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1 LEGO DR; ; AS970194; Permit
3/8/24, 12:06 PM AS9701 94 Permit Data City of Carlsbad AUTOMATIC SPRINKLER-COMM Permit No: AS970194 Job Address: 1 LEGO DR Status: ISSUED Permit Type: ASC Applied 12/9/1997 Parcel No: 2110221600 Approved: 2/19/1998 Lot#: 0 Reference No.: Issued: 2/19/1998 PC#: Inspector: Project Title: LEGOLAND CARLSBAD ADMIN #1 BLDG Applicant: GRINNELL FIRE PROTECTION 4223 PON DEROSA AVE STE D SAN DIEGO CA 619-279-1980 about:blank Fees($) 710 Add'I Fees($) 0 Owner: CARLSBAD ESTATE HOLDING INC Total($) 710 1/1 LEGOLAND -ADMINISTRATION ROOF AREA SWAY BRACE CONNECTION THROUGH WOOD MEMBER Line Hanger Average Weight = 18.0 +250.0 = 268.0 Main Hanger Average Weight = 24.5 +250.0 = 274.5 Lateral Sway Brace -Condition #1 (94) 4 -6.4.3.5.7 Exception -Worst Case Area@ Roof Zone Of Influence = 0' -0" @ Bulk Main = 40' -O" @ Mains = SWAY BRACE AT 40' MAX. = 114' -0" @ Branch Mains ( 4 ) typ. 40' -0" of 4" X 5.89Ibs./ft. = 235.6 00' -0" of 2½" x 2. 95Ibs./ft. = 00.0 00' -0" of 2" x 2.11 lbs./ft. = 00.0 00' -0" of 1½" X 1.52Ibs./ft. = 00.0 518' -0" of 1 ¼" x 1.26Ibs./ft. = 652.7 331 '-0" of 1" x 0.91 lbs.lft. = 301.2 ½ Weight of water filled pipe = 1189.5 < (94) 4 -6.4.3.5.3 -1" schd.10 x 7' -0" ( maximum ) Length @ 30" -44" = 1767 > 1189.5 (94) 4 -6.4.3.5.4 -½" x 4" Through Bolt In Wood ( Perpendicular) Config. f @ 60" -90" = 1247 > 1189.5 Longitudinal Sway Brace -Condition #2 (94) 4 -6.4.3.5.7 Exception -Worst Case Area@ Roof = SWAY BRACE AT 80' MAX. Zone Of Influence = 80' -0" @ Bulk Main 80' -O" of 4" x 5.89Ibs./ft. = 453.5 ½ Weight of water filled pipe = 453.5 < (94) 4 -6.4.3.5.3 -1" schd.10 x 7' -O" ( maximum ) Length @ 30° -44° = 1767 > 1189.5 (94) 4 -6.4.3.5.4 -½" x 4" Through Bolt In Wood ( Perpendicular) Config. f @ 60° -90° = 1247 > 1189.5 GRINNELL FIRE PROTECTION 4223 PONDEROSA AVENUE SUITED SAN DIEGO, CA. 92123 HYDRAULIC CALCULATIONS FOR LEGOLAND -CARLSBAD 5342 ARMADA DRIVE ·CARLSBAD,CALIFORNIA 92008 FILE NUMBER: LEG0230P .SDF ADMINISTRATION BLDG.PENDENTS DATE: Dec 04, 1997 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: SPRINKLER K-FACTOR: SPRINKLER MAX. COVERAGE AREA: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose}: SYSTEM FLOW(@ BORA): SYSTEM PRESSURE (@BORA): DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: LIGHT HAZARD SYSTEM 0.10 GPM/SQ.FT. 1,500.00 SQ.FT. 168 SQ.FT. 5.6 / 1/2" ORIFICE 168 SQ.FT./ MIN: 9.0 psi 14 SPRINKLER HEADS 285.6 GPM 385.6 GPM 285.6 GPM 49.3 PSI CHRISTOPHER FRYE CARLSBAD FIRE DEPT. C-16 / #280123 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 4C1324B) HRS SYSTEMS, INC. ATLANTA, GA ,. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203P .SDF JOB TITLE: ADMINISTRATION BUILDING PENDENTS WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) LEGO 109.0 84.0 3545.0 108.6 385.6 93.8 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 385.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 100.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 285.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE .TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 '162.5 K= 5.60 10.9 18.5 2 165.6 ----10.4 --- 3 165.6 ----10.8 --- 4 162.5 K= 5.60 10.8 18.4 5 165.6 ----10.4 --- 6 165.6 ----11.1 --- 7 162.5 K= 5.60 11.2 18.8 8 165.6 ----11.5 --- 9 165.6 ----12.1 --- 10 162.5 K= 5.60 13.1 20.3 11 165.6 ----13.6 --- 12 165.6 ----14.4 --- 13 162.5 K= 5.60 16.2 22.6 14 165.6 ----17.5 --- 15 165.6 ----18.4 --- 16 165.6 25.0 --- 17 165.6 ----38.8 --- 18 162.5 K= 5.60 14.8 21. 5 19 165.6 ----15.8 --- 20 165.6 ----16.2 --- 21 165.6 ----16.6 --- 22 162.5 K= 5.60 14.9 21. 6 23 165.6 ----16.2 --- 24 165.6 ----17.0 --- 25 162.5 K= 5.60 16.3 22.6 26 165.6 ----17.5 --- 27 165.6 ----18.4 --- 28 162.5 K= 5.60 19.2 24.6 29 165.6 ----20.4 --- 30 165.6 21. 5 --- 31 165.6 27.1 --- 32 165.6 38.8 --- 33 162 _.5 K= 5.60 9.0 16.8 34 165.6 ----·9,2 --- I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 12/04/1997 C:\HASS62\FI LES\LEGOLA-1\LEGO203P.SDF JOB TITLE: ADMINISTRATION BUILDING PENDENTS NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 165.6 ----9.7 --- 36 162.5 K= 5.60 9.7 17.4 37 165.6 ----9.8 --- 38 165.6 ----10.3 --- 39 162.5 K= 5.60 11.1 18.7 40 165.6 ----11. 3 --- 41 165.6 ----13.3 --- 42 162.5 K= 5.60 13.7 20.7 43 165.6 ----14.6 --- 44 165.6 ----15.4 --- 45 162.5 K= 5.6 0 17.1 23.2 46 165.6 18.2 --- 47 165.6 ----19.2 --- 48 165.6 25.5 --- 49 165.6 38.9 --- so 165.6 40.2 --- 51 165.6 41.7 --- 52 165.6 ----42.2 --- 53 165.6 ----43.3 --- 54 165.6 43.6 --- TORA 165.6 44.0 --- BORA 154.0 49.3 --- UGA 150.0 51.5 --- AUG4 151.0 54.6 --- AUG3 151. 