 3.260 120 PL 12.5 0.032 PF 0.47.2 FL 0.0 PE 0.0 TL 12.5 PV 0.3 44 37 - 39 486. 8 3.260 120 PI_ 12.5 0. 191 PF L} FL18.7 0.0 PF_. 0.0 TL 12.5 PV 2.4 45 39 - 40 46.6 1.442 120 PL 196.0 0.132 PF 20.39.2 FL 18.0 PE 0.0 TL 214.0 P V 0.6 46 38 - 40 141.8 3.260 120 PL 12.5 0.019 PF 0.25.5 FL 0.0 PE 0.0 TL 12.5 PV 0.2 47 39 - 41 533.4 4.260 120 PL 12.5 0.061 PF 0.812.0 FL 0.0 PE 0.0 TL 12,5, PV 1.0 48 41 47.2 1.442 120 PL 196.0 0.135 PF 29.0429.3 Ft_ 18.0 PE 0.0 TL 214.0 PV 0.6 49 40 - 95.2 3.260 120 PL 12.5 0.009 PF 0.1423.7 FL 0.0 PE 0.0 TL 12.5 PV 0.1 50 580.6 4.260 120 PL 12.5 0.072 PF 0.941 - 43 13.1 FL 0.0 PF-. 0.0 TL 12.5 PV 1.1 51 48.0 1.442 120 PI_ 196.0 0.139 PF 29.843 - 44 9.4 FL 18.0 PE 0.0 TL 214.0 PV 0.6 52 48.0 3.260 120 PL 12.5 0.003 PF 0.042 - 44 1.8 FL 0.0 PE 0.0 TL 12.5 PV 0.0 I 7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 JOB TITLE! RUSH HAMPTON - SYSTEM ##7 / AREA D (GRID) PIPE DATA (cont'd) PIPE FLOW(GPM) DIA(IN) H-W COEF LENGTH FRICTION I END NODES VEL(FPS) (FT) LOSS PSI/FT) 53 628.6 4.260 120 PL 6.3 0.083 PF 1.5 43 46 14.1 FL 12.0 PE i. `%' TL 18.3 PV 1.3 54 628.6 4.260 120 PL 47.0 0.083 PF 4.4 46 47 14.1 FL 6.0 PE 0.0 TL 53.0 PV 1.3 55 628.7 6.360 120 PL 18.9 0.012 PF 0.6 47 48 6.3 FL 35.0 PE 6.9 TL 53.9 PV 0.3 56 1128.6 8.040 150 PL 30.0 0.007 PF I 0.8 48 49 7.1 FL 73.0 PE 0.4 TL 103.0 PV 0.3 57 1128.4 9.870 150 PL 450.0 0.003 PF 1.6 49 45 4.7 FL 142.0 PE 0.0 TL. 592.0 PV 0.2 NOTES: 1) Calculations were Performed by the HASS 3.3 computer program under license no. 8101F40 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. At l ant_a, Georgia 30345 i e 2) The system has been balanced to provide an average imbalance .it each node-. of 0.133 gpm and a maximum imbalance at any node of 0.844 gpm. 3) Velocity pr•es•sur•e.s are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 20.7 ft/sec. 4) a. System remote area HAS been proven or 'peaked'. b. Minimum pressure at any sprinkler: 19.931 psi c. Minimum pressure with remote area shifted i one sprinkler space toward near cross main: 20.009 psi I d. Minimum pressure with remote area shifted one sprinkler space- toward far cross main: 19.987 psi J JOB TITLE: FLOW DIAGRAM RUSH HAMPTON - SYSTEM #7 / AREA D (GRID) T 106.0 77.7 51.5 :26.2 1.3 23.8 49.0 75.2 103.0 T 106.0 T i. 0 3. T C 1 i._l•--:>---•--;>---•--::>---••--:>----->---*--•::---+ t•-_<::__--x•---•c:---•--<.:---•(: T 106.1 77.8 51.5 26.2 1.3 23.8 49.1 75.3 103.1 T 212.0 206.4 T C 21 7+E--;>---+c-->--- 106.5 78.0 51.6 .26.2 1.2 24.0 49.4 75.6 103.6 v 318.4 4. C 313*------------------------------>-- v 41. 1 T 359. 5 269. 0 T C331*------------------------------'>------------------------------- f 41. 7 T 401.2 7.3 T t C35 3*------------------------------'>------------------- T 42. 7 T 443.9 i. 6 T T C37 1*------------------------------- >- T 44. 2 T 488.2 140. 4 t t C391*------------------------------ T 46. 2 T 534.3 94. '. T T C41 7 ------------------------------------------------------------- C 4'.:I T 46. 7 T 581.1 47.5 T T C431*-------------------------------:-----------__---.------------------*1. 44 3 47.5 4l r-o P j3/&a