0 54.6 --- BFP2 157.0 52.0 --- BFPl 157.0 64.0 --- AUG2 151.0 HOSE STREAM 66.7 100.0 AUGl 151.0 66.8 --- LEGO12 150.0 67.4 --- LEGOll 150.0 67.5 --- LEGO l 0 1.50. 0 67.7 --- 'LEGO9 150.0 68.3 --- LEGO8 150.0 68.7 --- LEGO7 150.0 69.2 --- LEGO6 150.0 69.5 --- LEGO5 150.0 70.1 --- LBFP2 150.0 70.1 --- LBFPl 150.0 81.1 --- LEGO4 150.0 81.1 --- METER2 150.0 81.2 --- METERl 150.0 86.2 --- LEGO3 134.0 93.2 --- LEGO2 133.0 93.8 --- LEGO 133.0 SOURCE 93.8 385.6 l ~ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEG0203P.SDF JOB TITLE: ADMINISTRATION BUILDING PENDENTS 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) F .L. /FT (PSI) Pipe: 1 -18.5 1.049 PL 3.00 PF 0.9 1 162.5 5.6 10.9 18.5 6.9 120 FTG T PE -1. 3 2 165.6 0.0 10.4 0.0 0.112 TL 8.00 PV 0.3 Pipe: 2 -18.5 1. 049 PL 1.00 PF 0.3 2 165.6 0.0 10.4 0.0 6.9 120 FTG E PE 0.0 3 165.6 0.0 10.8 0.0 0.112 TL 3.00 PV 0.3 Pipe: 3 -18.5 1. 380 PL 10.00 PF 0.3 3 165.6 0.0 10.8 0.0 4.0 120 FTG PE 0.0 6 165.6 0.0 11.1 0.0 0.030 TL 10.00 PV 0.1 Pipe: 4 -18.4 1. 049 PL 3.00 PF 0.9 4 162.5 5.6 10.8 18.4 6.8 120 FTG T PE -1.3 5 165.6 0.0 10 .4 0.0 0.112 TL 8.00 PV 0.3 Pipe: 5 -18.4 1.049 PL 1.00 PF 0.7 5 165.6 0.0 10.4 0.0 6.8 120 FTG T PE 0.0 6 165.6 0.0 11.1 0.0 0.112 TL 6.00 PV 0.3 Pipe: 6 -36.9 1.380 PL 9.70 PF 1.0 6 165.6 0.0 11.1 0.0 7.9 120 FTG PE 0.0 9 165.6 0.0 12.l 0.0 0.106 TL 9.70 PV 0,4 Pipe: 7 -18.8 1.049 PL 4.80 PF 1. 6 7 162.5 5.6 11. 2 18.8 7.0 120 FTG 2ET PE -1. 3 8 165.6 0.0 11. 5 0.0 0.116 TL 13.80 PV 0.3 Pipe: 8 -18;8 1. 049 PL 0.50 . PF 0.6 8 165.6 0.0 11. 5 o.b 7.0 120 FTG T PE 0.0 9 165.6 0.0 12.1 0.0 0.116 TL 5.50 PV ~ 0.3 Pipe: 9 -55.7 1. 380 PL 10.00 PF 2.3 9 165.6 0.0 12.1 0.0 11. 9 120 FTG PE 0.0 12 165.6 0.0 14.4 0.0 0.227 TL 10.00 PV 1. 0 Pipe: 10 -20.3 1.049 PL 5.00 PF 1. 9 10 162.5 5.6 13.1 20.3 7.5 120 FTG 2ET PE -1.3 11 165.6 0.0 13.6 0.0 0.133 TL 14.00 PV 0.4 Pipe: 11 -20.3 1. 049 PL 0.50 PF 0.7 11 165.6 0.0 13.6 0.0 7.5 120 FTG T PE 0.0 12 165.6 0.0 14.4 0.0 0.133 TL 5.50 PV 0.4 Pipe: 12 -76.0 1. 380 PL 10.00 PF 4.0 12 165.6 0.0 14.4 0.0 16.3 120 FTG PE 0.0 15 165.6 0.0 18.4 0.0 0.404 TL 10.00 PV 1. 8 Pipe: 13 -22.6 ·1.049 PL 7.10 PF 2.6 13 162.5 5.6 16.2 22.6 8.4 120 FTG 2ET PE -1. 3 14 165.6 0.0 17.5 0.0 0.163 TL 16.10 PV 0 ~5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203P.SDF JOB TITLE: ADMIN I STRATION BUILDING PENDENTS PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT} SUM. NODES (FT) ( K) (PSI) (GPM) F .L. /FT (PSI) Pipe: 14 -22.6 1.049 PL 0.50 PF 0.9 14 165.6 0.0 17.5 0.0 8.4 120 FTG T PE 0.0 15 165.6 0.0 18.4 0.0 0.163 TL 5 .50 PV 0.5 Pipe: 15 -98.5 1. 380 PL 10.00 PF 6.5 15 165.6 0.0 18.4 0.0 21.1 120 FTG PE 0.0 16 165.6 0.0 25.0 0.0 0 .654 TL 10.00 PV 3.0 Pipe: 16 -98.5 1.380 PL 15.20 PF 13.9 16 165.6 0.0 25.0 0.0 21.1 120 FTG T PE 0.0 17 165 .6 0.0 38.8 0.0 0.654 TL 21. 20 PV 3.0 Pipe: 17 -98.5 4.260 PL 13.00 PF o.o 17 165.6 0.0 38.8 0.0 2.2 120 FTG PE 0.0 32 165 .6 o.o 38.8 0.0 0.003 TL 13.00 PV 0.0 Pipe: 18 -21. 5 1. 049 PL 7.10 PF 2.4 18 162.5 5.6 14.8 21. 5 8.0 120 FTG 2ET PE -1.3 19 165.6 0 .0 15.8 0.0 0.149 TL 16.10 PV 0.4 Pipe : 19 -21. 5 1.049 PL 0.50 PF 0.4 19 165.6 0.0 15.8 0.0 8 .0 120 FTG E PE 0.0 20 165.6 0.0 16 .2 0.0 0.149 TL 2.50 PV 0.4 Pipe : 20 -21. 5 1. 380 PL 10.00 PF 0.4 20 165.6 0.0 16.2 0.0 4.6 120 FTG PE 0.0 21 165.6 0.0 16.6 0.0 0.039 TL 10.00 PV 0.1 Pipe: 21 -21.5 .1 .. 380 PL .lO .00 PF 0 .4 21 165.6 0 .0 16.6 0.0 4.6 • i20 FTG PE 0 .0 24 165.6 0.0 17.0 0.0 0.039 TL 10.00 PV • 0.1 Pipe: 22 -21.6 i.049 PL 8.30 PF 2.6 22 162.5 5.6 14 .9 21. 6 8.0 120 FTG 2ET PE -1.3 23 165.6 0.0 16.2 0.0 0.150 TL 17.30 PV 0.4 Pipe: 23 -21. 6 1.049 PL 0.50 PF 0.8 23 165.6 0.0 16.2 0.0 8.0 120 FTG T PE 0.0 24 165.6 0.0 17.0 0.0 0.150 TL 5.50 PV 0.4 Pipe: 24 -43.1 1.380 PL 10.00 PF 1.4 24 165 .6 0.0 17.0 0.0 9.3 120 FTG PE 0.0 27 165.6 0.0 18.4 0.0 0.142 TL 10.00 PV 0.6 Pipe: 25 -22.6 1.049 PL 6.50 PF 2 .5 25 162.5 5.6 16.3 22.6 8.4 120 FTG 2ET PE -1. 3 26 165.6 0.0 17.5 0.0 0.163 TL 15.50 PV 0 .5 Pipe: 26 -22.6 1.049 PL 0.50 PF 0.9 26 165.6 0.0 17.5 0.0 8.4 120 FTG T PE 0.0 27 -165 .6 0.0 18 .4 0.0 0.163 TL 5.50 PV 0 .5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA~1\LEGO203P.SDF JOB TITLE: ADMINISTRATION BUILDING PENDENTS PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C ) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 -65.7 1.380 PL 10.00 PF 3.1 27 165 .6 0.0 18.4 0.0 14.1 120 FTG PE 0.0 30 165.6 0.0 21.5 0.0 0.309 TL 10.00 PV 1. 3 Pipe: 28 -24.6 1_.049 PL 4.50 PF 2.6 28 162.5 5.6 19.2 24.6 9.1 120 FTG · 2ET PE -1.3 29 165.6 0.0 20.4 0.0 0.190 TL 13.50 PV 0.6 Pipe: 29 -24.6 1.049 PL 0.50 PF 1.0 29 165.6 0.0 20.4 0.0 9.1 120 FTG T PE 0.0 30 165.6 0.0 21.5 0.0 0.190 TL 5.50 PV 0.6 Pipe: 29A -90.3 1. 380 PL 10.00 PF 5.6 30 165.6 0.0 21. 5 0.0 19.4 120 FTG PE 0.0 31 165.6 0.0 27.1 0.0 0.556 TL 10.00 PV 2.5 Pipe: 30 -90.3 1.380 PL 15.20 PF 11.8 31 165.6 0.0 27.1 0.0 19.4 120 FTG T PE 0.0 32 165.6 0.0 38.8 0 .0 0.556 TL 21. 20 PV 2.5 Pipe: 31 -188.8 4.260 PL 8.00 PF 0.1 32 165.6 0.0 38 .8 0.0 4.3 120 FTG PE 0.0 49 165.6 0.0 38.9 0.0 0.009 TL 8.00 PV 0.1 Pi pe : 32 -16.8 1.049 PL 7.00 PF 1.5 33 162.5 5.6 9.0 16.8 6.2 120 FTG 2ET PE -1. 3 34 165.6 0.0 9 .2 0 .0 0.094 TL 16.00 PV 0.3 Pi pe: 33 -16 .. 8 l. 049 PL 0.50 . PF 0.5 34 165.6 0.0 9.2 0.0 6.2 120 FTG T PE 0.0 35 165 .6 0.0 9.7 0.0 0.094 TL 5.50 PV I 0.3 Pipe: 34 -16.8 1.380 PL 3.80 PF 0.1 35 165.6 0.0 9.7 0.0 3.6 120 FTG PE 0.0 37 165.6 0.0 9.8 0.0 0.025 TL 3.80 PV 0.1 Pipe: 35 -17.4 1.049 PL 7.30 PF 1.4 36 162.5 5.6 9.7 17.4 6.5 120 FTG ET PE -1.3 37 165.6 0.0 9.8 0.0 0.101 TL 14.30 PV 0.3 Pipe: 36 -34.2 1. 380 PL 6.10 PF 0.6 37 165.6 0.0 9.8 0.0 7.3 120 FTG PE 0.0 38 165.6 0.0 10.3 0.0 0.092 TL 6.10 PV 0.4 Pl pe: 37 -34.2 1. 380 PL 6.90 PF 0.9 38 165.6 0.0 10.3 0.0 7.3 120 FTG E PE 0.0 40 165.6 0.0 11.3 0.0 0.092 TL 9.90 PV 0.4 Pipe: 38 -18.7 1.049 PL 4.00 PF 1.5 39 162.S 5.6 11.1 18.7 6.9 120 FTG 2ET PE -1.3 4 0 165 .6 0 .. 0 11 .3 0.0 0.114 TL 13 .00 PV 0.3 j. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 12/04/199? C:\HASS62\FILES\LEGOLA~l\LEGO203P.SDF JOB TITLE! ADMINISTRATION BUILDING PENDENTS PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT} ( K) (PSI) (GPM) F. L. /FT (PSI) Pipe: 39 -52.9 1.380 PL 6.90 PF 2.0 40 165.6 0.0 11. 3 o.o 11.3 120 FTG E PE 0.0 41 165.6 0.0 13.3 0.0 0.207 TL 9.90 PV 0.9 Pipe: 40 -52.9 1. 380 PL 10.00 PF 2.1 41 165.6 0.0 13.3 0.0 11.3 120 FTG PE 0.0 44 165.6 0.0 15.4 0.0 0.207 TL 10.00 PV 0.9 Pipe: 41 -20.7 1.049 PL 7.00 PF 2.2 42 162.5 5.6 13.7 20.7 7.7 120 FTG 2ET PE -1. 3 43 165.6 0.0 14.6 0.0 0.139 TL 16.00 PV 0.4 Pipe: 42 -20.7 1.049 PL 0.50 PF 0.8 43 165.6 0.0 14.6 0.0 7 .7 120 FTG T PE 0.0 44 165.6 0.0 15.4 0.0 0.139 TL 5.50 PV 0.4 Pipe: 43 -73.6 1.380 PL 10.00 PF 3.8 44 165.6 0.0 15.4 0.0 15.8 120 FTG PE 0.0 47 165.6 0.0 19.2 0.0 0.381 TL 10.00 PV 1. 7 Pipe: 44 -23.2 1.049 PL 5.60 PF 2.5 45 162.5 5.6 17.1 23.2 8.6 120 FTG 2ET PE -1. 3 46 165.6 0.0 18.2 0.0 0.171 TL 14.60 PV 0.5 Pipe: 45 -23.2 1. 049 PL 0.50 PF 0.9 46 165.6 0.0 18.2 0.0 8.6 120 FTG T PE 0.0 47 165.6 0.0 19.2 0.0 0.171 TL 5.50 PV 0.5 P_ipe: 46 . -96 . 8 1.380 PL 10. 00 • PP 6.3 47 165.6 0.0 19.2 0.0 20.8 120 FTG PE 0.0 48 165.6 0.0 25.5 0.0 0.633 TL 10.00 PV : 2.9 Pipe: 47 -96.8 1. 380 PL 15.20 PF 13.4 48 165.6 0.0 25.5 0.0 20.8 120 FTG T PE 0.0 49 165.6 0.0 38.9 0.0 0.633 TL 21.20 PV 2 .9 Pipe: 48 -285.6 4.260 PL 50.00 PF 1. 3 49 165.6 0.0 38.9 0.0 6.4 120 FTG T PE 0.0 50 165.6 0.0 40.2 0.0 0.019 TL 66.00 PV 0.3 Pipe: 49 -285.6 4.260 PL 72.00 PF 1.5 50 165.6 0.0 40.2 0.0 6.4 120 FTG E PE 0.0 51 165.6 0.0 41. 7 0.0 0.019 TL 79.00 PV 0.3 Pipe: 50 -285.6 4.260 PL 6.50 PF 0.4 51 165.6 0.0 41. 7 0.0 6.4 120 FTG T PE 0.0 52 165.6 0.0 42.2 0.0 0.019 TL 22.§0 PV 0.3 Pipe: 5°1 -285.6 4.260 PL 44.20 PF 1.2 52 165.6 0.0 42.2 0.0 6.4 120 FTG T PE 0.0 53 16_5. 6 0.0 43.3 o.o · 0.019 TL _ 60.20 PV 0.3 -- " SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEG0203P.SDF JOB TITLE: ADMINISTRATION BUILDING PENDENTS PIJ?E DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C} (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 52 -285.6 4.260 PL 9.50 PF 0.3 53 165.6 0.0 43.3 0.0 6.4 120 FTG E PE 0.0 54 165.6 0.0 43.6 0.0 0.019 TL 16.50 PV 0.3 Pipe: 53 -285.6 4.260 PL 12.50 PF 0.4 54 165.6 0.0 43.6 0.0 6.4 ·120 FTG E PE 0.0 TORA 165.6 0.0 44.0 0.0 0.019 TL 19.50 PV 0.3 Pipe: 54 -285.6 4.260 PL 11.70 PF 0.2 TORA 165.6 0.0 44.0 0.0 6.4 120 FTG PE 5.0 BORA 154.0 0.0 49.3 0.0 0.019 TL 11.70 PV 0.3 Pipe: 55 -285.6 4.280 PL 15.00 PF 0.5 BORA 154.0 0.0 49.3 0.0 6.4 140 FTG 2E PE 1.7 UGA 150.0 0.0 51. 5 0.0 0.014 TL 37.00 PV 0.3 Pipe: 56 -285.6 4.070 PL 185.00 PF 3.5 UGA 150.0 0.0 51.5 0.0 7.0 150 FTG TG PE -0.4 AUG4 151. 0 0 .0 54.6 0.0 0.016 TL 218.00 PV 0.3 Pipe: 57 -285.6 7.680 PL 28.00 PF 0.0 AUG4 151.0 0.0 54.6 0.0 2.0 150 FTG E PE 0.0 AUG3 151.0 0.0 54.6 0.0 0.001 TL 52.00 PV 0.0 Pipe: 58 -285.6 8.510 PL 6.00 PF 0.0 AUG3 151.0 0.0 54.6 0.0 1.6 140 FTG T PE -2.6 BFP2 157.0 0.0 52.0 0.0 0.000 TL 53.00 PV 0.0 Pipe: 59 FIXED PRESSURE LOSS.DEVICE BFPi 157.0 0.0 64.0 0.0 12.o ·psi, 285.6 .gpm BFP2 157.0 0.0 52.0 0.0 Pipe: 60 -285.6 8.510 PL 6.00 PF 0.0 BFPl 157.0 0.0 64.0 0.0 1. 6 140 FTG 2E PE 2.6 AUG2 151.0 H.S. 66.7 100.0 0.000 TL 48.00 PV 0.0 Pipe: 61 -385.6 7.680 PL 18.00 PF 0.1 AUG2 151.0 H.S. 66.7 100.0 2.7 150 FTG T PE 0.0 AUGl 1§1.0 0.0 66.8 0.0 0.001 TL 71.00 PV o.6 Pipe: 62 -385.6 7.680 PL 115.00 PF 0.2 AUGl 151.0 0.0 66.8 0.0 2.7 150 FTG TG PE 0.4 LEG012 150.0 0.0 67.4 0.0 0.001 TL 174.00 PV 0.0 Pipe: 63 -385.6 7.680 PL 38.00 PF 0.1 LEG012 150.0 0.0 67.4 0.0 2.7 150 FTG E PE 0.0 LEGOll 150.0 0.0 67.5 0.0 0.001 TL 62.00 PV 0.0 Pipe: 64 -385.6 7.680 PL 145.00 PF 0.3 LEGOll 150.0 0.0 67.5 0.0 2.7 150 FTG TG PE 0.0 LEGOlO 150.0 0.0 67.7 0.0 0.001 TL 204.00 .. _PV 0.0 • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203P.SDF JOB TITLE, ADMINISTRATION BUILDING PENDENTS PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI} (GPM) F .L. /FT (PSI) Pipe: 65 -385.6 7.680 PL 410.00 PF 0.5 LEGOl0 150.0 0.0 67. 7 0.0 2.7 150 FTG PE 0.0 LEGO9 150.0 0.0 68.3 0.0 0.001 TL 410.00 PV 0.0 Pipe: 66 -385.6 7 .680 PL 327.00 PF 0.4 LEGO9 150.0 0.0 68.3 0. 0 ., 2.7 150 FTG PE 0.0 LBGO8 150.0 0.0 68.7 0.0 0.001 TL 327.00 PV 0.0 Pipe: 67 -385.6 7.680 PL 390.00 PF 0 .5 LEGO8 150.0 0.0 68.7 0.0 2.7 150 FTG B PE 0.0 LEGO? 150.0 0.0 69.2 0 .0 0.001 TL 414.00 PV 0.0 Pipe: 68 -385.6 7.680 PL 212.00 PF 0.3 LEGO7 150.0 0.0 69.2 0.0 2.7 150 FTG TG PE 0.0 LEGO6 150.0 0.0 69.5 0.0 0.001 TL 271. 00 PV 0.0 Pipe: 69 -385.6 7.680 PL 400.00 PF 0.5 LEGO6 150.0 0.0 69.5 0.0 2.7 150 FTG E PE 0.0 LEGO5 150.0 0.0 70.1 0.0 0.001 TL 424.00 PV 0.0 Pipe: 70 -385.6 8.510 PL 6.00 PF 0.0 LEGOS 150.0 0.0 70.1 0.0 2.2 140 FTG E PE 0.0 LBPP2 150.0 0.0 70.1 0.0 0.001 TL 27.00 PV 0.0 Pipe: 71 FIXED PRESSURE LOSS DEVICE LBFPl 150.0 0.0 81.1 0.0 11.0 psi, 385 .6 gpm LBFP2 150.0 0.0 70.1 0.0 . Pipe: 72 .·-385.6 8.510 PL 6.00 PF 0.0 LBFPl 150.0 0.0 81.1 0.0 2.2 140 FTG 2E PE 0.0 LEGO4 150.0 0.0 81.1 0.0 0.001 TL 48.00 PV ' 0 .0 Pipe: 73 -385.6 8.510 PL 10.00 PF 0.0 LEGO4 150.0 0.0 81.1 0.0 2 .2 140 FTG PE 0.0 METER2 150.0 0.0 81.2 0.0 0.001 TL 10.00 PV 0.0 Pipe: 74 FIXED PRESSURE LOSS DEVICE METERl 150.0 0.0 86.2 0.0 5.0 psi, 385.6 gpm METER2 150.0 0.0 81.2 0.0 Pipe: 75 -385.6 8.510 PL 110.00 PF 0.1 METERl 150.0 0.0 86.2 0.0 2.2 140 FTG TG PE 6.9 LEGO3 134.0 0.0 93.2 0.0 0.001 TL 163.00 PV 0.0 Pipe: 76 -385.6 11.650 PL 485.00 PF 0.1 LEG03 134.0 0.0 93.2 0.0 1. 2 150 FTG T2G PE 0.4 LBGO2 133.0 0.0 93.8 0.0 0.000 TL §94.00 PV 0.0 Pipe: 77 -385.6 11.650 PL 150.00 PF 0.0 LEGO2 133.0 0.0 93.8 0.0 1. 2 150 FTG TG PE 0.0 LEGO 133.0 SflCE 93.8 lN/A) 0.000 TL250.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEG0203P.SDF JOB TITLE: ADMINISTRATION BUILDING PENDENTS NOTES: (1) Calculations were performed by the HASS 6.2.0 computer program under license no. 422C1327E granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.152 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 21.1 ft/sec at pipe 15. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A Diameter ( in) l.0'19 1.380 PAGE: B Diameter (in) MATERIAL: S40/TG HWC: 120 Equivalent Fitting Lengths E T L C B Ell Tee 45'Ell ChkVlv BfyVlv 2.00 3.00 5.00 6.00 1.00 1.00 5.00 7.00 6.00 6.00 MATERIAL: TWL/GG HWC: 120 Equivalent Fitting Lengths E T L C B Ell Tee 45'Ell ChkVlv BfyVlv in Feet G A GatVlv AlmChk 1..00 1.00 in Feet 0.10 0.10 G A GatVlv AlmChk D DPVlv 0.10 0.10 D DPVlv 4.260 PAGE: D Diameter (in) 7.00 16.00 3.50 22.00 12.00 2.00 17.00 12.00 4.280 8.510 PAGE: E Diameter ( in) 11. 650 PAGE: K Diameter (in) 4.070 7.680 MATERIAL: DIRON HWC: 140 Equivalent Fitting Lengths E T L C B Ell Tee 45'Ell ChkVlv BfyVlv 11.00 27.00 8.00 30.00 16.00 21.00 47.00 17.00 60.00 16.00 MATERIAL: PVC150 HWC: 150 Equivalent Fitting Lengths E T L C B Ell Tee LngEll ChkVlv BfyVlv 33.00 91.00 27.00 98.00 32.00 MATERIAL: PVC200 HWC: 150 Equivalent Fitting Lengths E T L C B Ell Tee LngEll ChkVlv BfvVlf 12.00 30.00 9.00 33.00 18.00 24.00 53.00 20.00 68~00 18.00 in Feet G D GatVlv DetChk 3.00 39.00 6.00 78.00 in Feet G D GatVlv DetChk 9.00 105.00 in Feet G D GatVlv DetChk 3.00 39.00 6.00 78.0Cl. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203P JOB TITLE: ADMINISTRATION BUILDING PENDENTS WATER SUPPLY CURVE -lo?:- ,,.__ ,.. VI a. w a ::J (./) (./) w a 0. w ~ <C ~ WAT E R S UPPLY AN AL Y S I S Static : 109.00 ps i Re si d : 84.00 ps i Flow: 3545.0 gpm 120.0 t--r-------------------------, 100.0 1~· l 9~.t>P~I ', ' & "761=,,l'P~PM ., , .... , 80.0 ,, ,, "o . ..... 60.0 40.0 20.0 - 0.0 -14.7 _____ _.__...._ _ _._ _____ .._ __ ...._ ___ ..._ ___ .... 80Q 2001600 2000 2400 2800 3200 3600 4000 FLOW (GPM) LEGEND AvaLlable pressure 108. 59 psi e 385. 6 gpm Required pressure 93. 80 psi e 385. 6 gpm SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203P.SDF JOB TITLE: ADMINISTRATION BUILDING PENDENTS WATER SUPPLY CURVE 120+ 110*\\\\\ 0 \\\\\ \\\\\ \\\\\ 100+ \\\\\ \\\\\\ X \\\\\ \\\\\ 90+ \\\\\ P 80+ R E s S 70+ u R E 60+ ( p s I 50+ ) 40+ 30+ 20+ 10+ X 0 LEGEND = Required Water Supply 93.80 psi @ 385.6 gpm = Available Water Supply 108.59 psi @ 385 .6 gpm \\\\\ 84.0 psi@ 3545 gpm-> * Flow Test Point " II " " " " II " 0++-+---+----+-----+------+--------+--------+---------+-----------+ I... 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) GRINNELL FIRE PROTECTION 4223 PONDEROSA AVENUE SUITED SAN DIEGO, CA. 92123 HYDRAULIC CALCULATIONS FOR LEGOLAND -CARLSBAD 5342 ARMADA DRIVE CARLSBAD,CALIFORNIA 92008 FILE NUMBER: LEGO230U.SDF ADMINISTRATION BLDG.UPRIGHTS DATE: Dec 04, 1997 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: SPRINKLER K-FACTOR: SPRINKLER MAX. COVERAGE AREA: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose): SYSTEM FLOW (@BORA): SYSTEM PRESSURE (@BORA): DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: LIGHT HAZARD SYSTEM 0.10 GPM/SQ.FT. 1,500.00 SQ.FT. 130 SQ.FT. 5.6 / 1/2 11 ORIFICE 130 SQ.FT./ MIN: 7.0 psi 15 SPRINKLER HEADS 255.8 GPM 355.8 GPM 255.8 GPM 38.7 PSI CHRISTOPHER FRYE CARLSBAD FIRE DEPT. C-16 / #280123 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 4Cl324B) HRS SYSTEMS, INC. ATLANTA, GA ...... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203U.SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL . TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PS I ) (PSI) (GPM) (PSI ) (GPM) (PSI) LEGO 109.0 84.0 3545.0 108.6 355.8 82.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 355.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 100.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 255.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 162.5 ----9.1 --- 2 165.6 K= 5.60 7.7 15.6 3 165.6 ----8 .0 --- 4 162.5 ----9.0 --- 5 165.6 K= 5.60 7.7 15.5 6 165.6 ----8.2 --- 7 162.5 ----9.8 --- 8 165.6 K= 5.60 8.4 16.3 9 165.6 ----8.9 --- 10 162.5 ----11.4 --- 11 165.6 K= 5.60 10.0 17.7 12 165.6 ----10.6 --- 13 162.5 ----14 .3 --- 14 165.6 K= 5.60 12.9 20.1 15 165.6 ----13.7 --- 16 165.6 ----18.7 --- 17 165.6 ----29.3 --- 18 162.5 ----9.0 --- 19 165.6 K= 5.60 7.7 15.5 20 165.6 ----7.9 --- 21 165.6 K= 5.60 8.1 15.9 22 162.5 ----9.7 --- 23 165.6 K= 5.60 8.4 16.2 24 165.6 ----8.9 --- 25 162.5 ----11.3 --- 26 165.6 K= 5.60 10.0 17.7 27 165.6 ----10.6 --- 28 162.5 ----14.2 --- 29 165.6 K= 5.60 12.9 20.1 30 165.6 13.6 --- 31 165.6 ----18.6 ---32 165.6 --29.3 --- 33 162.5 8,.3 --- 34 165'. 6 K= 5.6 0 7.0 14.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203U .SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 165.6 ----7.4 --- 36 162.5 ----8.8 --- 37 165.6 7.5 --- 38 165.6 K= 5.60 7.6 15.4 39 162.5 ----9.7 --- 40 165.6 ----8.3 --- 41 165.6 K= 5.60 9.1 16.9 42 162.5 ----11.5 --- 43 165.6 K= 5.60 10.2 17.8 44 165.6 ----10.7 --- 45 162.5 ----14.4 --- 46 165.6 K= 5.60 13.0 20.2 47 165.6 ----13.8 --- 48 165.6 18.8 --- 49 165.6 ----29.3 --- 50 165.6 30.4 --- 51 165.6 31. 6 --- 52 165.6 32.0 --- 53 165.6 ----32.9 --- 54 165.6 ----33.2 --- TORA 165.6 ----33.5 --- BORA 154.0 ----38.7 --- UGA 150.0 ----40.9 --- AUG4 151.0 ----43.3 --- AUG3 151.0 43.3 --- BFP2 157.0 40.7 --- BFPl 157.0 ----52.7 --- AUG2 151.0 HOSE STREAM 55.4 100.0 AUGl 151.0 55.4 --- LEGO12 150.0 ----56.1 --- LEGOll 150.0 ----56.1 --- LEGOl0 150.0 .. 56. 3 --- LEGO9 150.0 56.8 --- LEGO8 150.0 ----57.2 --- LEGO? 150.0 ----57.6 --- LEGO6 150.0 57.9 --- LEGO5 150.0 ----58.4 --- LBFP2 150.0 58.4 --- LBFPl 150.0 ----69.4 --- LEGO4 150.0 69.4 --- METER2 150.0 69.4 --- METERl 150.0 74.4 --- LEGO3 134.0 ----81.5 --- LEGO2 133.0 ----82.0 --- LEGO 133.0 SOURCE 82.0 355.8 ~ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 1 2/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203U.SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS PI PE DATA PI PE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC . VEL(FPS) HW (C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F .L. /FT (PSI) Pipe: 1 0.0 1.049 PL 3.00 PF 0.0 1 162.5 0.0 9.1 0.0 0.0 120 FTG T PE -1.3 2 165.6 5.6 7.7 15.6 0.000 TL 8.00 PV 0.0 Pipe: 2 -15.6 1.049 PL 1.00 PF 0.2 2 165.6 5.6 7.7 15.6 5.8 120 FTG E PE 0.0 3 165.6 0.0 8.0 0.0 0.082 TL 3.00 PV 0.2 Pipe: 3 -15.6 1. 380 PL 10 .00 PF 0.2 3 165.6 0.0 8.0 0.0 3.3 120 FTG PE 0.0 6 165.6 0.0 8.2 0.0 0.021 TL 10.00 PV 0.1 Pipe: 4 0.0 1. 049 PL 3.00 PF 0.0 4 162.5 0.0 9.0 0.0 0.0 120 FTG T PE -1. 3 5 165.6 5.6 7.7 15.5 0.000 TL 8.00 PV 0.0 Pipe: 5 -15.5 1.049 PL 1.00 PF 0.5 5 165.6 5.6 7.7 15 .5 5.8 120 FTG T PE 0 .0 6 165.6 0.0 8.2 0.0 0.081 TL 6.00 PV 0 .2 Pipe: 6 -31.1 1. 380 PL 9.70 PF 0.8 6 165 .6 0 .0 8.2 0.0 6.7 120 FTG PE 0.0 9 165.6 0.0 8.9 0.0 0.077 TL 9.70 PV 0.3 Pipe : 7 0.0 1.049 PL 4.80 PF 0.0 7 162.5 0.0 9.8 0.0 0.0 120 FTG 2ET PE -1. 3 8 165.6 5.6 8.4 16.3 0.000 TL 13.80 PV 0.0 Pipe : 8 -16.3 1. 049 PL 0.50 PF 0.5 8 165.6 5.6 8.4 16.3 6.0 120 FTG T PE 0.0 9 165.6 0.0 8.9 0.0 0.089 TL 5.50 PV . 0.2 Pipe: 9 -47.4 1.380 PL 10.00 PF 1.7 9 165 .6 0.0 8.9 0.0 10.2 120 FTG PE 0.0 12 165.6 0.0 10.6 0.0 0.169 TL 10.00 PV 0.7 Pipe : 10 0.0 1.049 PL 5.00 PF 0.0 10 162.5 0.0 11.4 0.0 0.0 120 FTG 2ET PB -1. 3 11 165.6 5.6 10.0 17.7 0.000 TL 14.00 PV 0.0 Pipe: 11 -17.7 1.049 PL 0.50 PF 0.6 11 165.6 5.6 10.0 17.7 6.6 120 FTG T PE 0.0 12 165.6 0.0 10.6 0.0 0.104 TL 5.50 PV 0.3 Pipe: 12 -65.1 1.380 PL 10.00 PF 3.0 12 165.6 0.0 10.6 0.0 14.0 120 FTG PE 0.0 15 165.6 0.0 13.7 0.0 0.304 TL 10.00 PV 1.3 Pipe: 13 0.0 1.049 PL 7.10 PF 0.0 13 162.5 0.0 14.3 0.0 0.0 120 FTG 2ET PE -1.3 14 165.6 5.6 12.9 20 .1 0.000 TL 16.10 PV .0. 0 ., SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA~l\LEGO203U.SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS PIPE DATA (cont.) PIPE TAG Q (GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F .L. /FT (PSI) Pipe: 14 -20.1 1.049 PL 0.50 PF 0.7 14 165.6 5.6 12.9 20.1 7.5 120 FTG T PE 0.0 15 165.6 0.0 13.7 0.0 0.132 TL 5.50 PV 0.4 Pipe: 15 -85.2 1. 380 PL 10.00 PF 5.0 15 165.6 0.0 13.7 0.0 18.3 120 FTG PE 0.0 16 165.6 0.0 18.7 0.0 0.500 TL 10.00 PV 2.2 Pipe: 16 -85.2 1.380 PL 15.20 PF 10.6 16 165.6 0.0 18.7 0.0 18.3 120 FTG T PE 0.0 17 165.6 0.0 29.3 0.0 0.500 TL 21.20 PV 2.2 Pipe: 17 -85.2 4.260 PL 13.00 PF 0.0 17 165.6 0.0 29.3 0.0 1.9 120 FTG PE 0.0 32 165.6 0.0 29.3 0.0 0.002 TL 13.00 PV 0.0 Pipe: 18 0.0 1.049 PL 7.10 PF 0.0 18 162.5 0.0 9.0 0.0 0.0 120 FTG 2ET PE -1. 3 19 165.6 5.6 7.7 15.5 0.000 TL 16.10 PV 0.0 Pipe: 19 -15.5 1.049 PL 0.50 PF 0.2 19 165.6 5.6 7.7 15.5 5.8 120 FTG E PE 0.0 20 165.6 0.0 7.9 0.0 0.081 TL 2.50 PV 0.2 Pipe: 20 -15.5 1.380 PL 10.00 PF 0.2 20 165.6 0.0 7.9 0.0 3.3 120 FTG PE 0.0 21 165.6 5.6 8.1 15.9 0.021 TL 10.00 PV 0.1 Pipe: 21 -3J,.4 1.380 PL 10.00 PF 0.8 21 165.6 5.6 8.1 15.9 6.7 120 FTG PE 0.0 24 165.6 0.0 8.9 0.0 0.079 TL 10.00 PV . 0.3 Pipe: 22 0.0 1. 049 PL 8.30 PF 0.0 22 162.5 0.0 9.7 0.0 0.0 120 FTG 2ET PE -1.3 23 165.6 5.6 8.4 16.2 0.000 TL 17.30 PV 0.0 Pipe: 23 -16.2 1.049 PL 0.50 PF 0.5 23 165.6 5.6 8.4 16.2 6.0 120 FTG T PE 0.0 24 165.6 0.0 8.9 0.0 0.088 TL 5.50 PV 0.2 Pipe: 24 -47.6 1.380 PL 10.00 PF 1.7 24 165.6 0.0 8.9 0.0 10.2 120 FTG PE-0.0 27 165.6 0.0 10.6 0.0 0.170 TL 10.00 PV 0.7 Pipe: 25 0.0 1.049 PL 6.50 PF 0.0 25 162.5 0.0 11.3 0.0 0.0 120 FTG 2ET PE -1. 3 26 165.6 5.6 10.0 17.7 0.000 TL 15.50 PV 0.0 Pipe; 26 -17.7 1.049 PL 0.50 PF 0.6 26 165.6 , 5.6 10.0 17.7 6.6 120 FTG T PE 0.0 27 165.6 0.0 10.6 0 .-0 0.104 TL 5.50 PV 0.3 ... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203U .SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS PIPE DATA (cont .) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS . END ELEV. NOZ. PT DI SC. VEL (FPS) HW (C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F. L. /FT (PSI) Pipe: 27 -65.3 1.380 PL 10.00 PF 3.1 27 165.6 0.0 10.6 0.0 14.0 120 FTG PE 0.0 30 165.6 0.0 13.6 0.0 0.306 TL 10.00 PV 1.3 Pipe: 28 0.0 1.049 PL 4.50 PF 0.0 28 162.5 0.0 14.2 0.0 0.0 120 FTG 2ET PE -1.3 29 165.6 5.6 12.9 20.1 0 .000 TL 13.50 PV 0.0 Pipe: 29 -20.1 1.049 PL 0.50 PF 0.7 29 165.6 5.6 12.9 20.1 7.5 120 FTG T PE 0.0 30 165.6 0.0 13.6 0.0 0.131 TL 5.50 'PV 0.4 Pipe: 29A -85.4 1.380 PL 10.00 PF 5.0 30 165.6 0.0 ·13. 6 0.0 18.3 120 FTG PE 0.0 31 1 65.6 0.0 18.6 0.0 0.502 TL 10.00 PV 2.3 Pipe: 30 -85.4 1.380 PL 15.20 PF 10.6 31 165.6 0.0 18.6 0.0 18.3 120 FTG T PE 0.0 32 165.6 0.0 29.3 0.0 0.502 TL 21.20 PV 2. 3 Pi pe: 31 -170.7 4,260 PL 8.00 PF 0.1 32 165.6 0.0 29 .3 0 .0 3.8 120 FTG PE 0.0 49 165.6 0.0 29 .3 0.0 0.007 TL 8.00 PV 0 .1 Pipe : 32 0.0 1.049 PL 7'. 00 PF 0.0 33 162.5 0.0 8.3 0.0 0.0 120 FTG 2ET PE -1. 3 34 165.6 5.6 7.0 14.8 0.000 TL 16.00 PV 0.0 Pipe: 33 -14.8 1.049 PL-0.50 PF 0.4 34 165.6 5.6 7.0 14.8 5.5 120 FTG T PE 0.0 3 5 165.6 0.0 7.4 0.0 0.075 TL 5.50 PV . 0.2 Pipe: 34 -14.8 1. 380 PL 3 .. 80 PF 0.1 35 165.6 0.0 7.4 0.0 3. 2 120 FTG PE 0.0 37 165.6 0.0 7.5 0.0 0.020 TL 3.80 PV 0.1 Pipe: 35 0.0 1.049 PL 7.30 PF 0 .0 36 162.5 0.0 8.8 0.0 0.0 120 FTG ET PE -1. 3 37 165.6 0.0 7.5 0.0 0.000 TL 14.30 PV 0.0 Pipe: 36 -14.8 1.380 PL 6.10 PF 0.1 37 165.6 0 .0 7.5 o.o 3. 2 120 FTG PE 0.0 38 165.6 5.6 7.6 15.4 0.020 TL 6.10 PV 0 .1 Pipe: 37 -30.3 1.380 PL 6.90 PF 0.7 38 165.6 5.6 7.6 15.4 6.5 120 FTG E PE 0.0 40 165.6 0.0 8.3 0.0 0.074 TL 9.90 PV 0.3 Pipe: 38 0.0 1.049 PL 4.00 PF 0.0 39 162.5 0.0 9.7 0.0 0.0 120 FTG 2ET PE -1. 3 40 165.6 0.0 8.3 0.0 0 .000 TL 13.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEG0203U.SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F .L./FT (PSI) Pipe: 39 -30.3 1.380 PL 6.90 PF 0.7 40 165.6 0.0 8.3 0.0 6.5 120 FTG E PE 0.0 41 165 .6 5.6 9.1 16.9 0.074 TL 9.90 PV 0.3 Pipe: 40 -47.1 1.380 PL 10.00 PF 1.7 41 165.6 5.6 9.1 16.9 10.1 120 FTG PE 0.0 44 165.6 0.0 10.7 0.0 0.167 TL .10. 00 PV 0.7 Pipe: 41 0.0 1.049 PL 7.00 PF 0.0 42 162.5 0.0 11.5 0.0 0.0 120 FTG 2ET PE -1. 3 43 165.6 5.6 10.2 17.8 0.000 TL 16.00 PV 0.0 Pipe: 42 -17.8 1.049 PL 0.50 PF 0.6 43 165.6 5.6 10.2 17.8 6.6 120 FTG T PE 0.0 44 165.6 0.0 10.7 0.0 0.105 TL 5.50 PV 0.3 Pipe: 43 -65.0 1. 380 PL 10.00 PF 3.0 44 165.6 0.0 10.7 0.0 13.9 120 FTG PE 0.0 47 165.6 0.0 13.8 0.0 0.303 TL 10.00 PV 1. 3 Pipe: 44 0.0 1.049 PL 5.60 PF 0.0 45 162.5 0.0 14.4 0.0 0.0 120 FTG 2ET PE -1.3 46 165 .6 5.6 13.0 20.2 0.000 TL 14.60 PV 0.0 Pipe: 45 -20.2 1.049 PL 0.50 PF 0.7 46 165.6 5.6 13.0 20.2 7.5 120 FTG T PE 0.0 47 165.6 0.0 13.8 0.0 0.133 TL 5.50 PV 0.4 .Pipe: 46 .-85. 2 1. 380 PL 10. 00 .. PF . 5 ... o 47 165.6 0.0 13.8 0.0 18.3 120 FTG PE 0.0 48 165.6 0.0 18.8 0.0 0.499 TL 10.00 PV '. 2.2 Pipe: 47 -85.2 1.380 PL 15.20 PF 10.6 48 165 .6 0.0 18.8 0.0 18.3 120 FTG T PE 0.0 49 165.6 0.0 29.3 0.0 0.499 TL 21.20 PV 2.2 Pipe: 48 -255.8 4.260 PL 50.00 PF 1. 0 49 165.6 0.0 29.3 0.0 5.8 120 FTG T PE 0.0 50 165.6 0.0 30.4 0.0 0.016 TL 66.00 PV 0.2 Pipe: 49 -255.8 4.260 PL 72.00 PF 1.2 50 165.6 0.0 30.4 0.0 5.8 120 FTG E PE 0.0 51 165.6 0.0 31. 6 0.0 0.016 TL 79.00 PV 0.2 Pipe: 50 -255.8 4.260 PL 6.50 PF 0.4 51 165.6 0.0 31. 6 0.0 5.8 120 FTG T PE 0.0 52 165.6 0.0 32.0 0.0 0.016 TL 22.50 PV 0.2 Pipe: 51 -255.8 ' 4.260 PL 44.20 PF 0.9 52 165.6 0.0 32.0 0.0 5.8 120 FTG T PE 0.0 53 165.6 0.0 32.9 0.0 0.016 TL 60.20 PV 0.2 •-' ... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA~l\LEGO203U.SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS PIPE DATA (cont .) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES ( FT) (K) (PSI) (GPM) F .L. /FT (PSI) Pipe: 52 -255.8 4.260 PL 9.50 PF 0.3 53 165.6 0.0 32.9 0.0 5.8 120 FTG E PE 0.0 54 165.6 0.0 33.2 0.0 0.016 TL 16.50 PV 0.2 Pipe: 53 -255.8 4 .260 PL 12.50 PF 0.3 54 165.6 0.0 33.2 0.0 5 .8 120 FTG E PE 0.0 TORA 165.6 0.0 33.5 0.0 0.016 TL 19.50 PV 0.2 Pipe: 54 -255.8 4.260 PL 11.70 PF 0.2 TORA 165.6 0.0 33.5 0.0 5.8 120 FTG PE 5.0 BORA 154.0 0.0 38.7 0.0 0.0 16 TL 11.70 PV 0.2 Pipe: 55 -255.8 4.280 PL 15.00 PF 0.4 BORA 154.0 0.0 38.7 0.0 5.7 140 FTG 2E PE 1. 7 UGA 150.0 0.0 40.9 0.0 0.012 TL 37.00 PV 0.2 Pipe: 56 -255.8 4.070 PL 185.00 PF 2 .8 UGA 150.0 0.0 40.9 0.0 6.3 150 FTG TG PE -0.4 AUG4 151. 0 0.0 43.3 0.0 0.013 TL 218.00 PV 0 .3 Pipe: 57 -255.8 7.680 PL 28.00 PF 0.0 AUG4 151.0 0.0 43.3 0.0 1 .8 150 FTG E PE 0.0 AUG3 151.0 0.0 43.3 0.0 0.001 TL 52.00 PV 0.0 Pipe: 58 -255.8 8.510 PL 6.00 PF 0.0 AUG3 151.0 0.0 43.3 0.0 1.4 140 FTG T PE -2.6 BFP2 157.0 0.0 40.7 0.0 0.000 TL 53.00 PV 0.0 Pipe: 59 FIXED PRESSURE LOSS DEVICE BFPl 157.0 0.0 52.7 0.0 12.0 psi, 255.8 gpm BFP2 157.0 0.0 40.7 0.0 Pipe: 60 -255.8 8.510 PL 6 .00 PF 0.0 BFPl 157.0 0.0 52.7 0.0 1.4 140 FTG 2E PE 2 .6 AUG2 151.0 H.S. 55.4 100.0 0.000 TL 48.00 PV 0.0 Pipe: 61 -355.8 7.680 PL 18.00 PF 0.1 AUG2 151. 0 H.S. 55.4 100.0 2.5 150 FTG T PE 0.0 AUGl 151.0 0.0 55.4 0.0 0.001 TL 71.00 PV 0.0 Pipe: 62 -355.8 7.680 PL 115.00 PF 0.2 AUGl 151.0 0.0 55.4 0.0 2 .5 150 FTG TG PE 0.4 LEGO12 150.0 0.0 56.1 0 .0 0.001 TL 174.00 PV 0.0 Pipe: 63 -355.8 7.680 PL 38.00 PF 0.1 LEGO12 150.0 0.0 56.1 0.0 2.5 150 FTG E PE 0.0 LEGOll 150.0 0.0 56.1 0.0 0.001 TL 62.00 PV 0.0 Pipe: 64 -355.8 7.680 PL 145.00 PF 0.2 LEGOll 150.0 0.0 56.1 0.0 2.5 150 FTG TG PE 0.0 LEGOl0 150.0 0.0 56.3 0.0 0.001 TI,, 204.00 PV 0.0 - ,; SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEG0203U .SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 65 -355.8 7.680 PL 410.00 PF 0 .4 LEGOlO 150.0 0.0 56.3 0.0 2.5 150 FTG PE 0.0 LEG09 150.0 0.0 56.8 0.0 0.001 TL 410.00 PV 0.0 Pipe: 66 -355.8 7.680 PL 327.00 PF 0.4 LEG09 150.0 0.0 56.8 0.0 2.5 150 FTG PE 0.0 LEG08 150.0 0.0 57.2 0.0 0.001 TL 327.00 PV 0.0 Pipe: 67 -355.8 7.680 PL 390.00 PF 0.5 LEG08 150.0 0.0 57.2 0.0 2.5 150 FTG E PE 0.0 LEG07 150.0 0.0 57.6 0.0 0.001 TL 414.00 PV 0.0 Pipe: 68 -355.8 7.680 PL 212.00 PF 0 .3 LEGO? 150.0 0.0 57.6 0 .0 2.5 150 FTG TG PE 0.0 LEG06 150.0 0.0 57.9 0.0 0.001 TL 271.00 PV 0.0 Pipe: 69 -355.8 7.680 PL 400.00 PF 0.5 LEG06 150.0 0.0 57.9 0.0 2.5 150 FTG E PE 0 .0 LEGOS 150.0 0.0 58.4 0.0 0 .001 TL 424.00 PV 0.0 Pipe: 70 -355.8 8.510 PL 6.00 PF 0.0 LEG05 150.0 0.0 58.4 0.0 2.0 140 FTG E PE 0.0 LBFP2 150.0 0.0 58.4 0.0 0.001 TL 27.00 PV 0.0 Pipe: 71 FIXED PRESSURE LOSS DEVICE LBFPl 150.0 0.0 69.4 0.0 11.0 psi, 355.8 gpm LBFP2 150.0 0.0 58.4 0.0 Pipe: 72 -355.8 8.510 PL 6.00 PF o.o . LBFPl 150.0 0.0 69.4 0.0 2.0 140 FTG 2E PE 0.0 LEG04 150.0 0.0 69.4 0.0 0.001 TL 48.00 PV • 0.0 Pipe: 73 -355.9 8.510 PL 10.00 PF 0 .0 LEG04 150.0 0.0 69.4 0.0 2.0 140 FTG PE 0.0 METER2 150.0 0.0 69.4 0.0 0.001 TL 10.00 PV 0.0 Pipe: 74 FIXED PRESSURE LOSS DEVICE METER l 150.0 0.0 74.4 0.0 5.0 psi, 355.8 gpm METER2 150.0 0.0 69.4 0.0 Pipe: 75 -355.8 8.510 PL 110.00 PF 0.1 METERl 150.0 0.0 74.4 0.0 2.0 140 FTG TG PE 6.9 LEG03 134.0 0.0 81.5 0.0 0.001 TL 163.00 PV 0.0 Pipe: 76 -355.8 11.650 PL 485.00 PF 0 .1 LEG03 134.0 0.0 81. 5 0.0 1.1 150 FTG T2G PE 0.4 LEG02 133.0 0.0 82.0 0.0 0.000 TL 594.00 PV 0.0 Pipe: 77 -355.8 11.650 PL 150.00 PF 0.0 LEGQ.2 133.0 0.0 82.0 0.0 1.1 150 FTG TG PE 0.0 LEGO 1-33. 0 SRCE 82.0 (N/A) 0.000 TL 250.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEG0203U.SDF JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS NOTES: (1) Calculations were performed by the HASS 6.2.0 computer program under license no. 422Cl327E granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E . Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.058 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 18.3 ft/sec at pipe 29A. ( 4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40/TG HWC: 120 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G A Ell Tee 45'Ell ChkVlv BfyVlv GatVlv AlmChk 1.049 2.00 5.00 1.00 5.00 6.00 1.00 0.10 1.380 3.00 6.00 1.00 7.00 G.00 1.00 0.10 PAG E : B MATERIAL: TWL/GG HWC: 120 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G A Ell Tee 45'Ell ChkVlv BfyVlv GatVlv AlmChk 4.260 7.00 16.00 3.50 22.00 12.00 2.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G D Ell Tee 45'Ell ChkVlv BfyVlv GatVlv DetChk 4.280 11.00 27.00 8.00 30.00 16.00 3.00 39.00 8.510 21. 00 47.00 17.00 60.00 16.00 6.00 78.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G D Ell Tee LngEll ChkVlv BfyVlv GatVlv DetChk 11.650 33.00 91.00 27.00 98.00 32.00 9.00 105.00 PAGE: K MATERIAL: PVC200 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G D Ell Tee LngEll ChkVlv BfvVlf GatVlv DetChk 4.070 .12. 0.0 30.00 9.00 33.00 18.00 3.00 39.00 7.680 ,24 .00 53.00 2 0 . 0 0 -. 6 g . 0 0 1a·. oo 6.00 78.00 D DPVlv 0.10 0.10 D DPVlv 12.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203U JOB TITLE: ADMINISTRATION BUILDING UPRIGHTS WATER SUPPLY CURVE WA TER S UPPLY ANALYSIS Static: 109.00 p s i Res1d: 84.00 psi Flow: 3545.0 gpm 120.0 1-~---------------------~ LEGEND 100.0 -101• '7£?· I "' ,.. V\ a. ',J w a ::) 80.0 ~ 60.0 w a 0 . w l!) <C l!) 40.0 20.0 0.0 -&}. ,Cf'J?.,I ~ .,,..,., ' e,C!(t 1 -14.7 L...~_.__..,_ _ _._ __ .r..... __ ...__ __ ...... ___ .r..... ___ .... 800 2001600 2000 2400 2800 3200 3600 4000 FLOW (GP M) Available pressure 108. 64 psi e 355. 8 gpm Required pressure 82. 03 psi e 355. 8 gpm SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 Date: 12/04/1997 C:\HASS62\FILES\LEGOLA-1\LEGO203U.SDF JOB TITLE: ADMINISTRATION BUILD ING UPRIGHTS WATER SUPPLY CURVE 120+ 110*\\\\\ 0 \\\\\ \\\\\ \\\\\ 100+ \\\\\ \\\\\\ \\\\\ \\\\\ 90+ \\\\\ X P 80+ \\\\\ 84.0 psi@ 3545 gpm-> * Flow Test Point R E s s u R E 70+ 60+ ( p s I 50+ ) 40+ 30+ 20+ 10+ ====================:===~===== LEGEND X = Required Water Supply 82.03 psi@ 355.8 gpm 0 = Available Water Supply 108.64 psi@ 355.8 gpm " 11 O++-+---+----+-----+------+--------+--------+---------+-----------+ 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM)