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HomeMy WebLinkAbout1 LEGO DR; ; AS980126; Permit3/7/24, 4:45 PM AS980126 Permit Data City of Carlsbad AUTOMATIC SPRINKLER-COMM Permit No: AS980126 Status: ISSUED Applied 7/22/1998 Approved: 7/22/1998 Issued: 7/22/1998 Job Address: I LEGO DR Permit Type: ASC Parcel No: Lot #: 0 Reference No.: PC #: Inspector: Project Title: LEGO PARK THE BEGINNING SPRINKLERS, WEST COMPLEX 2 AREAS Applicant: Owner: COSCO FIRE PROTECTION 321 EAST GARDENABL GARDENA CA 213321 5155 Fees ($) Add'I Fees ($) Total ($) Balance ($) 300 0 300 0 about:blank 1/1 FIRE D E P A R ME N T PERMIT Permit No: A5980126 07/22/98 09:50 Project No: A9800219 Page 1 of I Bldg Permit#: CB981168 Job Address: 1 LEGO DR Suite: Permit Type: AUTOMATIC SPRINKLER-COMMERCIAL Parcel No: Construction Type: VN Occupancy Group: Description: LEGO PARK "THE BEGINNING" SPRINKLERS, WEST COMPLEX 2 AREAS Resp Party: COSCO FIRE PROTECTION 321 EAST GARDENA BL GARDENA CA 90247 ----. Status: ISSUED Applied: 07/22/98 Apr/Issue: 07/22/98 Entered By: CB 213 321 5155 Fire Dept. Ref eren'oce,t 9742B3/\,.. Fees Required1., /*** oil --------------••J7i____ Fees: /300. .' Adjustments: /4 \\ .00 TaiC±ed Total Fees: , 30.0.0O •b/'• Tótal Paymé / Balance-, Fee description ----------------- Enter # of Re-In•speti *TOTAL ted & Credits 300.00 300.00 .00 'M - 0-01 FIRE PREVENTION BUREAU 2560 ORION WAY, CARLSBAD, CA 92008-7280 (619) 931-2121 - COSCO FIRE PROTECTION, INC. !JUN 5 1998 -- 321 EAST GARDENA BOULEVARD BERNARDS BROS. INC. GARDENA, CA 90247 / HYDRAULIC CALCULATIONS FOR LEGOLAND/BEGINNING/WEST COMPLEX ONE LEGO DRIVE CARLSBAD, CA FILE NUMBER: LAC6163-A DATE: 26 MAY 98 -DESIGN DATA- OCCUPANCY CLASSIFICATION: . ORDINARY HAZARD GROUP II DENSITY: . .20 GPM/SQ. FT. AREA OF APPLICATION: 1500 SQ. FT. COVERAGE PER SPRINKLER: 100 SQ. FT. (130 SQ FT MAX) NUMBER OF SPRINKLERS CALCULATED: 19 FLOW AND PRESSURE (@ BOR): 507.7 gpm @ 63.0 psi FLOW AND PRESSURE (@ SOURCE) 657.7 gpm @ 90.5 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR- COSCO FIRE PROTECTION, INC. DESIGN/LAYOUT BY: S. HANSEN AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD AND SCHIRMER ENGINEERG CONTRACTOR CERTIFICATION NUMBER: C-16 577621 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE 44 4 C1288D ) A HRS SYSTEMS, INC. ATLANTA, GA SPRINKLER SYSTEM HYDRAULIC ANALYSIS .Date: 05/27/.998 JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL NODE PRESS. PRESS. © PRESS.. @ DEMAND TAG (PSI) (PSI) (GPM) (PSI) (GPM) SRC 98.1 75.6 3545.0 97.. 655.0 Page 1 LAC6163A .SDF REQ 'D PRESS. (PsI) 81.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 655.0 GPM 150.0 GPM 100.0 GPM 405.0 GPM NODE ANALYSIS DATA NODE TAG 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 50 51 52 53 54 55 56 ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 166.7 K: 5.60 13.2 20.3 166.7 K: 5.60 13.2 20.3 166.7 - - - - 13.3 166.7 - - - - 13.4 166.7 K: 5.60 13.5 20.5 166.7 K: 5.60 14.1 21.0 166.7 K: 5.60 15.4 22.0 166.7 ---•- 20.0 166.7 ---- 13.5 166.7 K: 5.60 13.5 20.6 166.7 K: 5.60 12.8 20.0 166.7 14.7 166.7 K: 5.60 14.8 21.5 166.7 K: 5.60 15.8 22.3 166.7 K: 5.60 17.8 23.6 166.7 14.8 166.7 K: 5.60 14.8 21.6 166.7 15.5 166.7 --•-- 15.7 166.7 K: 5.60 15.8 22.2 166.7 K= 5.60 16.9 23.1 166.7 .K: 5.60 13.0 20.2 166.7 K: 5.60 13.0 20.2 166.7 K= 5.60 13.2 20.3 166.7 K: 5.60 13.7 20.7 166.7 K: 5.60 14.7 21.5 166.7 K: 5.60 16.7 22.9 161.5 - - - - 45.5 161.5 45.5 161.5 - - - - 45.5 - - - 161.5 --- 45.5 161.5 - - - - 45.5 161.5 . - - - - 45.5 - - - 161.5 - - - - 45.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 05/27/1998 LAC6163A .SDF .303 TITLE: LEGOLAND/BEGINNING/WEST COMPLEX NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 57 161.5 - - - - 45.5 - - - 58 161.5 - - - - 45.5 - - - 59 161.5 - - - - 45.5 - - - 60 161.5 ---- 45.5 --loo 165.7 - - - - 14.0 - - - 101 166.7 - - - - 14.0 102 165.7 - - - - 13.9 - - - 103 166.7 - - - - 13.3 - - - 104 165.7 - - - - 13.9 - - - 105 166.7 - - - - 13.5 - - - 106 165.7 - - - - 13.9 - - - 107 166.7 - -. - - 13.3 108 165.7 - - - - 28.8 - - - 109 166.7 - - - - 24.4 110 165.7 - - - - 29.1 - - - 111 166.7 - - - - 31.7 - - - 112 165.7 ---- 29.1 113 166.7 - - - - 28.7 - - - 114 165.7 - - - - 29.2 - - - 115 166.7 ---- 31.5 116 165.7 - - - - 29.1 117 166.7 . - - - - . 26.7 118 165.7 - - - - 29.2 119 166.7 - - - - 31.4 - - - 120 165.7 29.2 121 166.5 - - - - 25.8 - - - 122 165.7 - - - - 29.2 - - - 123 166.7 - - - - 30.9 124 161.5 - - - - 45.5 - - - 125 161.5 - - - - 45.5 126 161.5 - - - 45.5 - - - 127 161.5 - - - - 45.5 - - - 128 161.5 - - - - 45.5 - - - 129 161.5 - - - - 45.5 - - 130 161.5 - - - - 45.5 - - 131 161.5 - - - - 45.5 - - - 132 161.5 - - - - 45.5 - - - 133 165.7 - - - - 43.7 - - - 134 165.7 - - - - 43.7 - - - 135 165.7 - - - - 43.7 136 165.7 - - - - 42.2 - - - 137 165.7 - - - - 43.9 138 165.7 -- - 42.1 - - - 139 165.7 - - - - 44.6 140 165.7 - - - - 42.7 141 165.7 - - - - 45.3 142 165.7 - - - - 42.9 - - - 143 165.7 - - - - 46.3 144 165.7 - - -. - 44.2 - - - TOR 164.2 - - - - 49.0 BOR 153.5 HOSE STREAM 54.1 100.0 BF1 150.0 - - - - 59.1 6F2 156.0. - - - - 57.5 BE3 156.0 - - - - 72.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 05/27/1998 LAC6163A.SDF 30B TITLE: LEGOLAND/BEGINNING/LJEST COMPLEX NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) BF4 150.0 - - - - 76.1 - - - SRC 150.0 SOURCE 81.5 505.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 05/27/1998 LAC6163A..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX 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 -0.3 1.610 PL 6.13 PF 0.0 - 1 166.7 5.6 13.2 20.3 0.0 120 FTG ---- PE 0.0 2 166.7 5.6 13.2 20.3 0.000 TL 6.13 PV 0.0 Pipe: 2 -20.6 1.610 PL 6.67 PF 0.2 2 166.7 5.6 13.2 20.3 3.2 120 FIG E PE 0.0 3 166.7 0.0 13.3 0.0 0.017 TL 10.67 PV 0.1 Pipe: 3 -20.6 1.610 PL 2.00 PF 0.1 3 166.7 0.0 13.3 0.0 3.2 120 FIG E PE 0.0 4 166.7 0.0 13.4 0.0 0.017 IL 6.00 PV 0.1 Pipe: 4 -20.6 1.610 PL 1.46 PF 0.0 4 166.7 0.0 13.4 0.0 3.2 120 FIG ---- PE 0.0 5 166.7 5.6 13.5 20.5 0.017 TL 1.46 PV 0.1 Pipe: 5 -41.1 1.610 PL 10.00 PF 0.6 5 166.7 5.6 13.5 20.5 6.5 120 FTG ---- PE 0.0 6 166.7 5.6 14.1 21.0 0.061 IL 10.00 PV 0.3 Pipe: 6 -62.1 1.610 PL 10.00 PF 1.3 6 166.7 5.6 14.1 0 21.0 9.8 120 FIG ---- PE 0.0 7 166.7 5.6 15.4 22.0 0.132 TL 10.00 PV 0.6 Pipe: 7 -84.1 1.610 PL 19.96 PF 4.6 7 166.7 5.6 15.4 22.0 13.3 120 FIG ---- PE 0.0 8 166.7 0.0 20.0 0.0 0.230 IL 19.96 PV 1.2 Pipe: 8 -119.2 1.610 PL 6.08 PF 4.4 8 166.7 0.0 20.0. 0.0 18.8 120 FTG E PE 0.0 109 166.7 0.0 24.4 0.0 0.439 TL 10.08 PV 2.4 Pipe: 9 -119.2 1.610 PL 1.00 PF 4.0 109 166.7 0.0 24.4 0.0 18.8 120 FTG T PE 0.4 108 165.7 0.0 28.8 0.0 0.439 IL 9.00 PV 2.4 Pipe: 10 -7.2 1.610 PL 6.13 PF 0.0 9 166.7 0.0 13.5 0.0 1.1 120 FIG ---- PE 0.0 10 166.7 5.6 13.5 20.6 0.002 IL 6.13 PV 0.0 Pipe: 11 -20.0 1.049 PL 1.00 PF 0.8 11 166.7 5.6 12.8 20.0 7.4 120 FIG I PE 0.0 10 166.7 5.6 13.5 20.6 0.130 IL 6.00 PV 0.4 Pipe: 12 -47.8 1.610 PL 6.67 PF 1.2 10 166.7 5.6 13.5 20.6 7.5 120 FIG I PE 0.0 - 12 166.7 0.0 14.7 0.0 0.081 TL 14.67 PV 0.4 Pipe: 13 -33.1 1.610 PL 1.46 PF 0.1 12 166.7 0.0 14.7 0.0 5.2 120 FTG ---- PE 0.0 13 166.7 5.6 14.8 21.5 0.041 TL 1.46 PV 0.2. SPRINKLER SYSTEM HYDRAULIC ANALYSIS. Page 5 Date; 05/27/1998 LAC6163A.SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.. NODES (Fl) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 -54.6 1.610 PL 10.00 PF 1.0 13 166.7 5.6 14.8 21.5 . 8.6 120 FTG ---- PE 0.0 14 166.7 5.6 15.8 22.3 0.104 TL 10.00 PV 0.5 Pipe: 15 -76.9 1.610 PL 10.00 PF 2.0 14 166.7 5.6 15.8 22.3 12.1 120 FTG ---- PE 0.0 15 166.7 5.6 17.8 23.6 0.195 TL 10.00 PV 1.0 Pipe: 16 -100.5 1.610 PL 26.04 PF 10.9 15 166.7 5.6 17.8 23.6 15.8 120 FTG T PE 0.0 113 166.7 0.0 28.7 0.0 0.320 IL 34.04 PV 1.7 Pipe: 17 -8.9 1 .610 PL 1.00 PF 0.0 113 166.7 0.0 28.7 0.0 1.4 120 FIG T PE 0.4 112 165.7 0.0 29.1 0.0 0.004 TL 9.00 PV 0.0 Pipe: 18 -14.7 1.610 PL 8.00 PF 0.1 12 166.7 0.0 14.7 0.0 2.3 120 FIG E PE 0.0 16 166.7 0.0 14.8 0.0 0.009 IL 12.00 PV 0.0 Pipe: 19 -14.7 1.610 PL 1.46 PF 0.0 16 166.7 0.0 14.8 0.0 2.3 120 FIG ---- PE 0.0 17 166.7 5.6 14.8 21.6 0.009 TL 1.46 PV 0.0 Pipe: 20 -36.3 1.610 PL 9.00 PF 0.6 17 166.7 5.6 14.8 21.6 5.7 120 FTG E PE 0.0 18 166.7 0.0 15.5 0.0 0.049 TL 13.00 PV 0.2 Pipe: 21 -36.3 1.610 PL 1.00 PF 0.2 18 166.7 0.0 15.5 0.0 5.7 120 FTG E PE 0.0 19 166.7 0.0 15.7 0.0 0.049 TL 5.00 PV 0.2 Pipe: 22 -36.3 1.610 PL 1.00 PF 0.0 19 166.7 0.0 15.7 0.0 5.7 120 FTG ----- PE 0.0 20 166.7 5.6 15.8 22.2 0.049 IL 1.00 PV 0.2 Pipe: 23 -58.5 1.610 PL 10.00 PF 1.2 20 166.7 5.6 15.8 22.2 9.2 120 FIG ---- PE 0.0 21 166.7 5.6 16.9 23.1 0.118 TL 10.00 PV 0.6 Pipe: 24 -81.6 1.610 PL 29.04 PF 9.8 21 166.7 5.6 16.9 23.1 12.9 120 FTG 2ET PE 0.0 117 166.7 0.0 26.7 0.0 0.218 IL 45.04 PV 1.1 Pipe: 25 -81.6 1.610 PL 1.00 PF 2.0 117 166.7 0.0 26.7 0.0 12.9. 120 FIG I PE 0.4 1.16 165.7 0.0 29.1 0.0 0.218 TL 9.00 PV 1.1 Pipe: 26 2.1 1.610 PL 6.00 PF 0.0 22 166.7 5.6 13.0 20.2 0.3 120 FTG ---- PE 0.0 23 166.7 5.6 13.0 20.2 0.000 IL 6.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 05/27/1998 LAC6163A..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 -18.2 1.610 PL 10.00. PF 0.1 23 166.7 5.6 13.0 20.2 2.9 120 FTG ---- PE 0.0 24 166.7 5.6 13.2 20.3 0.014 IL 10.00 PV 0.1 Pipe: 28 -38.5 1.610 PL 10.00 PF 0.5 24 166.7 5.6 13.2 20.3 6.1 120 FTG ---- PE 0.0 25 166.7 5.6 13.7 20.7 0.054 TL 10.00 PV 0.2 Pipe: 29 -59.2 1.610 PL 8.00 PF 1.0 25 166.7 5.6 13.7 20.7 9.3 120 FTG ---- PE 0.0 26 166.7 5.6 14.7 21.5 0.120 IL 8.00 PV 0.6 Pipe: 30 -80.7 1.610 PL 9.50 PF 2.0 26 166.7 5.6 14.7 21.5 12.7 120 FIG ---- PE . 0.0 27 166.7 5.6 16.7 22.9 0.213 TL 9.50 PV 1.1 Pipe: 31 -103.6 1.610 PL 18.50 PF 9.0 27 166.7 5.6 16.7 22.9 16.3 120 FTG T PE 0.1 121 166.5 0.0. 25.8 0.0 0.339 IL 26.50 PV 1.8 Pipe: 32 . -103.6 1.610 PL 1.00 PF 3.0 121 166.5 0.0 25.8 , 0.0 16.3 120 FIG T PE 0.3 120 165.7 0.0 29.2 0.0 0.339 TL 9.00 PV 1.8 Pipe: 33 . -35.1 1.610 PL 82.71 PF 6.0 101 166.7 0.0 14.0 0.0 5.5 120 FTG 8E21 PE 0.0 8 166.7 0.0 20.0 0.0 0.046 IL 130.71 PV 0.2 Pipe: 34 35.1 1.610 PL 1.00 PF 0.4 101 166.7 0.0 14.0 0.0 5.5 120 FIG I PE 0.4 100 165.7 0.0 14.0 0.0 0.046 IL 9.00 PV 0.2 Pipe: 35 -20.0 1.610 PL 1.00 PE 0.1 103 166.7 0.0 13.3 0.0 3.2 120 FIG I PE 0.4 102 165.7 0.0 13.9 0.0 0.016 IL 9.00 PV 0.1 Pipe: 36 7.2 1.610 PL 1.00 PF 0.0 105 166.7 0.0. 13.5 0.0 1.1 120 FIG I PE 0.4 104 165.7 0.0 13.9 0.0 0.002 TL 9.00 PV 0.0 Pip: 37 -22.3 1.610 PL 1.00 PF 0.2 107 166.7 0.0 13.3 0.0 3.5 120 FTG T PE 0.4 106 165.7 0.0 13.9 0.0 0.020 IL 9.00 PV 0.1 Pipe: 38 85.0 1.610 PL 1.00 PF 3.1 111 166.7 0.0 31.7 0.0 13.4 120 FIG El PE 0.4 110 165.7 0.0 29.1 0.0 0.235 IL 13.00 PV 1.2 Pipe: 39 . 80.2 1.610 PL 1.00 PF 2.7 115 166.7 0.0 31.5 0.0 12.6 120 FIG El PE 0.4 114 165.7 .0.0 29.2 0.0 0.211 IL 13.00 PV 1.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 05/27/1998 LAC6163A..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 40 78.1 1.610 PL 1.00 PF 2.6 119 166.7 0.0 31.4 0.0 12.3 120 FTG ET PE 0.4 118 165.7 0.0 29.2 0.0 0.201 IL 13.00 PV 1.0 Pipe: 41 70.0 1.610 PL 1.00 PF 2.1 123 166.7 0.0 30.9 0.0 11.0 120 FTG El PE 0.4 122 165.7 0.0 29.2 0.0 0.164 TL 13.00 PV 0.8 Pipe: 42 0.0 1.049 PL 13.63 PF 0.0 50 161.5 0.0 45.5 0.0 0.0 120 FTG 2ET PE 0.0 124 161.5 0.0 45.5 0.0 0.000 IL 22.63 PV 0.0 Pipe: 43 0.0 1.049 PL 4.63 PF 0.0 51 161.5 0.0 45.5 0.0 0.0 120 FIG T PE 0.0 124 161.5 0.0 45.5 0.0 0.000 TL 9.63 PV 0.0 Pipe: 44 0.0 1.049 PL 6.88 PF 0.0 52 161.5 0.0 45.5 0.0 0.0 120 FTG T PE 0.0 125 161.5 0.0. 45.5 0.0 0.000 TL 11.88 PV 0.0 Pipe: 45 0.0 1.049 PL 4.63 PF 0.0 53 161.5 0.0 45.5 0.0 0.0 120 FIG I PE 0.0 125 161.5 0.0 45.5 0.0 0.000 TL 9.63 PV 0.0 Pipe: 46 0.0 1.049 PL 6.88 PF 0.0 54 161.5 0.0 45.5 0.0 0.0 120 FTG T PE 0.0 126 161.5 0.0 45.5 0.0 0.000 IL 11.88 PV 0.0 Pipe: 47 00 1 .049 PL 4.63 PF 0.0 55 161.5 0.0 45.5 0.0 0.0 120 FIG I PE 0.0 126 161.5 0.0 45.5 0.0 0.000 TL 9.63 PV 0.0 Pipe: 48 0.0 1.049 PL 6.88 PF 0.0 56 161.5 0.0 45.5 0.0 0.0 120 FTG T PE 0.0 127 161.5 0.0 45.5 0.0 0.000 IL 11.88 PV 0.0 Pipe: 49 0.0 1.049 PL 4.63 PF 0.0 57 161.5 0.0 45.5 0.0 0.0 120 FIG I PE 0.0 127 161.5 0.0 45.5 0.0 0.000 TL 9.63 PV 0.0 Pipe: 50 0.0 1.049 PL 6.88 PF 0.0 58 161.5 0.0 45.5 0.0 0.0 120 FTG T PE 0.0 128 161.5 0.0 45.5 0.0 0.000 IL 11.88 PV 0.0 Pipe: 51 0.0 1.049 PL 4.63 PF 0.0 59 161.5 0.0 45.5 0.0 0.0 120 FTG I PE 0.0 128 161.5 0.0 45.5 0.0 0.000 TL 9.63 PV 0.0 Pipe: 52 . 0.0 1.049 PL 6.88 PF 0.0 60 161.5 0.0 45.5 0.0 0.0 120 FTG I PE 0.0 129 161.5 0.0 45.5 0.0 0.000 IL 1188 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 Date: 05/27/1998 LAC6163A..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX 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: 53 0.0 1.610 PL 8.00 PF 0.0 124 161.5 0.0 45.5 0.0 0.0 120 FTG ---- PE 0.0 125 161.5 0.0 45.5 0.0 0.000 IL 8.00 PV 0.0 Pipe: 54 0.0 1.610 PL 14.75 PF 0.0 125 161.5 0.0 45.5 0.0 0.0 120 FTG ---- PE 0.0 126 161.5 0.0 45.5 0.0 0.000 TL 14.75 PV 0.0 Pipe: 55 0.0 1.610 PL 14.75 PF 0.0 126 161.5 0.0 45.5 0.0 0.0 120 FTG ---- PE 0.0 127 161.5 0.0 45.5 0.0 0.000 IL 14.75 PV 0.0 Pipe: 56 0.0 1.610 PL 14.75 PF 0.0 127 161.5 0.0 45.5 0.0 0.0 120 FTG ---- PE 0.0 128 161.5 0.0 45.5 0.0 0.000 TL 14.75 PV 0.0 Pipe: 57 0.0 1.610 PL 14.75 PF 0.0 128 161.5 0.0 45.5 0.0 0.0 120FTG ---- PE 0.0 129 161.5 0.0. 45.5 0.0 0.000 IL 14.75 PV 0.0 Pipe: 58 0.0 1.610 PL 14.75 PF 0.0 129 161.5 0.0 45.5 , 0.0 0.0 120 FIG ---- PE 0.0 130 161.5 0.0 45.5 0.0 0.000 TL 14.75 PV 0.0 Pipe: 59 0.0 1.610 PL 14.75 PF 0.0 130 161.5 0.0 45.5 0.0 0.0 120 FTG ---- PE 0.0 131 161.5 0.0 45.5 0.0 0.000 IL 14.75 PV 0.0 Pipe: 60 0.0. 1.610 PL 10.08 PF 0.0 131 161.5 0.0 45.5 0.0 0.0 120 FIG 7E PE 0.0 132 161.5 0.0 45.5 0.0 0.000 TL 38.08 PV 0.0 Pipe: 61 0.1 2.635 PL 4.00 PF 0.0 132 161.5 0.0 45.5 0.0 0.0 120 FTG E PE -1.8 133 165.7 0.0 43.7 0.0 0.000 TL 12.24 PV 0.0 Pipe: 62 0.0 2.635 PL 29.04 PF 0.0 133 165.7 0.0 43.7 0.0 0.0 120 FIG I PE 0.0 134 165.7 0.0 43.7 0.0 0.000 TL 45.51 PV 0.0 ipe: 63 0.0 2.635 PL 4.58 PF 0.0 134 165.7 0.0 43.7 0.0 0.0 120 FTG ---- PE 0.0 135 165.7 0.0 43.7 0.0 0.000 IL 4.58 PV 0.0 Pipe: 64 -70.0 2.635 PL 14.92 PF 0.2 135 165.7 0.0 43.7 0.0 4.1 120 FIG ---- PE 0.0 137 165.7 0.0 43.9 0.0 0.015 TL 14.92 PV 0.1 Pipe: 65 -148.1 2.635 PL 12.25 PF 0.7 137 165.7 0.0 43.9 0.0 8.7 120 FTG ---- PE 0.0 139 165.7 .0.0 44.6 0.0 0.060 IL 12.25 PV 0.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 Date: 05/27/1998 LAC6163A..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont..) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HL.J(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 66 -228.3 2.635 PL 5.33 PF 0.7 139 165.7 0.0 44.6 0.0 13.4 120 FTG ---- PE 0.0 141 165.7 0.0 45.3 0.0 0.133 TL 5.33 PV 1.2 Pipe: 67 -319.9 2.635 PL 4.00 PF 1.0 141 165.7 0.0 45.3 0.0 18.8 120 FIG ---- PE 0.0 143 165.7 0.0 46.3 0.0 0.248 TL 4.00 PV 2.4 Pipe: 68 -404.9 4.260 PL 15.50 PF 2.0 143 165.7 0.0 46.3 0.0 9.1 120 FIG 3E PE 0.6 TOR 164.2 0.0 49.0 0.01 0.037 IL 55.00 PV 0.6 Pipe: 69 35.1 2.635 PL 8.00 PF 0.1 100 165.7 0.0 14.0 0.0 2.1 120 FIG I PE 0.0 102 165.7 0.0 13.9 0.0 0.004 IL 24.47 PV 0.0 Pipe: 70 -22.3 2.635 PL 10.50 PF 0.0 106 165.7 0.0 13.9 0.0 1.3 120 FIG ---- PE 0.0 104 165.7 0.0 13.9 0.0 0.002 TL 10.50 PV 0.0 Pipe: 71 -15.1 2.635 PL 9.00 PF 0.0 104 165.7 0.0 13.9 0.0 0.9 120 FIG ---- PE 0.0 102 165.7 0.0 13.9 0.0 0.001 TL 9.00 PV 0.0 Pipe: 72 70.0 2.635 PL 4.00 PF 0.1 122 165.7 0.0 29.2 0.0 4.1 120 FTG ---- PE 0.0 120 165.7 0.0 29.2 0.0 0.015 IL 4.00 PV 0.1 Pipe: 73 -33.6 2.635 PL 4.50 PF 0.0 120 165.7 0.0 29.2 0.0 2.0 120 FIG ---- PE .0.0 118 165.7 0.0 29.2 0.0 0.004 TL 4.50 PV 0.0 Pipe: 74 44.5 2.635 PL 6.58 PF 0.0 118 165.7 0.0 29.2 0.0 2.6 120 FIG ---- PE 0.0 116 165.7 0.0 29.1 0.0 0.006 IL 6.58 PV 0.0 Pipe: 75 -37.1 2.635 PL 5.67 PF 0.0 116 165.7 0.0 29.1 0.0 2.2 120 FIG ---- PE 0.0 114 165.7 0.0 29.2 0.0 0.005 TL 5.67 PV 0.0 Pipe: 76 43.2 2.635 PL 5.33 PF 0.0 114 165.7 0.0 29.2 0.0 2.5 120 FIG ---- PE 0.0 112 165.7 0.0 29.1 0.0 0.006 IL 5.33 PV 0.0 Pipe: 77 34.2 2.635 PL 4.00 PF 0.0 112 165.7 0.0 29.1 0.0 2.0 120 FIG ---- PE 0.0 - 110 165.7 0.0 29.1 0.0 0.004 TL 4.00 PV 0.0 Pipe: 78 -119.2 2.635 PL 8.00 PF 0.3 108 165.7 0.0 28.8 0.0 7.0 120 FTG ---- PE 0.0 110 165.7 0.0 291 0.0 0.040 IL 8.00 PV 0.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 Date: 05/27/1998 LAC6163A..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont..) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 79 -70.0 1.610 PL 50.25 PF 10,9 123 166.7 0.0 30.9 0.0 11.0 120 FIG 2ET PE 0.4 136 165.7 0.0 42.2 0.0 0.164 IL 66.25 PV 0.8 Pipe: 80 -70.0 1.610 PL 1.00 PF 1.5 136 165.7 0.0 42.2 0.0 11.0 120 FIG T PE 0.0 135 165.7 0.0 43.7 0.0 0.164 IL 9.00 PV 0.8 Pipe: 81 -78.1 1.610 PL 43.25 PF 10.3 119 166.7 0.0 31.4 0.0 12.3 120 FTG T PE 0.4 138 165.7 0.0 42.1 0.0 0.201 IL 51.25 PV 1.0 Pipe: 82 -78.1 1.610 PL 1.00 PF 1.8 138 165.7 0.0 42.1 0.0 12.3 120 FIG T PE 0.0 137 165.7 0.0 43.9 .0.0 0.201 TL 9.00 PV 1.0 Pipe: 83 -80.2 1.610 PL 43.25 PF 10.8 115 166.7 0.0 31.5 0.0 12.6 120 FIG I PE 0.4 140 165.7 0.0. 42.7 0.0 0.211 IL 51.25 PV 1.1 Pipe: 84 -80.2 1.610 PL 1.00 PF 1.9 140 165.7 0.0 42.7 , 0.0 12.6 120 FIG T PE 0.0 139 165.7 0.0 44.6 0.0 0.211 TL 9.00 PV 1.1 Pipe: 85 -91.6 1.610 PL 43.25 PF 13.8 113 166.7 0.0 28.7 0.0 14.4 120 FTG T PE 0.4 142 165.7 0.0 42.9 0.0 0.269 IL 51.25 PV 1.4 Pipe: 86 -91.6 1.610 PL 1.00 PF 2.4 142 165.7 0.0 42.9 0.0 14.4 120 FIG I PE 0.0 141 165.7 0.0 45.3 0.0 0.269 TL 9.00 PV 1.4 Pipe: 87 -85.0 1.610 PL 43.25 PE 12.0 111 166.7 0.0 31.7 0.0 13.4 120 FIG I PE 0.4 144 165.7 0.0 44.2 0.0 0.235 TL 51.25 PV 1.2 Pipe: 88 -85.0 1.610 PL 1.00 PF 2.1 144 165.7 0.0 44.2 0.0 13.4 120 FIG I PE 0.0 143 165.7 0.0 46.3 0.0 0.235 TL 9.00 PV 1.2 Pipe: 89 -22.3 1.610 PL 3.50 PF 0.2 22 166.7 5.6 13.0 20.2 3.5 120 FTG I PE 0.0 107 166.7 0.0 13.3 0.0 0.020 TL 11.50 PV 0.1 Pipe: 90 7.2 1.610 PL 3.21 PF 0.0 9 166.7 0.0 13.5 0.0 1.1 120 FIG T PE 0.0 - 105 166.7 0.0 13.5 0.0 0.002 TL 11.21 PV 0.0 Pipe: 91 -20.0 1.610 PL 321 PF 0.2 1 166.7 5.6 13.2 20.3 3.2 120 FTG T PE 0.0 103 166.7 0.0 13.3 0.0 0.016 IL 11.21 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 Date: 05/27/1998 LAC6163A..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont..) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 92 -404.9 4.260 PL 13.71 PF 0.5 TOR 164.2 0.0 49.0 0.0 9.1 120 FTG ---- PE 4.6 BOR 153.5 H.S. 54.1 100.0 0.037 IL 13.71 PV 0.6 Pipe: 93 -504.9 4.095 PL 50.00 PF 3.4 BOR 153.5 H.S. 54.1 100.0 12.3 140 FTG EG -PE 1.5 BF1 150.0 0.0 59.1 0.0 0.051 TL 67.34 PV 1.0 Pipe: 94 . -504.9 4.095 PL 6.00 PF 1.0 BF1 150.0 0.0 59.1 0.0 12.3 140 FTG E PE -2.6 BF2 156.0 0.0 57.5 0.0 0.051 IL 20.45 PV 1.0 Pipe: 95 FIXED PRESSURE LOSS DEVICE BF3 156.0 0.0 72.5 0.0 15.0 psi, 504.9 gpm BF2 156.0 0.0 57.5 0.0 Pipe: 96 -504.9 4.095 PL 6.00 PF 1.0 8F3 156.0 0.0 72.5 0.0 12.3 140 FTG E PE 2.6 BF4 150.0 0.0. 76.1 0.0 0.051 IL 20.45 PV 1.0 Pipe: 97 -505.0 4.095 PL 60.00 PF 5.4 BF4 150.0 0.0 76.1 , 0.0 12.3 140 FIG ETG PE 0.0 SRC 150.0 SRCE 81.5 (N/A) 0.051 TL 106.23 PV 1.0 NOTES: Calculations were per-Formed by the HASS 6.2.0 computer program under license no. 4 C1288D granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 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 0.197 gpm. Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 18.8 ft/sec at pipe 67. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 Date: 05/27/1998 LAC6163A.SDF JOB TITLE: LEGOLAND/BEGINNING/WEsT COMPLEX (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HL4C: 120 Diameter Equivalent Fitting Lengths i.n Feet (in) E T L C B G A D Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv N NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 1.610 4.00 8.00 2.00 9.00 600 1.00 10.00 10.00 8.00 PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee LngE1l ChkVlv BfyVlv GatVlv AlriiOhk DPViv 2.635 8.24 16.47 5.49 19.22 961 1.37 13.73 13.73 4.095 10.86. 21.73 6.52 23.90 13..04 2.17 21.73 10.86 4.260 13.17 26.33 7.90 28.97 15.80 2..63 26.33 13.17 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 Date: 05/27/1998 LAC6163A..SDF JOB TITLE: LEGOLAND/BEGINNING/L.JEST COMPLEX WATER SUPPLY CURVE 108+ :o \\\\\ \\\\\ 90+ \\\\\ \\\\\ 81+ X 75.6 psi @ 3545 gprn-> * Flow Test Point P 72+ R E S 963+ U R E 54+ ( I P S I 45+ ) 36+ 27+ 18+ LEGEND 0 I II X = Required Water Supply 81.51 Psi @ 655.0 gpm 9+ 1 0 = Available Water Supply 97.11 psi @ 655.0 gpm I II +--------+-------------------+-----------+ 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) U Check Any. Pipe Line Relief Valve Seat Center Reiisl Valve Piston Relief Valve Piston Any. Wiper Seal Relict Valve Bottom Plug " Body Flange iftF" Spring Auy. HOW IT OPUtATEC The unique relief valve COnstrUCtIon incorporates two channel.: one for Sir. one for water. When t1ke relief vale opens. as in the eccampenying air-in/water-out diagram. the right-hand channel admits air to via top of the reduced pressure zone, re- Coving the zone vacuum. The chan- nel on the left then drains the zone to atmosphere. Therefore, if both check valves foul. 1216 simuilaneOns negative supply and positive back pressure dsv,iops, the relief valve Water Air uses the sir-In/water-out principle to Patent 44,241.752 Out in stop potential backilow. Now Available, WattsBox insulated Enclosures. For more information, send for ES-W13 or ES-WB-T. A ASAAPSM IN VALVE ?RCIVNO&OGY FM F LIN qWAT1S REGULATOR —Sluice 's7m Watts Industries. lnc., Water Products Division • Safety & Control Valves First '' Mod 213-724-5227 DELCO SALES PAGE @2 ES-909RP0A Series 909RPDA Reduced Pressure Detector. Assembly' . Sizes: 21/2", 3", 4", 6", 811, 1 O 64, 76,100,150,200, 250mm 9O9RPDAOSy Series 909RPDA are designed exclusively for use in accordance with water utility authority containment requirements. It is mandatory to prevent the reverse flow of fire protection system substances, i.e.. glycerin wetting agents, stagnant water and water of non-potable quality from being pumped or siphoned into the potable water line. BENEFITS: Detects leaks.. . with emphasis on the cost of unaccount- a t. . to r- incorporates a meter which allow the water utility to: Detet leaks tnat historically create great annual cost due to waste. it prqvides a detection point for unauthorized use. It can help locate illeg3l taps. Module check design concept facilitates maintenance and assembly ac- cess. Al sizes are standardiy equipped with AWWA epoxy coated, UL/ FM listed OS&Y resilient seated gate valves, CFM (cubic feet per minute) or GPM, (gallon per minute) meter and ball type test cocks. A pressure differential relief vale is located in a zone between the check valves. Feature a modular design concept which facilitates maintenance and assembly access. All sizes are standardly equipped with gate valves and ball tvoe test cocks. Body construction fused epoxy coated cast iron Repijaceable bronze seats Maximum flow at low pressure drop Compact for economy combined with performance DeslQn simplicity for easy maintenance Furnished with % x3/4 (15 x 19mm) racordall meter ModI 25, bronze N 4ECIAL TOOLS REQUIRED OY. with outside stem & yoke resilient seated gate valves CIfM - with cubic feet per minute meter GPM - vJith.gallons per minute meter less gate valves (4-10')(1 00-250mm) A Red ued Pressure Detector Check Valve/Backf low Preventer shall be installeq on fire protection systems when connected to a public water supply. 1 Degree of hazard present is determined by the local authority ..._.. having jurisdiction. The unit—shall be a complete assembly including UL listed OS&Y shutoff valves with FM approval, including an auxiliary line conisting of an approved backilow preventer and water meter. Inc assembly shall meet the requirements 01 ASSE No. 1047; AWWA C511-92.: UL Classified File No. EX3 185; CSA B64 and USC Manual 8th. Edition. Watts Regulator Co. Series 909RPDA. 03/e6/1998 15:30 213-724-5227 DELCO SALES PAGE @3 MATERIALS Size 2W 10' ( 64.250mm) have epoxy coated cast iron body. bronze not and 6isr nQlder stainless steel trim and durable, tight-seating rubber check valve dlsc& All sizes 1uhlshed with bronze body ball valve test cocks. Furnished with out- side stem ind yoke (OSAY) gate valves UL/FM listed. No. 909RPDA bypass line unit coisists of an approved No. 909 reduced pressure backflow preven- tsr assembfr and CFM % a V4 (16 xl 9mm) water meter. ASSE No. 1047 AWWA C511-92: CSA 864 UL Classified File No. 5X3185; UI/FM. USC Manual for Cross-connection Control. 8th Edition APPROVALS ASSE: UL/FM Approved by the foundation for Cross-Connection Control and Hydraulic Research at the University of Southern California. Series 909AG AIR GAPS When installing a drain line. use Series 909 air gaps on No. 909 back- flow preventers. Air Can Dimensions Ima Isip For Ns. Orals Outlet blminslsii. No. O9$lzss size & I WalM ___ I. mm is. mm is. mm Is. mm lbs. 85$. 909A0•F 2½.3 I 64.76 2 51 4% 111 8f. 172 3.3 1.5 90946-K 4-6 1102-152 3 76 1 102 6%. 160 11"1 243 6.3 2.5 909A6-M 8-10 1203-254 4 7%. 186 11½ 286 15.5 7.0 poxy coatea Sizes 2W through 10 (64-250mm) are suitable for supply pressures up to 175 PSI (12.1 bars) and water temperatures to 140'F (60C) maximum. NOTE Piping for 3 909 will start from 01 gate valve and connect at 12 check valve. i D A (9090S&Y. OO9NRS) r0A DImensIon. We A C 0 Di E. 14 F.Fi 6 L S I Ti W,iØt In. mm In. mm j aim In. mm lii. mm In. mm is. mm In. mm In. mm In. I mm In. I mm in. 'em Iii. I kpa. 2½.3 6416 42½ 11070 iltil 470 5%61133 4½ 114 12 305 8 1203 7 178 6% 664 14 356 9 229 194 230 104 410255½ 1400 23~1 603 6 152 5% 149 17 432 9 1229 9½ 247 940 15 381 ~ 316 1~ 299 470 213 6 152 65% 1664 32½1 826 6 152 6 152 20~ 527 10~ 1267 14½ 365 44½ 1 52 3 1130 16 406 1 113 3% 346 1 17 1 11~ 299 798 362 $ 203 78v. 1985 39¼! 997 9~ 248 8¼ 219 26 660 11½ 1292 16½ 470 5½ 1403 17 432 18½ 470 16% 416 1456 660 10 254 93% 2378 9~ 246 2% 219 32 813 131!30 21½ 546 67½ 1715 18 457 18½ 470 16% 416 2230 1012 2 83/86/1996 15:38 213-724-5227 DELCO SALES PAGE 84 CAPACITY (T lypical maximum flow rate (7.5 feet/w.) use psi 21A" 909RPDA • bass psi 3 9O9RPDA2.1 . 38 1.7 1.4 1 1 T_j I U1 LH O 20 40 80 50 100 120 140 160 110 200 220 240 GPM a so so so 120 150 160 210 210 275 300 333360 GPM 0 76 152 226 304 810 458 532 608 664 760 138 812 LPM 0 114 228 342 455 570 681 708 812 11125 1110 12541200 LPM 5 7.5 10 16 FPS $ 7.5 10 15 FPS 1.8 2.3 3.0 4.9 MPS 1.5 2.3 3.0 4.5 Mn bait psi 4m 909RPDA * U1HHf1 O 50 100 150 200 250 800 850 400 450 500 560 500 GPM 0 190 810 570 750 960 1140 1330 1520 1711 100 20002200 LPM $ 7.5 10 15 FPS 1.5 2.3 3.0 4.6 MPS. ISIS pal 80 909RPDA * 1:7 26 1.4 20 1.0 15soft .7 10 .3 5 00 0 200 400 600 600 1000 1200 1400 1600 GPM 11 760 1520 2280 3040 3300 1650 $320 6050 LPM 5 7.5 10 15 FPS 1.5 2.3 3.0 4.8 MPS ::I.ikTLijI ------ ___________I ------ __________I ------ I - assess -- ______, ------ I 4 ['Ji•L1 LI I 11,,,I1 7 I1_____I -- .____ 200 400 800 100 1000 1200 1400 1600 1800 2000 GPM I 250 $00 750 1000 1230 1500 1750 2000 2230 2500 2750 3500 GPM 760 1520 2260 3040 3600 4510 5320 5080 6640 7100 LPM 0 950 ilss 2150 3100 1735 0700 1150 7500 $550 9500 10450 iuoo LPM 5 7.1 10 15 FPS $ 7.5 10 FPS 1.5 2.3 3.0 46 MPS 1.5 2.3 3.0 MPS Watts product specifications In U.S. customary units and metric are approximate and are provid e d f o r r e f e r e n c e only. For precise measurements. please contact Watts Technical Service. Watts reserves the right to change or modify produc t d e s i g n . c o n s t r u c t i o n , s p e c i f i c a t i o n s , o r m a t e r i a l s w i t h - out prior notice and without incurring any obligation to make such Changes and modifications on Watts products previously or subsequently sold. 3 L. COSCO FIRE PROTECTION, INC. 321 EAST GARDENA BOULEVARD GARDENA, CA 90247 ..UN 05 199R Bernrd Eros. C-.1- HYDRAULIC CALCULATIONS FOR LEGOLAND/BEGINNING/WEST COMPLEX ONE LEGO DRIVE CARLSBAD, CA FILE NUMBER: LAC6163-B DATE: 22 MAY 98 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: .10 GPM/SQ. FT. AREA OF APPLICATION: 1500 SQ. FT. COVERAGE PER SPRINKLER: 169.63 SQ. FT. (225 SQ FT MAX) NUMBER OF SPRINKLERS CALCULATED: 11 FLOW AND PRESSURE (@ BOR): 265.7 gpm @ 65.5 psi FLOW AND PRESSURE (@ SOURCE) 315.8 gpm @ 85.3 psi SPRINKLER ORIFICE SIZE: .1/2 inch NAME OF CONTRACTOR: COSCO FIRE PROTECTION, INC. DESIGN/LAYOUT BY: S. HANSEN AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD AND SCHIRMER ENGINEERG CONTRACTOR CERTIFICATION NUMBER: C-16 577621 CALCULATIONS BY HASS COMPUTER PROGRAM Line CttCrksr (LICENSE # 4 C1288D ) ,..r. LINL.. ATLANTA, GA SPRINKLER SYSTEMHYDRAULIC ANALYSIS .. Page .1 ..Date: 05/26/.998 LAC61638..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 98.1 75.6 3545.0 97.8 315.8 85.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 315.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 50.0 GPM OTHER HOSE STREAM ALLOWANCES 50.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 215.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 166.7 - - - - 57.9 2 166.7 - - - - 57.9 - - - 3 166.7 - - - - 57.9 4 . 166.7 - - - - 57.9 5 166.7 - - -i - 57.9 6 166.7 - - - 57.9 - - - 7 166.7 - - - - 57.9 8 166.7 ---- 57.9 9 166.7 -- -- 57.9 10 166.7 - - - - 57.9 11 166.7 - - - - 57.9 12 166.7 - - - - 57.9 - - - 13 166.7 - - - - . 57.9 14 166.7 - - - - 57.9 - - - 15 166.7 - - - - 57.9 16 .166.7 - - - - . 57.9 17 166.7 - - - - 57.9 18 166.7 - - - - 57.9 19 166.7 - - - - 57.9 20 166.7 - - - - 57.9 - - - 21 166.7 - - - - 57.9 22 166.7 - - - - 57.9 - - - 23 166.7 -- - - 57.9 24 166.7 - - - - 57.9 25 166.7 - - - - 57.9 26 166.7 - - - - 57.9 27 166.7 - - - - 57.9 _50 161.5 K= 5.60 9.2 17.0 51 161.5 K= 5.60 10.4 18.0 52 161.5 K= 5.60 10.2 17.9 53 161.5 K= 5.60 10.5 18.1 54 161.5 K= 5.60 10.9 18.5 55 161.5 . K= 5.60 11.1 18.7 56 161.5. K= 5.60 12.3 19.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS-.' Page 2 Date: 05/26/1998 LAC6163B..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX N ODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 57 161.5 K= 5.60 12.6 19.9 59 161.5 K= 5.60 14.9 21.6 59 161.5 K= 5.60 15.2 21.8 60 161.5 K= 5.60 19.1 24.4 .100 165.7 - - - - 58.3 - - - 101 166.7 - - - - 57.9 102 165.7 - - - - 58.3 - - - .133 166.7 - - - - 57.9 - - - 104 165.7 - - - - 58.3 - - - 105 .166.7 - - - - 57.9 106 165.7 - - - - 58.3 - - - 137 166.7 - - - - 57.9 108 165.7 - - - - 58.3 139 166.7 - --- . 57.9 110 165.7 - - - - 58.3 11L 166.7 - - - - 57.9 112 165.7 - - - - 58.3 113 166.7 - - - - 57.9 11.4 :65.7 - - - - 58.3 - - - 115 .66.7 - - - - 57.9 116 :65.7 - - - - 58.3 117 166.7 . - - - - 57.9 - - - 118 :65.7 - - - - 58.3 - - - 119 .66.7 ---- 57.8 120 :65.7 - - -, - . 58.3 - - - 12: :66.5 - - - - 57.9 122 165.7 - - - - 58.3 123 166.7 - - - - 57.8 124 161.5 ---- 125 161.5 - - - - 11.5 - - - 126 161.5 - - - - 12.2 - - 127 161.5 - - - 13.8 - - - 128 :61.5 - - - - :6.7 - - - 129 161.5 - - - - 21.3 - - - 130 161.5 - - - - - 27.0 - - - 131 161.5 - - - - 32.8 132 161.5 - - - - 50.3 133 165.7 - - - - 50.0 134 165.7 - - - - 55.4 135 165.7 - - - - 56.0 136 165.7 - - - - 56.0 - - - 137 165.7 - - - - 57.5 -- - 138 165.7 - --•- 57.5 139 165.7 - - - - 58.5 .140 165.7 - - - - 58.5 - - - 141 165.7 - - - - 59.0 142 165.7 - --- 59.0 143 165.7 - - - - 59.4 144 165.7 - - - - 59.4 TOR 164.2 - - - - 60.7 BOR 1534..5 HOSE STREAM 65.5 50.0 BF1 150.0 - - - - 68.1 BF2 156.0 . - - - - 65.8 BF3 156.0. - - - - 80.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 - - Date: 05/26/1998 LAC6163B..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) BF4 150.0 - - - - 83.7 SRC 150.0 SOURCE 85.3 265.8 n SPRINKLER SYSTEM HYDRAULIC ANALYSIS Rage 4 .Date: 05/26/1998 LAC6163B.SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA PIPE TAG . Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 1 -1.1 1.380 PL 6.13 PF 0.0 .1 166.7 0.0 57.9 0.0 0.2 120 FTG ---- PE 0.0 2 166.7 0.0 57.9 0.0 0.000 IL 6.13 PV 0.0 Pipe: 2 -1.1 1.380 PL 6.67 PF 0.0 2 166.7 0.0 57,9 0.0 0.2 120 FTG E PE 0.0 3 166.7 0.0 57.9 0.0 0.000 TL 9.67 PV 0.0 Pipe: 3 -1.1 1.380 PL 2.00 PF 0.0 3 166.7 0.0 57.9 0.0 0.2 120 FTG E PE 0.0 4 166.7 0.0 57.9 0.0 0.000 IL 5.00 PV 0.0 Pipe: 4 -1.1 1.380 PL 1.46 PF 0.0 4 166.7 0.0 57.9 0.0 0.2 120 FIG ---- PE 0.0 5 166.7 0.0 57.9 0.0 0.000 TL 1.46 PV 0.0 Pipe: 5 -1.1 1.380 PL 10.00 PF 0.0 5 166.7 0.0 57.9 0.0 0.2 120 FTG ---- PE 0.0 6 166.7 0.0. 57.9 0.0 0.000 TL 10.00 PV 0.0 Pipe: 6 -1.1 1.380 PL 10.00 PF 0.0 6 166.7 0.0 57.9 0.0 0.2 120 FIG ---- PE 0.0 7 166.7 0.0 57.9 0.0 0.000 TL 10.00 PV 0.0 Pipe: 7 . -1.1 1.380 PL 19.96 PF 0.0 7 166.7 0.0 57.9 0.0 0.2 120 FIG ---- PE 0.0 8 166.7 0.0 57.9 0.0 0.000 IL 19.96 PV 0.0 Pipe: 8 -1.9 1.610 PL 6.08 PF 0.0 8 166.7 0.0 57.9 0.0 0.3 120 FIG E PE 0.0 109 166.7 0.0 57.9 0.0 0.000 TL 10.08 PV 0.0 Pipe: 9 -1.9 2.635 PL 1.00 PF 0.0 109 166.7 0.0 57.9 0.0 0.1 120 FTG T PE 0.4 108 165.7 0.0 58.3 0.0 0.000 IL 17.47 PV 0.0 Pipe: 10 -0.5 1.380 PL 6.13 PF 0.0 166.7 0.0 57.9 0.0 0.1 120 FTG ---- PE 0.0 10 166.7 0.0 57.9 0.0 0.000 IL .6.13 PV 0.0 Pipe: 11 0.0 1.049 PL 1.00 PF 0.0 -11 166.7 0.0 57.9 0.0 0.0 120 FIG T PE 0.0 10 166.7 0.0 57.9 0.0 0.000 TL 6.00. PV 0.0 Pipe: 12 -0.5 1.380 PL 6.67 PF 0.0 10 166.7 0.0 57.9 0.0 0.1 120 FIG I PE 0.0 12 166.7 0.0 57.9 0.0 0.000 TL 12.67 PV 0.0 Pipe: 13 -2.0 1.380 PL 1.46 PF 0.0 12 166.7 0.0 57.9 0.0 0.4 120 FTG ---- PE 0.0 13 166.7 0.0 57.9 0.0 0.000 IL 1.46 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5. .Date: 05/26/1998 LAC6163B.SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX 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 -2.0 1.380 PL 10.00 PF 0.0 -13 166.7 0.0 57.9 0.0 0.4 120 FTG ---- PE 0.0 14 166.7 0.0 57.9 0.0 0.000 IL 10.00 PV 0.0 Pipe: 15 -2.0 1.380 PL 10.00 PF 0.0 14 166.7 0.0 57.9 0.0 0.4 120 FIG ---- PE 0.0 15 166.7 0.0 57.9 0.0 0.000 TL 10.00 PV 0.0 Pipe: 16 -2.0 1.610 PL 26..04 PF 0.0 15 166.7 0.0 57.9 0.0 0.3 120 FTG T PE 0.0 113 166.7 0.0 57.9 0.0 0.000 IL 34.04 PV 0.0 Pipe: 17 10.1 2.635 PL 1.00 PF 0.0 113 166.7 0.0 57.9 0.0 0.6 120 FTG T PE 0.4 112 165.7 0.0 58.3 0.0 0.000 TL 17.47 PV 0.0 Pipe: 18 1.5 1.380 PL 8.00 PF 0.0 12 166.7 0.0 57.9 0.0 0.3 120 FTG E PE 0.0 16 166.7 0.0. 57.9 0.0 0.000 IL 11.00 PV 0.0 Pipe: 19 1.5 1.380 PL 1.46 PF 0.0 16 166.7 0.0 57.9 0.0 0.3 120 FIG ---- PE 0.0 17 166.7 0.0 57.9 0.0 0.000 IL 1.46 PV 0.0 Pipe: 20 1.5 1.380 PL 9.00 PF 0.0 17 166.7 0.0 57.9 0.0 0.3 120 FIG E PE 0.0 .18 166.7 0.0 57.9 0.0 0.000 IL 12.00 PV 0.0 Pipe: 21 1.5 1.380 PL 1.00 PF 0.0 18 166.7 0.0 57.9 0.0 0.3 120 FIG E PE 0.0 19 166.7 0.0 57.9 0.0 0.000 TL 4.00 PV 0.0 Pipe: 22 . 1.5 1.380 PL 1.00 PF 0.0 19 166.7 0.0 57.9 0.0 0.3 120 FIG ---- PE 0.0 20 166.7 0.0 57.9 0.0 0.000 IL 1.00 PV 0.0 Pipe: 23 1.5 1.380 PL 10.00 PF 0.0 20 166.7 0.0 57.9 0.0 0.3 120 FIG ----- PE 0.0 21 166.7 0.0 57.9 0.0 0.000 TL 10.00 PV 0.0 Pipe: 24 .1.5 1.610 PL 29.04 PF 0.0 -21 166.7 0.0 57.9 0.0 0.2 120 FTG 2ET PE 0.0 117 166.7 0.0 57.9 0.0 0.000 IL 45.04 PV 0.0 Pipe: 25. 1.5 2.635 PL 1.00 PF 0.0 117 166.7 0.0 57.9 0.0 0.1 . 120 FIG T PE 0.4 116 165.7 0.0 58.3 0.0 0.000 TL 17.47 PV 0.0 Pipe: 26 2.4 1.380 PL 6.00 PF 0.0 22 166.7 0.0 57.9 0.0 0.5 120 FTG ---- PE 0.0 23 166.7 0.0 57.9 0.0 0.001 IL 6.00 PV 0.0 SPRINKLER SYSTEM HYDRAULICANALYSIS Page 6 -Date: 05/26/1998 LAC6163B.SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont..) PIPE TAG O(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 2.4 1.380 PL 10.00 PF 0.0 -23 166.7 0.0 57.9 0.0 0.5 120 FIG ---- PE 0.0 24 166.7 0.0 57.9 0.0 0.001 TL 10.00 PV 0.0 Pipe: 28 . 2.4 1.380 PL 10.00 PF 0.0 24 166.7 0.0 57.9 0.0 0.5 120 FIG ---- PE 0.0 25 166.7 0.0 57.9 0.0 0.001 TL 10.00 PV 0.0 Pipe: 29 2.4 1.380 PL 8.00 PF 0.0 25 166.7 0.0 57.9 0.0 0.5 120 FTG ---- PE 0.0 26 166.7 0.0 57.9 0.0 0.001 IL 8.00 PV 0.0 Pipe: 30 2.4 1.380 PL 9.50 PF 0.0 26 166.7 0.0 57.9 0.0 0.5 120 FTG ---- PE 0.0 27 166.7 0.0 57.9 0.0 0.001 TL 9.50 PV 0.0 Pipe: 31 2.4 1.610 PL 18.50 PF 0.0 27 166.7 0.0 57.9 0.0 0.4 120 FTG T PE 0.1 121 166.5 0.0. 57.9 0.0 0.000 IL 26.50 PV 0.0 Pipe: 32 2.4 2.635 PL 1.00 PF 0.0 121 166.5 0.0 57.9 0.0 0.1 120 FIG I PE 0.3 120 165.7 0.0 58.3 0.0 0.000 TL 17.47 PV 0.0 Pipe: 33 -0.8 1.380 PL 82.71 PF 0.0 101 166.7 0.0 57.9 0.0 0.2 120 FIG 8E2T PE 0.0 8 166.7 0.0 57.9 0.0 0.000 TL 118.71 PV 0.0 Pipe: 34 0.8 2.635 PL 1.00 PF 0.0 101 166.7 0.0 57.9 0.0 0.0 120 FIG I PE 0.4 100 165.7 0.0 58.3 0.0 0.000 TL 17.47 PV 0.0 Pipe: 35 1.1 2.635 PL 1.00 PF 0.0 103 166.7 0.0 57.9 0.0 0.1 120 FIG T PE 0.4 102 165.7 0.0 58.3 0.0 0.000 IL 17.47 PV 0.0 Pipe: 36 0.4 2.635 PL 1.00 PF 0.0 105 166.7 0.0 57.9 0.0 0.0 120 FIG I PE 0.4 104 165.7 0.0 58.3 0.0 0.000 TL 17.47 PV 0.0 Pipe: 37 -2.4 2.635 PL 1.00 PF 0.0 -107 166.7 0.0 57.9 0.0 0.1 120 FIG I PE 0.4 106 165.7 0.0 58.3 0.0 0.000 IL 17.47 PV 0.0 Pipe: 38 15.5. 2.635 PL 1.00 PF 0.0 111 166.7 0.0 57.9 0.0 0.9 120 FIG El PE 0.4 110 165.7 0.0 58.3 0.0 0.001 TL 25.71 PV 0.0 Pipe: 39 6.2 2.635 PL 1.00 PF 0.0 115 166.7 0.0 57.9 0.0 0.4 120 FTG ET PE 0.4 114 165.7 0.0 58.3 0.0 0.000 IL 25.71 PV 0.0 SPRINKLER SYSTEM HYDRAULIC 7-4. ANALYSIS Page 05/26/1998 LAC6163B..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (Fl) (K) (PSI) (GPM) F.L./FT (Psi) Pipe: 40 -13.3 •2.635 PL 1.00 .PF 0.0 -119 166.7 0.0 57.8 0.0 0.8 120 FIG ET PE 0.4 .118 165.7 0.0 58.3 0.0 0.001 TL 25.71 PV 0.0 Pipe: 41 -20.5 2.635 PL 1.00 PF 0.0 123 166.7 0.0 57.8 0.0 1.2 120 FIG El PE 0.4 122 165.7 0.0 58.3 0.0 0.002 TL 25.71 PV 0.0 Pipe: 42 -17.0 1.049 PL 13.63 PF 2.2 50 161.5 5.6 9.2 17.0 6.3 120 FTG 2ET PE 0.0 124 161.5 0.0 11.4 0.0 0.096 IL 22.63 PV 0.3 Pipe: 43 -18.0 1.049 PL 4.63 PF 1.0 51 161.5 5.6 10.4 18.0 6.7 120 FIG I PE 0.0 124 161.5 0.0 11.4 0.0 0.107 IL 9.63 PV 0.3 Pipe: 44 -17.9 1.049 PL 6.88 PF 1.3 52 161.5 5.6 10.2 17.9 6.7 120 FTG T PE 0.0 125 161.5 0.0 11.5 0.0 . 0.106 IL 11.88 PV 0.3 Pipe: 45 -18.1 1.049 PL 4.63 PF 1.0 53 161.5 5.6 10.5 18.1 6.7 120 FIG I PE 0.0 125 161.5 0.0 11.5 0.0 0.108 IL 9.63 PV 0.3 Pipe:. 46 -18.5 1.049 PL 6.88 PF 1.3 54 161.5 5.6 10.9 18.5 6.9 120 FTG T PE 0.0 126 161.5 0.0 12.2 0.0 0.113 IL 11.88 PV 0.3 Pipe: 47 -18.7 1.049 PL 4.63 PF 1.1 55 161.5 5.6 11.1 18.7 6.9 120 FIG I PE 0.0 126 161.5 0.0 12.2 0.0 0.115 TL 9.63 PV 0.3 Pipe: 48 -19.7 1.049 PL 6.88 PF 1.5 56 161.5 5.6 12.3 19.7 7.3 120 FTG T PE 0.0 127 161.5 0.0 13.8 0.0 0.126 IL 11.88 PV 0.4 Pipe: 49 -19.9 1.049 PL 4.63 PF 1.2 57 161.5 5.6 12.6 19.9 7.4 120 FIG I PE 0.0 127 161.5 0.0 13.8 0.0 0.129. IL 9.63 PV 0.4 Pipe: 50 -21.6 1.049 PL 6.88 PF 1.8 -58 161.5 5.6 14.9 21.6 8.0 120 FIG T PE 0.0 128 161.5 0.0 16.7 0.0 0.150 IL 11.88 PV 0.4 Pipe: 51 -21.8 1.049 PL 4.63 PF 1.5 59 161.5 5.6 15.2 21.8 8.1 120 FIG I PE 0.0 128 161.5 0.0 16.7 0.0 0.153 TL 9.63 PV 0.4 Pipe: 52 -24.4 1.049 PL 6.88 PF 2.2 60 161.5 5.6 19.1 24.4 9.1 120 FIG T PE 0.0 129 161.5 0.0 21.3 0.0 0.189 IL 11.88 PV 0.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS -. Page 8 .Date: 05/26/1998 LAC61638..SDF .JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HLaJ(C) (Fl) SUM. NODES (Fl) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 53 -35.0 2.067 PL 8.00 PF 0.1 .124 161.5 0.0 11.4 0.0 3.3 120 FTG ---- PE 0.0 125 161.5 0.0 11.5 0.0 0.013 IL 8.00 PV 0.1 Pipe: 54 -71.1 2.067 PL 14.75 PF 0.7 125 161.5 0.0 11.5 0.0 6.8 120 FTG ---- PE 0.0 126 161.5 0.0 12.2 0.0 0.050 TL 14.75 PV 0.3 Pipe: 55 -108.2 2.067 PL 14.75 PF 1.6 126 161.5 0.0 12.2 0.0 10.3 120 FTG ---- PE 0.0 127 161.5 0.0 13.8 0.0 0.109 IL 14.75 PV 0.7 Pipe: 56 -147.8 2.067 PL 14.75 PF 2.9 127 161.5 0.0 13.8 0.0 14.1 120 FTG ---- PE 0.0 128 161.5 0.0 16.7 0.0 0.194 TL 14.75 PV 1.3 Pipe: 57 . -191.3 2.067 PL 14.75 PF 4.6 128 161.5 0.0 16.7 0.0 18.3 120 FTG ---- PE 0.0 129 161.5 0.0. 21.3 0.0 0.312 IL 14.75 PV 2.3 Pipe: 58 -215.7 2.067 PL 14.75 PF 5.7 129 161.5 0.0 21.3 0.0 20.6 120 FIG ---- PE 0.0 130 161.5 0.0 27.0 0.0 0.390 IL 14.75 PV 2.9 Pipe: 59 -215.7 2.067 PL 14.75 PF 5.7 130 161.5 0.0 27.0 0.0 20.6 120 FIG ---- PE 0.0 131 161.5 0.0 32.8 0.0 0.390 IL 14.75 PV 2.9 Pipe: 60 -215.7 2.067 PL 10.08 PF 17.6 131 161.5 0.0 32.8 0.0 20.6 120 FIG 7E PE 0.0 132 161.5 0.0 50.3 0.0 0.390 TL 45.08 PV 2.9 Pipe: 61 -215.7 2.635 PL 4.00 PF 1.5 132 161.5 0.0 50.3 0.0 12.7 120 FTG E PE -1.8 133 165.7 0.0 50.0 0.0 0.119 IL 12.24 PV 1.1 Pipe: 62 -215.7 2.635 PL 29.04 PF 5.4 133 165.7 0.0 50.0 0.0 12.7 120 FTG I PE 0.0 134 165.7 0.0 55.4 0.0 0.119 TL 45.51 PV 1.1 Pipe: 63 -215.7 2.635 PL 4.58 PF 0.5 .134 165.7 0.0 55.4 0.0 12.7 120 FTG ---- PE 0.0 -135 165.7 0.0 56.0 0.0 0.119 IL 4.58 PV 1.1 Pipe: 64 -195.2 2.635 PL 14.92 PF 1.5 135 165.7 0.0 56.0 0.0 11.5 120 FIG ---- PE 0.0 137 165.7 0.0 57.5 0.0 0.099 TL 14.92 PV 0.9 Pipe: 65 -181.9 2.635 PL 12.25 PF 1.1 137 165.7 0.0 57.5 0.0 10.7 120 FIG ---- PE 0.0 139 165.7 0.0 58.5 0.0 0.087 IL 12.25 PV 0.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 Date: 05/26/1998 LAC6163B..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont..) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HL4(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 66 -188.1 2.635PL 5.33 PF 0.5 .139 165.7 0.0 58.5 0.0 11.1 120 FTG ---- PE 0.0 141 165.7 0.0 59.0 0.0 0.093 TL 5.33 PV 0.8 Pipe: 67 -200.2 2.635 PL 4.00 PF 0.4 141 165.7 0.0 59.0 0.0 11.8 120 FTG ---- PE 0.0 143 165.7 0.0 59.4 0.0 0.104 TL 4.00 PV 0.9 Pipe: 68 -215.7 4.260 PL. 15.50 PF 0.6 143 165.7 0.0 59.4 0.0 4.9 120 FIG 3E PE 0.6 TOR 164.2 0.0 60.7 0.0 0.012 IL 55.00 PV 0.2 Pipe: 69 0.8 2.635 PL 8.00 PF 0.0 100 165.7 0.0 58.3 0.0 0.0 120 FIG I PE 0.0 102 165.7 0.0 58.3 0.0 0.000 TL 24.47 PV 0.0 Pipe: 70 -2.4 2.635 PL 10.50 PF 0.0 106 165.7 0.0 58.3 0.0 0.1 120 FTG ---- PE 0.0 104 165.7 0.0 58.3 0.0 0.000 TL 10.50 PV 0.0 Pipe: 71 -1.9 2.635 PL 9.00 PF 0.0 104 165.7 0.0 58.3 , 0.0 0.1 120 FIG ---- PE 0.0 102 165.7 0.0 58.3 0.0 0.000 IL 9.00 PV 0.0 Pipe: 72 -20.5 2.635 PL 4.00 PF 0.0 122 165.7 0.0 58.3 0.0 1.2 120 FIG ---- PE 0.0 1.20 165.7 0.0 58.3 0.0 0.002 IL 4.00 PV 0.0 Pipe: 73 -18.1 2.635 PL 4.50 PF 0.0 120 165.7 0.0 58.3 0.0 1.1 120 FIG ---- PE 0.0 118 165.7 0.0 58.3 0.0 0.001 IL 4.50 PV 0.0 Pipe: 74 -31.5 2.635 PL 6.58 PF 0.0 118 165.7 0.0 58.3 0.0 1.9 120 FTG ---- PE 0.0 116 165.7 0.0 58.3 0.0 0.003 IL 6.58 PV 0.0 Pipe: 75 -29.9 2.635 PL 5.67 PF 0.0 116 165.7 0.0 58.3 0.0 1.8 120 FIG ---- PE 0.0 114 165.7 0.0 58.3 0.0 0.003 TL 5.67 PV 0.0 Pipe: 76 -23.8 2.635 PL 5.33 PF 0.0 114 165.7 0.0 58.3 0.0 1.4 120 FTG ---- PE 0.0 :112 .165.7 0.0 58.3 0.0 0.002 IL 5.33 PV 0.0 Pipe: 77 -13.6 2.635 PL 4.00 PF 0.0 112 165.7 0.0 58.3 0.0 0.8 120 FIG ---- PE 0.0 110 165.7 0.0 58.3 0.0 0.001 IL 4.00 PV 0.0 Pipe: 78 -1.9 2.635 PL 8.00 PF 0.0 108 165.7 0.0 58.3 0.0 0.1 120 FIG ---- PE 0.0 110 165.7 0.0 58.3 . 0.0 0.000 IL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 Date: 05/26/1998 . . LAC6163B.SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX 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: 79 20.5 1.38.0 PL 50.25 PF 2.2 123 166.7 0.0 57.8 0.0 4.4 120 FTG 2ET PE 0.4 -.136 165.7 0.0 56.0 0.0 0.036 TL 62.25 PV 0.1 Pipe: 80 20.5 2.635 PL 1.00 PF 0.0 136 165.7 0.0 56.0 0.0 1.2 120 FIG I PE 0.0 135 165.7 0.0 56.0 0.0 0.002 TL 17.47 PV 0.0 Pipe: 81 13.3 1.380 PL 43.25 PF 0.8 119 166.7 0.0 57.8 0.0 2.9 120 FTG T PE 0.4 138 165.7 0.0 57.5 0.0 0.016 IL 49.25 PV 0.1 Pipe: 82 13.3 2.635 PL 1.00 PF 0.0 138 165.7 0.0 57.5 0.0 0.8 120 FIG I PE 0.0 137 165.7 0.0 57.5 0.0 0.001 TL 17.47 PV 0.0 Pipe: 83 . -6.2 1.380 PL 43.25 PF 0.2 115 166.7 0.0 57.9 0.0 1.3 120 FTG T PE 0.4 140 165.7 0.0. 58.5 0.0 0.004 IL 49.25 PV 0.0 Pipe: 84 -6.2 2.635 PL 1.00 PF 0.0 140 165.7 0.0 58.5 0.0 0.4 120 FIG I PE 0.0 139 165.7 0.0 58.5 0.0 0.000 TL 17.47 PV 0.0 Pipe: 85 -12.1 1.380 PL 43.25 PF 0.7 113 166.7 0.0 57.9 0.0 2.6 120 FTG T PE 0.4 142 165.7 0.0 59.0 0.0 0.014 TL 49.25 PV 0.0 Pipe: 86 -12.1 2.635 PL 1.00 PF 0.0 142 165.7 0.0 59.0 0.0 0.7 120 FIG I PE 0.0 141 165.7 0.0 59.0 0.0 0.001 TL 17.47 PV 0.0 Pipe: 87 -15.5 1.380 PL 43.25 PF 1.1 111 166.7 0.0 57.9 0.0 3.3 120 FTG T PE 0.4 144 165.7 0.0 59.4 0.0 0.021 IL 49.25 PV 0.1 Pipe: 88 -15.5 2.635 PL 1.00 PF 0.0 144 165.7 0.0 59.4 0.0 0.9 120 FIG I PE 0.0 143 165.7 0.0 59.4 0.0 0.001 TL 17.47 PV 0.0 Pipe:69 -2.4 1.380 PL 3.50 PF 0.0 22 166.7 0.0 57.9 0.0 0.5 120 FTG T PE 0.0 - 107 166.7 0.0 57.9 0.0 0.001 IL 9.50 PV 0.0 Pipe: 90 0.5 1.380 PL 3.21 PF 0.0 9 166.7 0.0 57.9 0.0 0.1 120 FIG I PE 0.0 105 166.7 0.0 57.9 0.0 0.000 TL 9.21 PV 0.0 Pipe: 91 1.1 1.380 PL 3.21 PF 0.0 1 166.7 .0.0 57.9 0.0 0.2 120 FTG T PE 0.0 103 166.7 .0.0 57.9 0.0 0.000 IL 9.21 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 .Date: 05/26/1998 LAC61638.SDF 30B TITLE: LEGOLAND/BEGINNING/WEST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (Fl) (K) (PSI) (GPM) F.L./FT (PSI) • Pipe: 92 -215.7 4.260 PL 13.71 PF 0,2 .TOR 164.2 0.0 60.7 0.0 4.9 120 FTG ---- PE 4.6 153.5 H.S. 65.5 50.0 0.012 TL 13.71 PV 0.2 Pipe: 93 -265.7 4.095 PL 50.00 PF 1.0 BOR 153.5 H.S. 65.5 50.0 6.5 140 FIG EG PE 1.5 BF1 150.0 0.0 68.1 0.0 0.015 TL 67.34 PV 0.3 • Pipe: 94 -265.7 4.095 PL 6.00 PF 0.3 BF1 150.0 0.0 68.1 0.0 6.5 140 FTG E PE -2.6 BF2 156.0 0.0 65.8 0.0 0.015 IL 20.45 PV 0.3 Pipe: 95 FIXED PRESSURE LOSS DEVICE 8F3 156.0 0.0 80.8 0.0 15.0 psi, 265.7 gpm BF2 156.0 0.0 .65.8 0.0 Pipe: 96 -265.7 4.095 PL 6.00 PF 0.3 BF3 156.0 0.0 80.8 0.0 6.5 140 FTG E PE 2.6 BF4 150.0 0.0. 83.7 0.0 0.015 IL 20.45 PV 0.3 Pipe: 97 -265.8 4.095 PL 60.00 PF 1.6 BF4 150.0 0.0 83.7 0.0 6.5 140 FIG ETG PE 0.0 SRC 150.0 SRCE 85.3 (N/A) 0.015 TL 106.23 PV 0.3 NOTES: Calculations were performed by the HASS 6.2.0 computer program under license no. 4 C1288D granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 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 0.216 gpm. Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 20.6 ft/sec at pipe 58. . SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 .Date: 05/26/1998 . LAC6163B..SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX (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 Eli Tee LngEll ChkVlv -------------------------------------------------------- BfyVlv GatViv AlmChk DPVlv • N. 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 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: * MATERIAL: 540 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E . T L C B G A D Eli Tee LngEi1 ChkVlv BfyVlv GatVlv AlmChk DPVlv 2.635 8.24 16.47 ,5.49 19.22 9.61 1.37 13.73 13.73 4.095 10.86 21.73 6.52 23.90 13.04 2.17 21.73 10.86 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 13.17 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page. 13 Date: 05/26/1998 . .. LAC6163B.SDF JOB TITLE: LEGOLAND/BEGINNING/WEST COMPLEX WATER SUPPLY CURVE 108+ 99*\\\\\ 1 0 \\\\\ 90+ \\\\\ \\\\\\ \\\\\ 81+ \\\\\ 75.6 psi @ 3545 gpm-) * Flow Test Point P72+ R 11 E S S63+ U R E 54+ ( P S I 45+ ) 36+ 27+ 18+ LEGEND X = Required Water Supply 85.33 Psi @ 315.8 gpm u IN 9+ 0 = Available Water Supply 97.84 Psi @ 315.8 gpm +-------I---------+--------+ --------- + ----------- + 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) PAGE 82 :--*-• " WE s;MIX -:- '-,' Relief Valve Piston Auy. Wiper Seal Relief Volvo Bottom Plug Body Flange Spring Msy. HOW IT OPUAT55 The unique rail.f valve construction mcorporates; two channil.: one for air. one for water. When the relief vile opens. as In the-accompanying arItilwater-Out diagram. the right. oto hand channel admits air to tns top of the reduced pressure zone. re- living the zone vacuum. The chin- nil on the left then drama We zone to atmosphere. Therefore. if both check valves foul. and simultaneous ni_vs supply and pcilhive bash pressure develops, the relief wafts Water Air uses The alr-Wwatsr.cui plincipt. to Patent 14,241752 Out in stop potential backilow. Now Available, WattsBoz Insulated Enclosures. For more information, send for ES-W8 or ES-WB-T. ALEADSNINVALVE 7MC#VNOL040V . - 1% qWAT1S° REGULATOR 91'%c. 2174 Wsttslndualriea.lnc... Water Products Division • Safety & Control Valves 1r 909RPDAOSY Cheek May. I Pipe Una Relief Valve Seat center Relief Valve Piston Firs' Mod 03/86/1998 15:38 213-724-5227 VMNA- - Stries 9O9RPDA R ducd'd — D tectorASSernbIy: Siz s: 21/2", 3,4'!, 6°,8, 10 64, 76,100,150, 200,250mm Series 909RPDA are designed exclusively for use in accordance with water itillty authority containment requirements. it Is mandatory to prevent the reverse flow of fire protection system substances, I.e., glycerin wetting agents. stagnant water and water of non-potable quality prom being pumped or siphonedinto the potable water line. BEN EFITS: Detects leaks.. . with emphasis on the cost of unaccount- able water: incorporates a miter which allow the water utility to; Detet leaks that historically create great annual cost due to waste. It provides a detection point for unauthorized use. it can help locate illegdi taps. Mod ula check design concept facilitates maintenance and assembly ac- cess. All sizes are standardly equipped with AWWA epoxy coated, UL/ FM listed OS&Y resilient seated gate valves, CFM (cubic feet per minute) or C" '(gallon per minute) meter and ball type test cocks. A pressure dinerenial relief vale is located in a zone betwein the check valves. Feature a modular design concept which facilitates maintenance and assemIy access. All sizes are standardly equipped with gate valves and bal type test.cocks. BadV construction fused epoxy coated cut Iron Replaceable bronze salts Maximum flaw at low pressure drop Compact for economy combined with performance Desln simplicity for easy maintenance Fum!shed with % x Y4 (15 x 19mm) recordall meter Model 25, bronze NO SPECIAL TOOLS REQUIRED Suflx: 0Y. with outside stem & yoke resilient seated gate valves C1M - with cubic feet per minute meter GPM - with gallons per minute meter less gate valves (4. 101(100.250mm) SPECIFICATIONS A Redu ed Pressure Detector Check Valve!Backflow Preventer shall be installec 1 on fire protection systems when connected to a public water supply. Degree of hazard present Is determined by the local authority \_. having iurlsdiCtion. The unit shall be a complete assembly including UL listeà OS&Y shutoff valves with FM approval. Including an auxiliary line col4sisting of an approved backflow preventer and water meter. The assembly shall meet the requirements 01 ASSE No, 1047; AWWA C511-92: UL Classified File No. EX3.185; CSA 064.and USC Manual 8th. Edition. Watts Regulator Co. Series 909RPDA. PAGE 63 63/06/1998 15:30 213-724-5227 DELCO SALES - ' MATERIALS Size 2%' t4 ir (54.250mm) have epoxy coated cast Iron D*. bronzesext and disc hldsc stainless still trim Sad durab1e.tlpht-seatlng rubber chCCk' valve di All sizes furnished with bronze body ball valve test cocks: thU0t Furnished w side stem 5n1 yoke (OS1Y) pate valves UIJFM listed. 'No. so9pDAbypas::. Selies 909AG one unit co)lslsts it an approved No. 909 reduced pressure bickilow preifl: ter assemb'y and CFM % a VA (16 a 19mm) water mater. AIR GAPS I £ • - When Installing a drain line. use - Series 909 air gaps on No. 909 back- ASS No. 1047: AWWA C511.92: C$A 554 now proven". (IL Ciassilid File No. 5X3185: UI/FM. USC Manu1 for Cross.connscllon Control. 8th EditIon Air Gap Dimensions APPROVALS ____ ______ ASSE:Udy Approve the foundation for Cross-Connection Control and Nydãuhic Ricaarc nc Ufl1vcrItv of Southern California. _________________-- Epoxycoatsd PRESSURE — TEMPERATURE -. Sizes 2W hrough 10' (64-250mm) are euhlaDis for supply pressures up to 175 PSI (12.1 bars) and water temperatures to 1409F (6rC) maximum. .1 h!a ?E I WEIGHTS ( ) NOTE: Piping for 3 809 will start from 01 gate valve and connect at *2 check valve. lien lily For N.. - Drilu Oulist Dimuimlons No. No Sim Size * 1 W.iØl ______ In. mm Ii. mm Is. mm lea. as. 90MG-F 2½.3 64.75 2 51 13•90949-K 6~ 172 3.3 4-6 102-152 3 76 ±4%111 9~. 243 8.3 2.8 909*G-M 8-10 203-211 4 102 11¼ 216 15.5 7.0 Dl Dimensions Sit. A C 0 Di E.Ei fE 6 L I T Weigh in. .ncf In. mm Is. mm ii,. mm In. mm Iii. mm In. mm in. mm In. I mm I In. I mm I.. I mm In. I mm lbs. Egs. 2½.3 66.6 42½ 1070 18½ 470 6'A-[133 4½ 114 12 305 8 1203 7 178 26¼ 564 14 356 9 229 7% 194 230 101 4 10 55½ 1400 23% 603 6 152 5% 149 17 432 9 1229 9½ 241 37 940 15 381 13¼ 315 1171%V,299 470 213 6 152 65½ 1664 32½ 826 6 152 6 152 20% 527 10½ l287 14½ 368 4½ 1130 16 405 13% 348 11% 299 798 352 8 203 78¼ 1985 39½ 997 9% 248 Ski 219 26 660 11½ 1292 18½ 170 55½ 1403 17 432 1814 410 16% 416 1456 560 10 254 93% 2376 48 1219 9% 248 8% 219 32 513 13 1330 21½ 546 67½ 1715 18 457 18½ 470 16¼ 418 2230 1012 2 IbI1b 15:30 2137245227 DELCO SALES FAac 04 jo CAPACITY * 'Typical maximum flow rate (75 lest/eec) bars "I 21ho 909RPDA • ban PSI 3 OOØRPDA • 1.7 26 26 1.4 20 1.4 20 O 20 40 80 00 100 120 140 100 180 200 220 240 GPM 0 30 60 •0_ 120 110 180 210 240 270 300 330360 GPM 0 78 152 228 304 380 456 532 60$ 084 760 638 012 LPM 0 114 220 342 450 570 814 795 912 1021 1110 12541101 LPM 6 7.5 10 ii FPS 5 7.5 10 15 FPS Ii 2.3 3.0 4.9 MPS 1.5 2.3 3.0 4.8 MPS bars pal 4U 909RP0A * !3 10 i444fjffffR I 5$ 100150200 250300850 404 450 500 IS0100GPM 0 160 850 $70 760 950 1140 1330 1520 1715 I= 20002216 LPM s 7.5 Ii 15 FPS 1.5 2.3 3.0 4.6 MPS bin psi 00.9OSPPDA2.1 of 1.7 26 S 9r1f::4IHHHH 0 200 400 000 800 1000 1200 14001600 GPM 9 760 1520 2200 3040 3800 4500 $320 5000 LPM 5 7.5 10 15 :FPS 1.5 2.3 3.0 4.6 MPS bars psi 8" 909RPDAMI * bars P1 10" 909RPDAMI * 2.1 30 1.7 25 I 1:7251 ::; 1 I IA 20 I i.i ___________________________ 1:0 15 IIH[H ___________________________ I Ii t 1 10 .710 .3 5 I .3 00 _J Ce 0 200 400 500 000 1000 1200 1400 1600 10002000 GPM 0 250 500 730 1000 1210 las mo 2000 2030 aoo 2000 3000 8PM 0 700 1520 2280 3040 3000 4580 5320 5080 50407000 LPM 0 950 1100 2100 3500 1750 0700 5050 7500 5550 9500 tout litol LPM 5 75 10 15 FPS $ --7.5 10 FPS 1.5 2.3 3.5 4.6 MPS 1.5 2.3 3.0 MPS Watts product specifications In U.S. customary units and metric-are approximate and are provided for reference only. For precise measuremenil. please contact Watts Technical Service. Watts reserves Me right to chang6 or modify product design. construction, s p e c i f i c a t i o n s , o r m a t e r i a l s w i t h -out prier notice and without incurring any obligation to make such changes and modifications on Watts products previ o u s l y o r . s u b s e u e n u y s o l d . 3 a I S b, 7. •..- •.• BE1;tPDs BROS. CO'STRUCTION SUBMITTAL NO. /53 30 .O2M. ECTC NO._/ REVIEWED FOR GENERAL COe1FOMANCE.BY DATE FILE NUMBER: 61638E DATE: 15 MAY, 1998 CALCULATED AREA: 1500 SQ. FT. -DESIGN DATA- OCCUPANCY CLASSIFICATION: ORDINARY HAZARD II DENSITY: .20 GPM/SQ FT.. AREA OF APPLICATION: 1500 SQ. FT. COVERAGE PER SPRINKLER: 130.0 SQ..FT. [MAX.] NUMBER OF SPRINKLERS CALCULATED: 24 SPRINKLERS FLOW AND PRESSURE (© BOR): 772.1 GPM © 66.9 PSI FLOW AND PRESSURE (© SOURCE) 922.2 GPM © 89.1 SPRINKLER ORIFICE SIZE: 1/2 inch(K=5.6) NAME OF CONTRACTOR: COSCO FIRE PROTECTION, INC. DESIGN/LAYOUT BY: K..DAVIS AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD AND SCHIRMER ENGR. CONTRACTOR CERTIFICATION NUMBER: C16-577621 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE 4* 4 C1288D ) HRS SYSTEMS, INC. ATLANTA, GA LI - REC,FJ\/r AUG 0 6 198 BERNARDS !: COSCO FIRE PROTECTION, IN 321 EAST GARDENA BOULEVAF GARDENA, CA. 90247 11 HYDRAULIC CALCULATIONS FOR: BEGINNINGS/EAST COMPLEX ONE LEGO DRIVE CARLSBAD, CA. SPRINKLER SYSTEM HYDRAULICANALYSIS Page 1 Date: 05/15/1998 6163BE..SDF JOB TITLE: BEGINNINGS/EAST COMPLEX WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 0 PRESS. © DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 98.1 75.6 3545.0 96.2 922.2 89.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 922.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 150.0 GPM OTHER HOSE STREAM ALLOWANCES 100.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 672.2 GPM NODE ANALYSIS DATA NODE TAG 1 2 3 3A 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 - ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 161.0 K= 5.60 27.4 29.3 165.9 - - - - 30.0 160.0 K= 5.60 28.0 29.6 165.4 34.0 163.0 K= 5.60 26.2 . 28.7 165.7 30.5 163.0 K= 5.60 28.2 . 29.7 163.0 K= 5.60 28.9 30.1 165.4 32.9 163.0 K= 5.60 30.4 30.9 161.0 K= 5.60 18.4 24.0 166.2 20.8 165.0 K= 5.60 19.3 24.6 166.2 22.5 161.0 K= 5.60 20.9 25.6 165.8 - - - - 25.2 165.6 - - - 26.3 165.0 K= 5.60 20,3 25.2 165.6 - - - - 24.5 - - 163.0 K= 5.60 23.9 27.4 163.0 K= 5.60 29.7 30.5 163.0 K= 5.60 29.6 30.5 165.4 - - - - 33.4 163.0 K= 5.60 30.8 31.1 163.0 K= 5.60 23.7 27.3 166.3. - - - - 26.5 166.0 - - - - 27.0 166.0 - - - - 27.1 165.0 K= 5.60 . 21.2 25.8 166.0 - - - - 24.3 165.0 K= 5.60 22.4 26.5 165.7 - - - - 28.9 165.5 - - - - 30.4 165.0 K= 5.60. 27.8 29.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 05/15/1998 61636E.SDF JOB TITLE: BEGINNINGS/EAST COMPLEX NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 161.0 K= 5.60 20.7 25.5 35 166.3 - - - 21.8 - - - 36 163.0 K= 5.60 . 20.6 25.4 37 166.0 - - - - 23.5 38 165.0 K= 5.60 21.7 26.1 39 165.7 - - - 27.7 - - -. 40 165.0 K= 5.60 25.5 28.3 41 163.0 K= 5.60 28.7 30.0 42 165.4 - - - - 32.3 - - - 43 163.0 K= 5.60 29.8 30.6 AT 165.4 - - - 35.1 - - - AB 163.5 - - - - 37.1 81 165.4 - - - - 34.7 BB 163.5 - - - - 37.1 - - - Cl 165.4 - - - - 33.7 CB 163.5 - - - - . 37.1 Dl 165.4 - - - - 35.2 DB 163.5 - - - - 37.3 El 165.4 - - - - 35.4 EB 163.5 - - - - 37.5 FT 165.4 - - - - 34.0 FB 163.5 - - - - 37.7 G 163.5 - - - - 43.1 HT 163.5 - - - - .44.9 HB 162.5 - - - - 46.9 JT 162.5 - - - - 49.3 - - - JB 161.5 ---- 50.5 J 161.5 - - - - 63.1 TOR 161.5 - - - 63.6 - - - BOR 154.3 HOSE STREAM 66.9 100.0 K 150.0 - - - - 69.5 L 150.0 - - - - 70.8 --- M 150.0 - - - - 71.2 - - - BF1 156.5 - - - - 69.1 BF2 156.5 - - - - 84.1 - - - N 150.0 - - - - 88.3 - - - SRC 150.0 SOURCE 89.1 772.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 05/15/1998 61638E..SDF JOB TITLE: BEGINNINGS/EAST COMPLEX PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 1 -29.3 1.049 PL 11.92 PF 4.7 1 161.0 5.6 27.4 29.3 10.9 120 FTG 3E PE -2.1 2 165.9 0.0 30.0 0.0 0.264 IL 1.7.92 PV 0.8 Pipe: 2 -29.6 1.049 PL 8.00 PF 4.6 3 160.0 5.6 28.0 29.6 11.0 120 FIG 2E1 PE -2.6 2 165.9 0.0 30.0 0.0 0.269 IL 17.00 PV O.B. Pipe: 3 -58.9 1.380 PL 14.92 PF 3.8 2 165.9 0.0 30.0 0.0 12.6 120 FTG ---- PE 0.2 3A 165.4 0.0 34.0 0.0 0.252 IL 14.92 PV 1.1 Pipe: 4 -58.9 1.610 PL 1.19 PF 1.1 3A 165.4 0.0 34.0 0.0 9.3 120 FIG I PE 0.0 AT 165.4 0.0 35.1 0.0 0.119 IL 9.19 PV 0.6 Pipe: 5 -58.9 1.610 PL 1.92 PF 1.2 AT 165.4 0.0 35.1 0.0 9.3 120 FIG I PE 0.8 AS 163.5 0.0 37.1 0.0 0.119 IL 9.92 PV 0.6 Pipe: 6 -58.9 4.260 PL 5.21 PF 0.0 AS 163.5 0.0 37.1 0.0 1.3 120 FIG ---- PE 0.0 BB 163.5 0.0 37.1 0.0 0.001 IL 5.21 PV 0.0 Pipe: 7 -178.3 4.260 PL 4.00 PF 0.0 BB 163.5 0.0 37.1 0.0 4.0 120 FTG ---- PE 0.0 CB 163.5 0.0 37.1 0.0 0.008 IL 4.00 PV 0.1 Pipe: 8 -335.6 4.260 PL 8.46 PF 0.2 CS 163.5 0.0 37.1 0.0 7.6 120 FIG ---- PE 0.0. DB 163.5 0.0 37.3 0.0 0.026 IL 8.46 PV 0.4 Pipe: 9 . -397.2 4.260 PL 5.00 PF 0.2 DB 163.5 0.0 37.3 0.0 8.9 120 FIG ---- PE 0.0 ES 163.5 0.0 37.5 0.0 0.036 IL 5.00 PV 0.5 Pipe: 10 -506.3 4.260 PL 4,00 PF 0.2 EB 163.5 0.0 37.5 0.0 11.4 120 FIG ---- PE 0.0 FB 163.5 0.0 37.7 0.0 0.056 IL 4.00 PV 0.9 Pipe': 11 -672.1 4.260 PL 40.86 PF 5.4 FB 163.5 0.0 37.7 0.0 15.1 120 FIG 16.00 PE 0.0 G 163.5 0.0 43.1 0.0 0.094 IL 56.86 PV 1.5 Pipe: 12 -672.1 4.260 PL 12.50 PF 1.8 G 163.5 0.0 43.1 0.0 15.1 120 FIG 6.80 PE 0.0 HI - 163.5 0.0 44.9 0.0 0.094 IL 19.30 PV 1.5 Pipe: 13 -672.1 4.260 PL 1.00 PF 1.6 HI 163.5 0.0 44.9 0.0 15.1 120 FIG 16.00 PE 0.4 HB - 162.5 0.0 46.9 0.0 0.094 IL 17.00 PV 1.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 05/15/1998 61638E.SDF JOB TITLE: BEGINNINGS/EAST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 -672.1 4.260 PL 18.29 PF 2.4 HB 162.5 0.0 46.9 0.6 15.1 120 FTG 6.80 PE 0.0 31 162.5 0.0 49.3 0.0 0.094 TL 25.09 PV 1.5 Pipe: 15 -672.1 4.260 PL 1.00 PF 0.7 31 162.5 0.0 49.3 0.0 15.1 .120 FIG 6.80 PE 0.4 JB 161.5 0.0 50.5 0.0 0.094 IL 7.80 PV 1.5 Pipe: 16 -672.1 4.260 PL 100.00 PF 12.6 33 161.5 0.0 50.5 0.0 15.1 120 FIG 34.00 PE 0.0 3 161.5 0.0 '63.1 0.0 0.094 TL 134.00 PV 1.5 Pipe: 16A -672.1 6.357 PL 32.00 PF 0.6 3 161.5 0.0 63.1 0.0 6.8 120 FIG 10.00 PE 0.0 TOR 161.5 0.0 63.6 0.0 0.013 TL 42.00 PV 0.3 Pipe: 17 -672.1 6.357 PL 7.17 PF 0.1 TOR 161.5 0.0 63.6 0.0 6.8 120 FIG ---- PE 3.1 BOR 154.3 H.S. 66.9 100.0 0.013 IL 7.17 PV 0.3 Pipe: 18 . . -772.1 5.890 PL 6.00 PF 0.8 BOR 154.3 H.S. 66.9 100.0 9.1 140 FIG E PE 1.9 K 150.0 0.0 69.5 0.0 0.019 IL 39.86 PV 0.6 Pipe: 19 . -772.1 6.134 PL 46.00 PF 1.3 K 150.0 .0.0 69.5 0.0 8.4 150 FIG TG PE 0.0 L 150.0 0.0 70.8 0.0 0.014 IL 98.69 PV 0.5 Pipe: 20 -772.1 6.134 PL 2.00 PF 0.3 L 150.0 0.0 708 0.0 8.4 150 FIG E PE .0.0 M 150.0 0.0 71.2 0.0 0.014 IL 24.35 .PV 0.5 Pipe: 21 -772.1 5.890 PL 6.50 PF 0.8 M 150.0 0.0 71.2 0.0 9.1 140 FIG E PE -2.8 BFI 156.5 0.0 69.1 0.0 0.019 IL 40.36 PV 0.6 Pipe: 22 FIXED PRESSURE LOSS DEVICE 6F2 156.5 0.0 84.1 0.0 15.0 Psi, 772.1 gpm BF1 156.5 0.0 69.1 0.0 Pipe: 23 -772.1 5.890 PL 6.50 PF 1.4 BF2 156.5 0.0 84.1 0.0 9.1 140 FIG 2E PE 2.8 N 150.0 0.0 88.3 0.0 0.019 IL 74.23 PV 0.6 Pipe: 24 -772.2 6.134 PL 5.00 PF 0.8 N 150.0 0.0 88.3 0.0 8.4 . 150 FTG TG PE 0.0 SRC 150.0 SRCE 89.1 (N/A) 0.014 IL 57.69 PV 0.5 Pipe: 25 -28.7 1.049 PL 15.50 PF 5.4 4. 163.0 5.6 26.2 28.7 10.6 120 FTG 3E PE -1.2 5 165.7 0.0 30.5 0.0 0.253 IL. 21.50 PV 0.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 05/15/1998 61638E.SDF JOB TITLE: BEGINNINGS/EAST COMPLEX PIPE DATA (cont..) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 26 -29.7 1.049 PL 3.69 PF 3.4 6 163.0 5.6 28.2 29.7 11.0 120 FTG 2ET PE -1.2 5 165.7 0.0 30.5 0.0 0.271 IL 12.69 PV 0.8 Pipe: 27 -58.4 1.380 PL 10.44 PF 4.1 5 165.7 0.0 30.5 0.0 12.5 120 FIG I PE 0.1 BT 165.4 0.0 34.7 0.0 0.248 TL 16.44 PV 1.1 Pipe: 28 -119.4 2.067 PL 1.92 PF 1.6 BI 165.4 0.0 34.7 0.0 11.4 120 FTG T PE 0.8 BB 163.5 0.0 '.37.1 0.0 0.130 IL 11.92 PV 0.9 Pipe: 29 -30.1 1.049 PL 12.25 PF 5.1 7 163.0 5.6 28.9 30.1 11.2 120 FIG 3E PE -1.0 8 165.4 0.0 32.9 0.0 0.277 IL 18.25 PV 0.8 Pipe: 30 -30.9 1.049 PL 3,42 PF 3.6 9 163.0 5.6 30.4 30.9 11.5 . 120 FTG 2ET PE -1.0 8 165.4 0.0 32.9 0.0 0.290 IL 12.42 PV 0.9 Pipe: 31 -61.0 1.380 PL 0.56 PF 1.8 8 165.4 0.0 32.9 0.0 13.1 120 FIG I PE 0.0 BT 165.4 0.0 34.7 0.0 0.269 TL 6.56 PV 1.2 Pipe: 32 . -24..0 1.049 PL 17.75 PF 4.7 10 161.0 5.6 18.4 24.0 8.9 120 FTG 4E PE -2.3 11 166.2 0.0 20.8 0.0 0.182 IL 25.75 PV 0.5 Pipe: 33 -24.6 1.049 PL 1.50 PF 2.0 12 165.0 5.6 19.3 24.6 9.1 120 FIG 2ET PE -0.5 11 166.2 0.0 20.8 0.0 0.191 TL 10.50 PV 0.6 Pipe: 34 -48.6 1.380 PL 3.79 PF 1.7 11 166.2 0.0 20.8 0.0 10.4 120 FIG I PE 0.0 13 166.2 0.0 22.5 0.0 0.177 IL 9.79 PV 0.7 Pipe: 35 -25.6 1.049 PL 12.79 PF 3.9 .14 161.0 5.6 20.9 25.6 9.5 120 FIG 3E PE -2.3 13 166.2 0.0 22.5 0.0 0.206 IL 18.79 PV 0.6 Pipe: '36 -74.2 1.610 PL 13.83 PF 2.5 - 13 166.2 0.0 22.5 0.0 11.7 120 FIG ---- PE 0.2 15 165.8 0.0 25.2 0.0 0.183 IL 13.83 PV 0.9 Pipe: 37 -74.2 1.610 PL 5.42 PF 1.0 15 165.8 0.0 25.2 0.0 11.7 120 FIG ---- I€ 0.1 16 - 165.6 0.0 26.3 0.0 0.183 TL 5.42 PV 0.9 Pipe: 38 -25.2 1.049 PL 11.23 PF 4.4. 17 165.0 5.6 20.3 25.2 9.4 120 FTG 3ET . PE -0.3 18 - 165.6 0.0 24.5 0.0 0.200 IL 22.23 PV 0.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 05/15/1998 6163BE..SDF JOB TITLE: BEGINNINGS/EAST COMPLEX PIPE DATA (cont..) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) Hw(c) (Fr) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 39 -27.4 1.049 PL 1.17 PF - 1.7 19 163.0 5.6 23.9 27.4 10.2 120 FIG 3E PE -1.1 18 165.6 0.0 24.5 0.0 0.233 IL 7.17 PV 0.7 Pipe: 40 -52.6 1.380 PL 3.00 PF 1.8 18 165.6 0.0 24.5 0.0 11.3 120 FIG I PE 0.0 16 165.6 0.0 26.3 0.0 0.205 TL 9.00 PV 0.9 Pipe: 41 126.9 1.610 PL 6.77 PF 7.3 16 165.6 0.0 26.3 0.0 20.0 120 FIG T PE 0.1 CT 165.4 0.0 .33.7 0.0 0.493 IL 14.77 PV 2.7 Pipe: 42 -157.4. 2.067 PL 1.92 PF 2.6 CT 165.4 0.0 33.7 0.0 15.0 120 FIG I PE 0.8 CB 163.5 0.0 37.1 0.0 0.217 IL 11.92 PV 1.5 Pipe: 43 -30.5 1.049 PL 10.65 PF 5.0 20 163.0 5.6 29.7 30.5 11.3 120 FTG El PE -1.0 CT 165.4 0.0 33.7 0.0 0.284 TL 17.65 PV 0.9 Pipe: 44 -30.5 1.049 PL 11.13 PF 4.9 21 163.0 5.6 29.6 30.5 11.3 120 FIG 3E PE -1.0 22 165.4 0.0 33.4 0.0 0.283 IL 17.13 PV 0.9 Pipe: 45 -31.1 1.049 PL 3.46 PF 3.7 23 163.0 5.6 30.8 31.1 11.5 120 FIG 2EI PE -1.0- 22 165.4 0.0 33.4 0.0 0.294 IL 12.46 PV 0.9 Pipe: 46 -61.5 1.380 PL 0.57 PF 1.8 22 165.4 0.0 33.4 0.0 13.2 120 FIG I PE 0.0 DT 165.4 0.0 35.2 0.0 0.274 IL 6.57 PV 1.2 Pipe: 47 -61.5 1.610 PL 1.92 PF 1.3 DI 165.4 0.0 35.2 0.0 9.7 120 FTG I PE 0.8 DB 163.5 0.0 37.3 0.0 0.129 IL 9.92 PV 0.6 Pipe: 48 -27.3 1.049 PL 9.25 PF 4.2 24 163.0 5.6 23.7 27.3 10.1 120 FIG 2ET PE -1.4 25 166.3 0.0 26.5 0.0 0.231 IL 18.25 PV 0.7 Pipe: 49 -27.3 1.380 PL 7.00 PF 0.4 25 166.3 0.0 26.5 0.0 5.8 120 FIG ---- PE 0.1 26 166.0 0.0 27.0 0.0 0.061 IL 7.00 PV 0.2 Pipe: 50 -27.3 1.610 PL 1.50 PF 0.0 26 166.0 0.0 27.0 0.0 4.3 120 FTG ---- FE 0.0 27 166.0 0.0 27.1 0.0 0.029 TL 1.50 PV 0.1 Pipe: 51 -25.8 1.049 PL 10.79 PF 3.5 28 165.0 5.6 21.2 25.8 9.6 120 FIG 3E PE -0.4 29 166.0 0.0 24.3 0.0 0.208 IL 16.79 PV 0.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 05/15/1998 6163BE.SDF JOB TITLE: BEGINNINGS/EAST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 52 -26.5. 1.049 PL 1.54 PF 2.3 30 165.0 5.6 22.4 26.5 9.8 120 FIG 2ET PE -0.4 29 166.0 0.0 24.3 0.0 0.219 TL 10.54 PV 0.7 Pipe: 53 -52.3 1.380 PL 4.67 PF 2.8 29 166.0 0.0 24.3 0.0 11.2 120 FIG El PE 0.0 • 27 166.0 0.0 27.1 0.0 0.203 IL 13.67 PV 0.8 Pipe: 54 -79.6 1.610 PL 8.00 PF' 1.7 27 .166.0 0.0 27.1 0.0 12.5 120 FIG ---- PE 0.1 31 165.7 0.0 28.9 0.0 0.208 IL 8.00 PV 1.1 Pipe: 55 -79.6 1.610 PL 7.08 PF 1.5 31 165.7 0.0 28.9 0.0 12.5 120 FIG ---- PE 0.1 32 165.5 0.0 30.4 0.0 0.208 TL 7.08 PV 1.1 Pipe: 56 -29.5 1.049 PL 1.63 PF 2.8 33 165.0 5.6 27.8 29.5 11.0 120 FIG 2ET PE -0.2 32 165.5 0.0 30.4 0.0 0.267 IL 10.63 PV 0.8 Pipe: 57 -109.1 1.610 PL 5.10 PF 4.9 32 165.5 0.0 30.4 0.0 17.2 120 FIG I PE 0.0 ET 165.4 0.0 35.4 0.0 0.373 IL 13.10 PV 2.0 Pipe: 58 -109.1 2.067 PL 1.92 PF 1.3 ET 165.4 0.0 35.4 0.0 10.4 120 FIG T PE 0.8 EB 163.5 0.0 37.5 0.0 0.110 IL 11.92 PV 0.7 Pipe: 59 -25.5 1.049 PL 10.83 PF .34 34 161.0 5.6 20.7 25.5 9.5 120 FIG 3E PE -2.3 35 166.3 0.0 21.8 0.0 0.203 IL 16.83 PV 0.6 Pipe: 60 . -25.4 1 .049 PL 3.92 PF 2.6 36 163.0 5.6 20.6 25.4 9.4 120 FTG 2ET PE -1.4 35 166.3 0.0 21.8 0.0 0.203 IL 12.92 PV 0.6 Pipe: 61 -50.9 1.380 PL 8.17 PF 1.6 35 166.3 0.0 21.8 0.0 10.9 120 FIG --- PE 0.1 37 166.0 0.0 23.5 0.0 0.193 IL 8.17 PV 0.8 Pipe: 62 -26.1 1.049 PL 1.33 PF 2.2 - 38 165.0 5.6 21.7 26.1 9.7 120 FTG 2ET PE _04 37 166.0 0.0 23.5 0.0 0.213 IL 10.33 PV 0.6 Pipe: 63 -77.0 1.610 PL 12.58 PF 4.0 37 166.0 0.0 23.5 0.0 12.1 120 FIG 2E RE 0.1 39 - 165.7 0.0 27.7. 0.0 0.196 TL 20.58 PV 1.0 Pipe: 64 -28.3 1.049 PL 1.21 PF 2.5 40 165.0 5.6 25.5 283 10.5 120 FTG 2ET PE -0.3 39 - 165.7 . 0,0 27.7 0.0 0.247 IL 10.21 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 Date: 05/15/1998 61638E.SDF JOB TITLE: BEGINNINGS/EAST COMPLEX PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI )(GPM) F.L./FT (PSI) Pipe: 65 -165..3 1.610 PL 9.87 PF 6.2 39 165.7 0.0 27.7 0.0 16.6 120 FTG T PE 0.1 FT 165.4 0.0 34.0 0.0 0.349 IL 17.87 PV'. 1.9 Pipe: 66 -165..8 2.067 PL 1.92 PF 2.9 FT 165.4 0.0 34.0 0.0 15.9 120 FIG I PE 0.8 FB 163.5 0.0 37.7 0.0 0.240 IL 11.92 PV 1.7 Pipe: 67 -30.0 1.049 PL 10.94 PF 4.7 41 163.0 5.6 28.7 30.0 11.1 120 FIG 3E PE -1.0 42 165.4 O.Q. i32.3 0.0 0.275 IL 16.94 PV 0.8 Pipe: 68 -30.6 1.049 PL 3.27 PF 3.5 43 163.0 5.6 29.8 30.6 11.4 120 FIG 2E1 PE -1.0 42 165.4 0.0 32.3 0.0 0.285 TL 12.27 PV 0.9 Pipe: 69 -60.6 1.380 PL 0.57 PF 1.7 42 165.4 0.0 32.3 0.0 13.0 120 FIG T PE 0.0 FT 165.4 0.0 34.0 0.0 0.266 IL 6.57 PV. 1.1 NOTES: (1) Calculations were performed by the HASS 6.2.0 computer program under license no. 4 C1288D granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 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 0.127 gpm. velocity pressures are printed for information, only, and are not used in balancing the system. Maximum water velocity is 20.0 ft/sec at pipe 41. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 Date: 05/15/1998 6163BE.SDF JOB TITLE: BEGINNINGS/EAST COMPLEX (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD..PIP PAGE: A MATERIAL: S40 HL4C: 120 Diameter Equivalent Fitting Lengths in Feet (in) E I L C B G A D Eli Tee LngEll ChkViv -------------------------------------------------------- BfyVlv GatVlv AimChFc DPVlv NPTee 1.049 2.00 5.00 200 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 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: * MATERIAL: S40 HI4C: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee LngEli ChkViv BfyVlv GatVlv AimChk DPViv 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 13.17 5.890 25.46 53.04 16.97 57.29 19.10 4.24 44.56 31.83 6.134 14.79 31.70 9.51 33.81 10.57 3.17 29.59 20.08 6.357 17.60 37.72 11,32 40.23 12.57 3.77 35.21 23.89 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 Date: 05/15/1998 6163BE..SDF JOB TITLE: BEGINNINGS/EAST COMPLEX WATER SUPPLY CURVE 108+ 99*\\\\\ \\\\\ 90+ X \\\\\ \\\\\ \\\\\ 81+ \\\\\ \\\\\ 75.6 psi. © 3545 9pm-> * Flow Test Point P72+ R E S S63+ U R E 54+ ( I P S I 45+ ) 36+ 27+ 18+ LEGEND I II X = Required Water Supply I' • 89.11 psi © 9222 gpm 9+ 1 0 = Available Water Supply 96.24 Psi © 922.2 gpm I II o -------------------------------------------------------- --------+ 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) ..ø3/86/998 15:38 213-724-5227 DELCO SALES PAGE 82 - Si'Vies 909RPOA.., ROduced Pressureir POtector. MOM bi Y`?'I . Sizes: 21/2", 3"4" 6",8", 10 64, 76, 100, 150,200,250mm Series 909RPDA are designed exclusively for use in accordance with water hilly authority containment requirements. It is mandatory to preven the reverse flow QfJjre protection system subtancss. I.e., glyceri wetting agents, stagnant water and water of non-potable quality from being pumped orsiphofled into the potable water line. BENEF IS: Detects leaks ... with emphasis on the cost of unaccount-able w Icr: Incorporates a meter which allow the water utility to: is Detept leaks that historically create great annual cost due to waste. It prvldes a detection point for unauthorized use. It can help locate i11e taps. Mod ulr check design concept facilitates maintenance and assembly ac- cess. i sizes are standardiy equipped with AWWA epoxy coated, UL/ FM listed OS&Y. resilient seated gate valves, CFM (cubic feet per minute) or GPM (gallon per minute) meter and bail type test cocks. A pressure differertiai relief vale is located in a zone between the chick valves. - .. Featur4 a modular design concept which facilitates maintenance and assembly access. All sizes are siandardly equipped with gate valves and ball type test cocks. Bad,, construction fused epoxy Coated cast iron RepaceabIe bronze seats Mom mum flow at low pressure drop Con pact for economy combined with performance Design simplicity for easy maintenance Punished with %x%(116 x 19mm) recordall meter Mo4I 25, bronze NO SPECIAL TOOLS REQUIRED with outside stem & yoke resilient seated gate valves - with cubic feet per minute meter - with gallons per minute meter less gate valves (4'. 10')(100-250mm) A Redu ed Pressure Detector Check Valve/Backf low Preventer shall be installe on fire protection systems when connected to a public water supply. Degree of hazard present Is determined by the local authority having urisdiction. The unit shall b a completó sS8mbly Including UL lisle OS&Y shutoff valves with FM approval. Including an auxiliary line co sisting of an approved backflow preventer and water meter. The as embly shall meet the requirements 01 ASSE No. 1047; AWWA C511-9 : (IL Classified File No. EX3185: CSA B64 and USC Manual 8th. Edition. Watts Regulator Co. Series 909RPDA. 9O9RPDAOsy Check Any. Pipe Line Relief Valve Seat Relief Valve Piston Relief Valve Piston Any. Wiper Seal Relief Volvo Bottom Plug Body Flange Spring Alloy. HOW IT OPERATU The unique relief valve construction incorporates two channel.: one for air, one for water. When the relief vale opens. as In the accompanying air-Wwater-Out diagram, the right-hand channel admits air to the to of the reduced pressure zone. to-loving the zone vacuum. The chin- net on the left than drains the zone to atmosPhere. Therslore. If both check valves foul, and simuhansous negative supply and positive back pressure devaieM. the relief valve Water Air uses the aIr-Sri/water-out p1ncIpie to Patent p4,241.752 Out In atop potential backilow. Now Available, - WattsBox Insulated Enclosures. For more information, send for ES-W8 or ES-WB-T. A LS4DSR FM VALVf ?MCHMOLOGP' WATS REGULATOR SI'%c. s7 Wattslriduatfieg.inc,. Water Products Division • Safety a Control Valves r I rjj/ab/1tNW 1b:30 213-724-5227 Size 2%' to 10 ( 64.250mm) have epoxy coated cast iron body, bronze seat and disc holder stainless steel trim and durable tight-seating rubber check valve discs. All sizes furnished with bron2e body ball valve test cocks. Furnished with out- side stem and yoke (OS&Y) gate valves UL/FM listed. No, 909RPDA bypass line unit consists of an approved No. 909 reduced pressure backliow proven- ter assembly and CFM ½ z VA (16 a 19mm) water meter. STANDARDS ASSE No. 1047: AWWA C511-92; CSA 864 UL Classified File No. 6X31 85; UIJFM. USC Manual for Cross-connection Control, em edition APPROVALS ASSE; UIIFM Approved by the foundation for Cross-Connection Control and Hydraulic Research at the University of Southern California. PRESSURE - TEMPERATURE - Sizes 2W through 10' (64-250mm) are suitable for supply pressures up to 175 Psi (12.1 bars) and water temperatures to 1407 (60C) maximum. DELCO SALES Series 909AG I AIR GAPS 8 When installing a drain line, use I Series 909 air gaps on No. 909 back- flow preveiflers. IWL Air Gap Dimensions tee left For N.. Drain Outlet Dimmmlens No. 881 SIan Silo A 1 I W.iØt ____ In. mm Ii.mmIii.mm in. mm lbs. k91. 90MG-F 2½.3 64.78 2 1 51 4% 111 639 172 3.3 1.5 989A9-K 4-5 102-152 3 79 We J 160 We 243 83 2.8 901)AG-M 8-10 1 203-254 4 102 794. 198 11% 288 15.5 7.0 *Epoxy coated / NOTE: Piping for 3 909 will start from 01 gate and connect at 42 check valve. A (9090S&Y, 9O9NRS) Size A C 0 Di E. Es F. Pt 0 L T Ti '- Ia. mm Ia. mm In. mm In. mm In. mm In. mm In. mm In. mm Ia. mm in. mm ID. mm In. mm lbr. kgu. 2½,3 64,76 421A 6½ 133 4½ 12 305 8 203 7 178 26% 684 14 356 9 229 7% 194 20 104 4 102 55½ 1400 23% 603 6 152 5% 149 17 432 9 229 9½ 241 37 940 15 391 13% 345 11~ 299 up 213 6 1 152 I 65½ 1664 1 1070 118%1 470 32% 826 6 152 1 6 1 114 152 20% 527 10½ 267 14½ 368 44VS 1130 16 406 1339 346 11 V4 299 798 362 8 203 79',. 1988 39'/. 997 W. 249 61i 219 26 660 11½ 292 16½ 470 55V. 1403 17 432 18½ 470 16% 416 146 660 10 254 93% 2378 49 1219 9~ 248 8% 219 32 913 13 330 21½ 546 67½ 1715 18 457 18½ 470 16% 418 2230 1012 2 U 03/06/ 998 15:30 213-724-5227 DELCO SALES PAGE 04 CAPACITY Typical maximum flow rate (7.5 feet/sec.) bats psi 'A" 909RPDA * bars p$ " 909RPDA 2.1 39 1.7 26 IA 20 ! Li H I LII .HJJ W go o 2 40 SI 10 100 120 140 160 110 200. 220 240 GPM 0 30 60 30 120 150 180 210 240 270 300 330 350 GPM 0 76 152 221 304 380 455 532 506 184 760 535 012 LPM 0 114 221 342 456 $70 684 708 612 1221 tIll 12501301 LPM S 7.5- 10 ii FP* - S 7.5 10 15 FPS 1.8 2.3 3.0 di MPS. 1.5 2.3 3.0 4.1 Nfl bats pal 4" 909RPDA * 14.!I54.4JfJ IfH I 60 100 150 200 210 300 310 400 450 500 550 500 GPM o 100 310 570 760 160 1140 1330 1520 1711.10 2000 2210 LPM 5 75 10 15 FPS 1.5 2.3 3.0 dIMPS ISIS psi 6U909RPDA a 2.130 -- 1.72$ 1.420 - 1.016 .710 .3 $ -- 00 -- $ 200 400 600 800 1000 1200- 14001600 GPM 0 760 1520 2280 3040 3500 4550 5320 6080 LPM 5 7.5 10 15 FPS 1.5 2.3 3.0 4.6 Nfl -;bars psi 8' OOORPDAMI * bar3 psi 10" 909RPDAMI 0 OL-'- 0 111 , 0 200 400 800 800 1000 1200 1400 1600 1100 2000 GPM I 250 500 750 1000 1050 1281 1750 SIll 2230 0500 2750 3000 GPM 0 760 1520 2280 3040 3800 4580 5320 6080 $8407440 LPM 0 650 1500 2150 3500 1750 5700 050 71a0 051 asco iose ii501 LPM 5 7.1 10 15 FPS 5 7.5 10 FPS 1.5 2.3 3.0 . 4.6 MPS 1.5 . 23 - 3.0 MPS Watts p pduct specifications In U.S. customary units and metric are approximate and are provided for reference only. For precise measurements. please contact Watts Technical Service. Watts reserves the right to change or-modify product design. construction. specifications, or materials with- out prioTlzlotice and without incurring any obligation to make such changes and modifications on Watts products previously or subsequently sold. 3 COSCO FIRE PROTECTION, INC. 321 EAST GARDENA BOULE ___ GARDENA, CA. 90247 pjS BROS. CONSTRUCTION HYDRAULIC CALCULATIONS SUBMITTAL NO. FOR: SECTION NO.4 - BEGINNINGS/EAST COMPLEX REVIEWED FOR GENERAL ONE LEGO DRIVE CONFORMNCEB'1'__" - CARLSBAD, CA. FILE NUMBER: 6163BE1 DATE: 22 JULY, 1998 CALCULATED AREA: 1500 S -DESIGN DATA- OCCUPANCY CLASSIFICATION: ORDINARY HAZARD II DENSITY: .20 GPM/SQ FT.. AREA OF APPLICATION: 1500 SQ. FT. COVERAGE PER SPRINKLER: 130.0 SQ.FT. [MAX.] NUMBER OF SPRINKLERS CALCULATED: 14 SPRINKLERS FLOW AND PRESSURE (@ BOR): 508.1 GPM © 58.1 PSI FLOW AND PRESSURE (© SOURCE) 658.2 GPM © 62.5 SPRINKLER ORIFICE SIZE: 1/2 inch(K=5.6) NAME OF CONTRACTOR: COSCO FIRE PROTECTION,. INC. DESIGN/LAYOUT BY: K.DAVIS AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD AND SCHIRMER ENGR. CONTRACTOR CERTIFICATION NUMBER: C16-577621 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE 4* 4 C1288D ) HRS SYSTEMS, INC. ATLANTA, GA RFCFJ\Iir - AUG 0 6 1998 13ERNARD$ BROS. INC. Page 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 07/22/1998 JOB TITLE: BEGINNINGS/EAST COMPLEX WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL NODE PRESS. PRESS. © PRESS. © DEMAND TAG (PSI) (PSI) (GPM) (PSI) (GPM) SRC 98.1 75.6 3545..0 97.1 658.2 Page 1 6163BE1 .SDF REQ 'D PRESS. (PSI) 62.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 658.2 GPM 150.0 GPM 100.0 GPM 408.2 GPM NODE TYPE K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 HOSE STREAM SOURCE PRESSURE (PSI) 20.9 22.3 23.7 25.7 29.2 34.6 35.2 37.3 21.0 22.4 23.8 25.8 29.3 34.8 34.1 37.8 42.9 38.0 43.0 44.8 45.5 46.6 47.6 48.3 54.8 58.1 60.3 61.0 61.1 58.7 58.7 62.1 62.5 DISCHARGE (GPM) 25.6 26.5 27.3 28.4 30.2 33.0 33.2 25.7 26.5 27.3 28.4 30.3 33.0 32.7 508.2 NODE ANALYSIS DATA NODE TAG ELEVATION (FT) 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 165.4 163.5 165.4 163.5 163.5 163.5 162.5 162.5 161.5 161.5 154.3 150.0 150.0 150.0 156.5 156.5 150.0 150.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 07/22/1998 61638E1..SDF JOB TITLE: BEGINNINGS/EAST COMPLEX 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 -25.6 1.049 PL 7.00 PF., 1.4 100 165.4 5.6 20.9 25.6 9.5 120 FTG ---- PE 0.0 101 165.4 5.6 22.3 26.5 0.205 TL 7.00 PV 0.6 Pipe: 2 -52.1 1.380 PL 7.00 PF 1.4 101 165.4 5.6 22.3 26.5 11.2 120 FIG ---- PE 0.0 102 165.4 5.6 23.7 27.3 0.201 IL 7.00 PV 0.8 Pipe: 3 -79.4 1.610 PL 9.50 PF 2.0 102 165.4 5.6 23.7 27.3 12.5 120 FTG ---- PE 0.0 103 165.4 5.6 25.7 28.4 0.207 IL 9.50 PV 1.1 Pipe: 4 -107.7 1.610 PL 9.50 PF 3.5 103 165.4 5.6 25,7 28.4 17.0 120 FIG ---- PE 0.0 104 165.4 5.6 29.2 30.2 0.364 IL 9.50 PV 1.9 Pipe: 5 -138.0 1.610 PL 9.50 PF 5.5 104 165.4 5.6 29.2 30.2 21.7 120 FIG ---- PE 0.0 105 165.4 5.6 34.6 33.0 0.576 IL 9.50 PV 3.2 Pipe: 6 -170.9 2.067 PL 2.67 PF 3.2 105 165.4 5.6 34.6 33.0 16.3 120 FIG I PE 0.0 PT 165.4 0.0 37.8 0.0 0.253 TL 12.67 PV 1.8 Pipe: 7 -33.2 1.049 PL 6.25 PF 2.1 106 165.4 5.6 35.2 33.2 12.3 120 FTG ---- PE 0.0 107 165.4 0.0 37.3 0.0 0.333 IL 6.25 PV 1.0 Pipe: 8 -33.2 1.380 PL 0.53 PF 0.6 107 165.4 0.0 37.3 0.0 7.1 120 FIG I PE 0.0 PT 165,4 0.0 37.8 0.0 0.087 IL 6.53 PV 0.3 Pipe: 9 -204.2 2.067 PL 1.92 PF 4.2 PT 165.4 0.0 37.8 0.0 19.5 120 FIG I PE 0.8 PB 163.5 0.0 42.9 0.0 0.352 IL 11.92 PV 2.6 Pipe: 10 -25.7. 1.049 PL 7.00 PF 1.4 108 165.4 5.6 21.0 25.7 9.5 120 FIG ---- PE 0.0 109 165.4 5.6 22.4 26.5 0.206 IL 7.00 PV 0.6 Pipe: 11 -52.2 1.380 PL 7.00 PF 1.4 109 165.4 5.6 22.4 26.5 11.2 120 FTG ---- PE 0.0 110 1654 5.6 23.8 27.3 0.202 IL 7.00 PV 0.8 Pipe: 12 -79.5 1.610 PL 9.50 OF 2.0 110 165.4 5.6 23.8 27.3 12.5 120 FIG ---- PE 0.0 111 165.4 5.6 25.8 28.4 0.208 IL 9.50 PV 1.1 Pipe: 13 -108.0 1.610 PL 9.50 PF 3.5 111 165.4 5.6 25.8 28.4 17.0 120 FTG ---- PE 0.0 112 165.4 5.6 29.3 30.3 0.366 IL 9.50 PV 1.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 07/22/1998 6163BE1..SDF JOB TITLE: BEGINNINGS/EAST COMPLEX 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: 13A -138.3 1.610 PL 9.50 PF. 5.5 112 165.4 5.6 29.3 30.3 21.8 120 FTG ---- PE 0.0 113 165.4 5.6 34.8 33.0 0.578 TL 9.50 PV 3.2 Pipe: 13B -171.3 2.067 PL 2.67 PF 3.2 113 165.4 5.6 34.8 33.0 16.4 120 FIG I PE 0.0 QT 165.4 0.0 38.0 0.0 0.254 TL 12.67 PV 1.8 Pipe: 13C -32.7 1.049 PL 7.13 PF 3.9 114 165.4 5.6 34.1 32.7 12.1 120 FTG I PE 0.0 01 165.4 0.0 38.0 0.0 0.323 IL 12.13 PV 1.0 Pipe: 13D -204.0 2.067 PL 1.92 PF 4.2 01 165.4 0.0 38.0 0.0 19.5 120 FIG I PE 0.8 QB 163.5 0.0 43.0 0.0 0.351 TL 11.92 PV 2.6 Pipe: 13D1 -204.2 4.260 PL 13.46 PF 0.1 PB 163.5 0.0 42.9 0.0 4.6 120 FTG ---- PE 0.0 08 163.5 0.0 43.0 0.0 0.010 IL 13.46 PV 0.1 Pipe: 13E -408.1 4.260 PL 22.29 PF 1.8 08 163.5 0.0 43.0 0.0 9.2 120 FIG I PE 0.0 G 163.5 0.0 44.8 0.0 0.037 TL 48.62 PV 0.6 Pipe: 13F -408.1 4.260 PL 12.50 PF 0.7 G 163.5 0.0 44.8 0.0 9.2 120 FIG 6.80 PE 0.0 HI 163.5 0.0 45.5 0.0 0.037 IL 19.30 PV 0.6 Pipe: 13G -408.1 4.260 PL 1.00 PF 0.6 HI 163.5 0.0 45.5 0.0 9.2 120 FTG 16.00 PE 0.4 HB 162.5 0.0 46.6 0.0 0.037 TL 17.00 PV 0.6 Pipe: 14 -408.1 4.260 PL 18.29 PF 0.9 HB 162.5 0.0 46.6 0.0 9.2 120 FIG 6.80 PE 0.0 .31 162.5 0.0 47.6 0.0 0.037 IL 25.09 PV 0.6 Pipe: 15 -408.1 4.260 PL 1.00 PF 0.3 31 162.5 0.0 47.6 0.0 9.2 120 FIG 6.80 PE 0.4 38 161.5 0.0 48.3 0.0 0.037 TL 7.80 PV 0.6 Pipe: 16 -408.1 4.260 PL 132.08 PF 6.5 38 161.5 0.0 48.3 0.0 9.2 120 FIG 40.80 PE 0.0 TOR 161.5 0.0 54.8 0.0 0.037 IL 172.88 PV 0.6 Pipe: 17 -408.1 4.260 PL 7.17 OF 0.3 TOR 161.5 0.0 54.8 0.0 9.2 120 FIG ---- PE 3.1 BOR 154.3 H.S. 58.1 100.0 0.037 TL 7.17 PV 0.6 Pipe: 18 -508.1 5.890 PL 6.00 PF 0.3 BOR 154.3 H.S. 58.1 100.0 6.0 140 FTG E PE 1.9 K 150.0 0.0 60.3 0.0 0.009 TL 39.86 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 07/22/1998 JOB TITLE: BEGINNINGS/EAST COMPLEX PIPE DATA (cont..) Page 4 6163BE1 .SDF 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: 19 -508.1 6.134 PL 46.00 PF. 0.6 K 150.0 0.0 60.3 0.0 5.5 150 FTG TG PE 0.0 L 150.0 0.0 61.0 0.0 0.006 IL 98.69 PV 0.2 Pipe: 20 -508.1 6.134 PL 2.00 PF 0.2 L 150.0 0.0 61.0 0.0 5.5 150 FTG E PE 0.0 M 150.0 0.0 61.1 0.0 0.006 TL 24.35 PV 0.2 Pipe: 21 -508.1 5.890 PL 6.50 PF 0.4 M 150.0 0.0 61.1 0.0 6.0 140 FTG E PE -2.8 BF1 156.5 0.0 58.7 0.0 .0.009 IL 40.36 PV 0.2 Pipe: 22 508.1 5.890 PL 1.00 PF 0.0 BF2 156.5 0.0 58.7 0.0 6.0 120 FIG ---- PE 0.0 BF1 156.5 0.0 58.7 0.0 0.012 TL 1.00 PV 0.2 Pipe: 23 -508.1 5.890 PL 6.50 PF 0.6 BF2 156.5 0.0 58.7 0.0 6.0 140 FTG 2E PE 2.8 N 150.0 0.0 62.1 0.0 0.009 IL 74.23 PV 0.2 Pipe: 24 -508.2 6.134 PL 5.00 PF 0.4 N 150.0 0.0 62.1 0.0 5.5 150 FIG TG PE 0.0 SRC 150.0 SRCE 62.5 (N/A) 0.006 TL 57.69 PV 0.2 NOTES: (i) Calculations were performed by the HASS 6.2.0 computer program under license no. 4 C1288D granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 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 0.056 gpm. Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 21.8 ft/sec at pipe 13A. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 07/22/1998 61638E1.SDF JOB TITLE: BEGINNINGS/EAST COMPLEX (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E I L C B G A D Eli Tee LngEli ChkViv BfyVlv GatVlv A1mChk DPViv -------------------------------------------------------- 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 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: * MATERIAL: S40 HL4C: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee LngEll ChkVlv BfyVlv GatViv A1mChk DPViv 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 13.17 5.890 25.46 .53.04 16.97 57.29 19.10 4.24 44.56 31.83 6.134 14.79 31.70 9.51 33.81 10.57 3.17 29.59 20.08 ..,. 3 . SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 07/22/1998 . . .'. 61638E1.SDF JOB TITLE: -BEGINNINGS/EAST COMPLEX WATER SUPPLY CURVE 108+ 99*\\\\\ 10 \\\\\ \\\\\ 90+ \\\\\ 81+ \\\\\ \\\\\ 75.6 psi © 3545 gpm-> * Flow Test Point P72+ R E 1 S 563+X U: R E 54+ I I ¼ S 145+ ) 36+ 27+ 18+ LEGEND I II • lx = Required Water Supply 62.50 psi © 658.2 gpm U 9+ it 1 0 = Available Water Supply If 97.10 Psi © 658.2 gpm 0++----------+-----+ ------- + -------- + -------- + --------- +------------ 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) First rhmoir Mod ib: Jod 213-724-5227 DELCO SALES PAGE 02 ES-9O9RPOA Sp,mes 909.RPDA ROduced Pressure Ptector. Assembly%.. io Siz 7641 : 2½u, 3", 4", 6", 8", lOU 76, 100, 150,200, .25Qmm Series I909RPDA are designed exclusively for use in accordance with water (itility authority containment requirements. It is mandatory to prevent the reverse flow ojjjre protection system subtances. I.e. , glycerili wetting agents, stagnant water and water of non-potable quality from being pumped or siphoed into the potable water line. BENEF IS: Detects leaks ... with emphasis on the cost of unaccount-able wter: Incorporates a meter which allow the water utility to: Deteft leaks that historically create great annual cost dueto waste. It provides a detection point for unauthorized use. It can help locate illegal taps. Moøulr check design concept facilitates maintenance and assembly ac- cess. Al sizes are standardly equipped with AWWA epoxy coated, UL/ FM listâd OS&Y resilient seated gate valves. CFM (cubic feet per minute) or GPM (gallon per minute) meter and bail type test cocks. A pressure differeitial relief vale is located in a zone between the check valves. Featur* a modular design concept which facilitates maintenance and assemly access. All sizes are standardly equipped with gate valves and bail type test cocks. Bod construction fused epoxy coated cast iron ptacsabic bronze seats '1ixmum flow at low pressure drop rnpact for economy combined with performance Design simplicity for ,y maintenance rtiished with V. x ~ (16 x lamm) recordail meter ModI 25, bronze NO SPECIAL TOOLS REQUIRED Sffix: OSY. with outside stem & yoke resilient seated gate valves CM - with cubic feet per minute meter G!M - with gallons per minute meter ILF less gate valves (4- 10)(100•250mm) - A Redu ed Pressure Detector Check Valve/8ack110w Preventer shall be instaile I on fire protection systems when connected to a public water supply. Degree of hazard present is determined by the local authority having urisdiction. The unit shall be a complete ssómbly including UI. liste I OS&Y shutoff valves with FM approval. Induding an auxiliary line coi?sisting of an approved backflow preventer and water meter. The assembly shall meet the requirements of ASSE No. 1047; AWWA C511-92: UL Classified File No. EX3185; CSA 864 and USC Manual 8th. Edition. Watts Regulator Co. Series 90911120A. 9O9RPDAOSY Cheek Assy. Pipe Line Relief Valve Seat Center Relief Valve Piston Relief Valve Piston Auy. Wiper Seal Relief Valve Bottom Plug Body Flings spring Any. NOW IT OPSRATES The unique relief valve construction incorporates two channels: one for air, one for water. When Ill, relief vale opens. as In the accompanying alr.Wwater-out diagram. the right-hand channel admits air to thi lop of the reduced pressure zone, re-lieving thezon. vacuum. The chan-nel on the left then drains the zone to atmosphere. Therefore, if both check valves foul, and simultaneous negative supply and positive back pressure dsvups. the relief valve Water Air uses the alr4Wwater.cul principle to Patent 04,241.752 Out in stop potential backflow. Now Available, WattsBox Insulated Enclosures. For more information, send for ES-WB or ES-WB.T. A &EAD&R IN VALVE TECHNOLOGY - ffil UREGU A OR —9I'ic• $574 Watts industries, Inc.,.. Water Products Division . Safety & Control Valves rw lvii Co S Lili . Fu I DELCO SALES IPPA6E Size 2W to 10' (64.250mm) have epoxy coated cast Iron body. bronze seat and disc holder stainless steel trim and durable, fight-seating rubber check valve discs. All sizes furnished with bronze body ball valve test cocks. Furnished with out-side stem and yoke (OSY) gate valves UL/FM listed. No. 909RPDA bypass line unit consists of an approved No. 909 reduced pressure backilow pro v e n - ter assembly and CFM ',t xV4 (16 xl 9mm) water meter. ASSE No. 1047: AWWA C511.92: CSA 864 UL Classified He No. 6X3185: UI/FM. USC Manual for Cross-connection Control. Silt Edition APPROVALS @L1.W/QFMb-#M..d SSE; UI/FM Approved by the foundation for Cross-Connection Control and Hydra u l i c Research at the University of Southern California. 1:1tuI;1-.II1ftIUJ;T Sizes 2W through 10' (64-250mm) are suitable for supp1y pressures up to 175 PSI (12.1 bars) and water temperatures to 1407 (600C) maximum. 'HAl Series 909AG fl% AIR GAPS When Installing a drain tine, use I .Series 909 air gaps on No. 909 back- flow preventers. .• I Air Gap Dimenslona Iron lady IN Ni. Droll Oullul Dimensions No. 808 Slasa SIts 1 8 WeIght In. mm Ii.__mmIn. ISM Is. mm lot. kz. 909A5-F 214.3 84.78 2 51 4% 111 6% 172 3.3 1.5 90919K 4-6 102-152 3 76 6%. 180 891. 243 6.3 25 909AG-M 8-10 203-25k 4 102 7%. 188 1116 286 15.5 7.0 *Epoxy coated NOTE: Piping for 3 809 will start from #1 gate Va ve and connect at 52 check valve. I .0 f I Eii E LH A (9090S&Y, QOVNRS) C Open Dimseilon. -. Size A C 0 Di E.Ei F. 0 L - a T T In. mm Iii. mm in. mm In. mm In. mm in. mm In. m m I i i . m m I n . m m I i . I m m I n . I m m i n . I m m l b . . I k g i . 214.3 64.76 42½ 1070 18½ 470 6V4 1T 4%'i 114 12 305 8 1 330 203 7 178 2614 664 14 356 9 229 7% 194 230 104 4 102 55½ 1400 23% 603 8 152 5% 149 17 432 9 229 9½ 241 37 910 15 381 1314 316 11~ 299 47.0 213 6 152 6514 1664 32½ 826 6 152 6 152 20~ 527 1014 287 14½ 368 44½ 1130 16 406 1314 346 11% 299 798 352 8 203 78'/. 1985 3gv 997 9~ 248 894 219 26 6 6 0 1 1 1 4 292 18½ (70 5514 1403 1? 432 1814 470 16% 416 1456 650 10 254 93% 2378 40 1219 9½ 248 8% 219 32 013 13 2114 546 8714 1715 18 457 10141470 16V. 418 2230 1012 U bars sal 311 9OQRPDA . MKIPIROMMMOMMOMMOR a • 40 60 10 100 120 140 150 (I 160 200.220 240 GPM a a so so 90 120 150 180 210 240 270 300 330360 GPM 152 221 304 310 456 532 605 864 760 136 612 1PM 0 114 225 342 458 $70 664 796 612 iou ilio 12641361 1PM 6 7;6- 10 16 FPS . 5 7.5 10 15 FPS 18 2.3 3.0 4.9 MPS 1.5 2.3 3.0 4.5 MPS Borg psi 909RPDA 2.1 1.7 1.4 1.0 .7 .3 0 0 20' 76, UU 11 I1W!I_ 144-j44f D1.LCO SALES PAGE 84 CAPACITY lypical maximum flow rate (7.5 feat/aec.) bars psi 4" 909RPDA * 2.1 30 1.7 25 1.4 20 1.0 15 ______ fJ FI H H .710 : 0 50 100 150 200 260 300 360 400 460 500 $60 500 GPM 0 190 $50 870 700 960 1140 1330 1520 1115 IM 2090 2510 LPM 5 7.5 10 15 FPS 1.5 2.3 3.0 4.6 MPS barn pal 2.1 30 6U909RPDA C l.7251-1- 1.420 1.0 16 _fliHHW .710 0 200 400 630 . 600 1000 1200- 1400 1600 GPM 0 760 1520 2250 3040 3800 4650 $320 6060 LPN 5 7.5 10 15 FPS 1.5 2.3 3.0 4.6 MPS bars psi 2.130 1.7 25 1.4 20 1.0 15 .7 10 .3 5 00 * -bars psi Iu' 909RPDAM1 * I F t 1 1IIVØ4mI.I4 H i LI tH H 0 200 400 600 800 1000 1200 1400 1600 1500 2000 GPM 0 250 500 760 taos 1250 1505 nsa toss nsa asol zisc sass GPM 760 1520 2280 3040 3600 4580 5320 6080 8840 7500 1PM 0 950 IXO 2550 3100 1150 1700 1116'7500 1550 9500 15119 15105 1PM Watts product specifications In U.S. customary units and metric are approximat e a n d a r e p r o v i d e d f o r r e f e r e n c e o n l y . F o r p r e c i s e m e a s u r e m e n t s . please contact Watts Technical Service. Watts reserves the right to change or modify product design, construction. specifications, or m a t e r i a l s w i t h -out prior, notice and without incurring any obligation to make such chang e s a n d m o d i f i c a t i o n s o n W a t t s p r o d u c t s p r e v i o u s l y o r s u b s e q u e n t l y s o l d . all - ------- COSCO FIRE PROTECTION, INC. 321 EAST GARDENA BOULEVARD GARDENA, CA 90247 BERNDS BROS. CONSTRUCTION 0 17 C CALCULATIONS SUBMAL NO.._ SECTION NO. $22-- koR r4ED FOR GEkL fr" BYLAND '4nIMTION TH DATE LAC6163N 5-20-98 -DESIGN DATA- OCCUPANCY CLASSIFICATION: ORDINARY GP. 2 DENSITY: .20 gpm/sq. ft. AREA OF APPLICATION: 1500S F COVERAGE PER SPRINKLER: 121 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 20 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 524. gpm TOTAL WATER REQUIRED (including hose): 774. gpm FLOW AND PRESSURE (@ BOR): 62O gpm @ 44.5 psi SPRINKLER ORIFICE SIZE: .5 inch NAME OF CONTRACTOR: COSCO FIRE PROTECTION DESIGN/LAYOUT BY: JEFF H. AUTHORITY HAVING JURISDICTION: SCHIRMER ENGR. CORP. \ CITY OF CARLSBAD CONTRACTOR CERTIFICATION NUMBER: C16-577621 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 4 C1288D ) HRS SYSTEMS, INC. ATLANTA, GA 11 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 05/19/1998 LAC6163N.SDF JOB TITLE: LEGOLAND / IMAGINATION / NORTH WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ 'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 98.1 75.6 3545.0 96.8 774.5 91.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 774.5 GPM 150.0 GPM 100.0 GPM 524.5 GPM a NODE TYPE K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.38 K= 5.38 K= 5.38 K= 5.38 K= 5.38 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 K= 5.60 HOSE STREAM SOURCE PRESSURE (PSI) 19.7 20.0 21.6 23.2 25.2 19.7 20.0 21.6 23.2 25.4 20.2 20.5 22.0 23.6 25.5 20.7 21.2 23T.1 -. - 25.7 26.2 26.1 28.1 26.2 28.1 26.4 28.3 26.5 28.5 38.8 44 .5 68.9 75.7 90.7 91.9 DISCHARGE (GPM) 24 .8 25.0 26.0 27.0 28.1 24 .9 25.1 26.0 27.0 27.1 24.2 24.4 25.3 26.]. 28.3 25.5 25.8 26.9 28.4 28.7 100.0 624.5 NODE ANALYSIS DATA NODE TAG ELEVATION (FT) 1 178.3 2 178.3 3 178.3 4 178.3 5 178.3 6 178.3 7 178.3 8 178.3 9 178.3 10 178.3 11 178.3 12 178.3 13 178.3 14 178.3 15 178.3 16 178.3 17 178.3 18 178.3 19 178.3 20 178.3 A 178.3 Al 177.5 B 178.3 Bi 177.5 C 178.3 Cl 177.5 D 178.3 Dl 177.5 TOR 177.5 BOR 167 .5 E 160.0 BF1 150 .0 BF2 150.0 SRC 150.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 05/19/1998 LAC6163N.SDF JOB TITLE: LEGOLAND / IMAGINATION / NORTH 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 -24.8 1.380 PL 6.41. PF 0.3 1 178.3 5.6 19.7 24.8 5.3 120 FTG ---- PE 0.0 2 178.3 5.6 20.0 25.0 0.051 TL 6.41 PV 0.2 Pipe: 2 -49.9 1.380 PL 8.50 PF 1.6 2 178.3 5.6 20.0 25.0 10.7 120 FTG ---- PE 0.0 3 178.3 5.6 21.6 26.0 0.185 TL 8.50 PV 0.8 Pipe: 3 -75.9 1.610 PL 8.50 PF 1.6 3 178.3 5.6 21.6 26.0 12.0 120 FTG ---- PE 0.0 4 178.3 5.6 23.2 27.0 0.190 TL 8.50 PV 1.0 Pipe: 4 -102.8 1.610 PL 0.75 PF 2.9 4 178.3 5.6 23.2 27.0 16.2 120 FTG T PE 0.0 A 178.3 0.0 26.1 0.0 0,334 TL 8.75 PV 1.8 Pipe: 5 -28.1 1.380 PL 7.66 PF 0.9 5 178.3 5.6 25.2 28.1 6.0 120 FTG T PE 0.0 A 178.3 0.0 26.1 0.0 0.064 TL 13.66 PV 0.2 Pipe: 6 -130.9 2.067 PL 0.50 PF 1.6 A 178.3 0.0 26.1 0.0 12.5 120 FTG T PE 0.3 Al 177.5 0.0 28.1 0.0 0.155 TL 10.50 PV 1.1 Pipe: 7 -130.9 4.260 PL 11.75 PF 0.1 Al 177.5 0.0 28.1 0.0 2.9 120 FTG ---- PE 0.0 Bi 177.5 0.0 28.1 0.0 0.005 TL 11.75 PV 0.1 Pipe: 8 -24.9 1.380 PL 6.41 PF 0.3 6 178.3 5.6 19.7 24.9 5.3 120 FTG ---- PE 0.0 7 178.3 5.6 20.0 25.1 0.051 TL 6.41 PV 0.2 Pipe: 9 -49.9 1.380 PL 8.50 PF 1.6 7 178.3 5.6 20.0 25.1 10.7 120 FTG ---- PE 0.0 8 178.3 5.6 21.6 26.0 0.186TL 8.50 PV 0.8 Pipe: 10 -76.0 1.610 PL 8.50 PF 1.6 8 178.3 5.6 21.6 26.0 12.0 120 FTG ---- PE 0.0 9 178.3 5.6 23.2 27.0 0.191 TL 8.50 PV 1.0 Pipe: 11 -103.0 1.610 PL 0.75 PF 2.9 9 178.3 5.6 23.2 27.0 16.2 120 FTG T PE 0.0 B 178.3 0.0 26.2 0.0 0.335 TL 8.75 PV 1.8 Pipe: 12 -27.1 1.380 PL 7.66 PF 0.8 10 178.3 5.4 25.4 27.1 5.8 120 FTG T PE 0.0 B 178.3 0.0 26.2 0.0 0.060 TL 13.66 PV 0.2 Pipe: 13 -130.1 2.067 PL 0.50 PF 1.6 B 178.3 0.0 26.2 0.0 12.4 120 FTG T PE 0.3 B1 177.5 0.0 28.1 0.0 0.153 TL 10.50 PV 1.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 05/19/1998 LAC6163N.SDF JOB TITLE: LEGOLAND / IMAGINATION / NORTH 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 . -261.0 4.260 PL 8.87. PF 0.1 B]. 177.5 0.0 28.1 0.0 5.9 120 FTG ---- PE 0.0 Cl 177.5 0.0 28.3 0.0 0.016 TL 8.87 PV 0.2 Pipe: 15 -24.2 1.380 PL 6.41 'PF 0.3 11 178.3 5.4 20.2 24.2 5.2 120 FTG ---- PE 0.0 12 178.3 5.4 20.5 24.4 0.049 TL 6.41 PV 0.2 Pipe: 16 -48.6 1.380 PL 8.50 PF 1.5 12 178.3 5.4 20.5 24.4 10.4 120 FTG ---- PE 0.0 13 178.3 5.4 22.0 25.3 0.177 TL 8.50 PV 0.7 Pipe: 17 -73.8 1.610 PL 8.50 PF 1.5 13 178.3 5.4 22.0 25.3 11.6 120 FTG ---- PE 0.0 14 178.3 5.4 23.6 26.1 0.181 TL 8.50 PV 0.9 Pipe: 18 -100.0 1.610 PL 0.75 PF 2.8 14 178.3 5.4 23.6 26.1 15.8 120 FTG T PE 0.0 C 178.3 0.0 26.4 0.0 0.317 TL 8.75 PV 1.7 Pipe: 19 -28.3 1.380 PL 7.66 PF 0.9 15 178.3 5.6 25.5 28.3 6.1 120 FTG T PE, 0.0 C 178.3 0.0 26.4 0.0 0.065 TL 13.66 PV 0.2 Pipe: 20 -128.2 2.067 PL 0.50 PF 1.6 C 178.3 0.0 26.4, 0.0 12.3 120 FTG T PE 0.3 Cl 177.5 0.0 28.3 0.0 0.149 TL 10.50 PV 1.0 Pipe: 21 -389.3 4.260 PL 8.00 PF 0.3 Cl 177.5 0.0 28.3 0.0 8.8 120 FTG ---- PE 0.0 Dl 177.5 0.0 28.5 0.0 0.034 TL 8.00 PV 0.5 Pipe: 22 -25.5 1.380 PL 8.90 PF 0.5 16 178.3 5.6 20.7 25.5 5.5 120 FTG ---- PE 0.0 17 178.3 5.6 21.2 25.8 0.054TL 8.90 PV 0.2 Pipe: 23 -51.2 1.380 PL 10.00 PF 1.9 17 178.3 5.6 21.2 25.8 11.0 120 FTG ---- PE 0.0 18 178.3 5.6 23.1 .26.9 0.195 TL 10.00 PV 0.8 Pipe: 24 -78.1 1.610 PL 8.75 PF 3.4 18 178.3 5.6 23.1 26.9 12.3 120 FTG T PE 0.0 D 178.3 0.0 26.5 0.0 0.201 TL 16.75 PV 1.0 Pipe: 25 -28.4 1.380 PL 6.58 PF 0.4 19 178.3 5.6 25.7. 28.4 6.1 120 FTG ---- PE 0.0 20 178.3 5.6 26.2 28.7 0.066 TL 6.58 PV 0.2 Pipe: 26 -57.1 1.380 PL 1.25 PF 0.3 20 178.3 5.6 26.2 28.7 12.2 120 FTG T PE 0.0 D 178.3 0.0 26.5 0.0 0.238 TL 1.25 PV 1.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 05/19/1998 LAC6163N.SDF JOB TITLE: LEGOLAND / IMAGINATION / NORTH 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 -135.2 2.067 PL 0.50. PF 1.7 D 178.3 0.0 26.5 0.0 12.9 120 FTG T PE 0.3 Dl 177.5 0.0 28.5 0.0 0.164 TL 10.50 PV 1.1 Pipe: 28 -524.5 4.260 PL 107.00 PF 10.3 Dl 177.5 0.0 28.5 0.0 11.8 120 FTG 3ET PE 0.0 TOR 177.5 0.0 38.8 0.0 0.060 TL 172.84 PV 0.9 Pipe: 29 -524.5 4.260 PL 10.00 PF 1.4 TOR 177.5 0.0 38.8 0.0 11.8 120 FTG E PE 4.3 BOR 167.5 H.S. 44.5 100.0 0.060 TL 23.17 PV 0.9 Pipe: 30 -624.5 4.266 PL 290.00 PF 21.1 BOR 167.5 H.S. 44.5 100.0 14.0 150 FTG 3ET PE 3.2 E 160.0 0.0 68.9 0.0 0.054 TL 390.17 PV 1.3 Pipe: 31 -624.5 6.134 PL 200.00 PF 2.5 E 160.0 0.0 68.9 0.0 6.8 150 FTG 3E PE 4.3 BF1 150.0 0.0 75.7 0.0 0.009 TL 267.06 PV 0.3 Pipe: 32 FIXED PRESSURE LOSS DEVICE BF2 150.0 0.0 90.7 0.0 15.0 psi, 624.5 gpm BF1 150.0 0.0 75.7 0.0 Pipe: 33 -624.5 6.134 PL 15.00 PF 1.2 BF2 150.0 0.0 90.7. 0.0 6.8 150 FTG 3ETG PE 0.0 SRC 150.0 SRCE 91.9 (N/A) 0.009 TL 134.75 PV 0.3 NOTES: Calculations were performed by the HASS 6.2.0 computer program under license no. 4 C1288D granted by HRS Systems, Inc. 2193 Ranchwood Dr.,-N.E. Atlanta, GA 30345 - 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 0.067 gpm. Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 16.2 ft/sec at pipe 11. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 05/19/1998 LAC6163N.SDF JOB TITLE: LEGOLAND I IMAGINATION / NORTH (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 Eli Tee LngEil ChkViv BfyViv GatVlv AimChk DPVlv --------------------------------------------------------- NPTee 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 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee LngEli ChkVlv BfyVlv GatVlv AlmChk DPV1v -------------------------------------------------------- NPTee 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 13.17 26.33 4.266 13.26 26.52 7.95 29.17 15.91 2.65 26.52 13.26 26.52 6.134 14.79 31.70 9.51 33.81 10.57 3.17 29.59 20.08 31.70 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 05/19/1998 L1AC6163N.SDF JOB TITLE: LEGOLAND / IMAGINATION / NORTH WATER SUPPLY CURVE 108+ 99*\\\\\ 0 \\\\\ \\\\\ x \\\\\ 90+ \\\\\ \\\\\\ \\\\\ 81+ \\\\\ \\\\\ 75.6 psi @ 3545 gpm-> * Flow Test Point P 72+ R E S S 63+ U R E 54 + 36+ I- 18+ LEGEND It I, X = Required Water Supply 91.92 psi @ 774.5 gpm 9+ 0 = Available Water Supply " 96.75 psi © 774.5 gpm 'I 0++_+___+____+-----+ ------+ --------+ --------+ ---------+ -----------+ 8001200 1600 2000 2400 2800 3200 3600 4000 FLOW (GPM) Pipe Lint Relief1 Valve Seat Center Relief Valve Piston Relief Valve I- PIston Auy. F WiperSci Relief lva Body Flange Bottom Plug Spring Aszy, MOW IT OPP.ATU The unique rellet,y&ve construction incorporates two channels: one for sir. on, for water. When the relief vale opens. as in the accompanying air-inlwate v-Out diagram, the right-hand channel admits air to me lop of the reduced pressure zone, to-Roving the zone vacuum. The chan- nel on the left then drains the zone to atmosphere. Therefore, if both check v51v03 tui, and simultaneous negative supply and positive back preuur• developi, the relief valve -. Air uses the alr-ln/water-oul principle to Patent 54.241.752 Out In atop potential backi low. Now Available, Watts Box Insulated Enclosures. For more information, send for ES-WB or ES-WB-T. 'fJ6/1998 15:30 213-724-5227 DELCO SALES PAGE 62 Series 909RPDA Reduced Pressure Detector. Assembly Sizes: 21/2", 311 411, 6", 8", lO 64, 76, 100, 150, 200, 250mm Series 909RPDA are designed exclusively for use in accordanc e w i t h water utility authority containment requirements. it is mandatory to prevent the reverse flow of tire protection system substances, i.e., glycerin Wetting agents, stagnant water and water of non-potable quality from being pumped or siphoned into the potable water line. BENEFITS: Detects leaks . ... with emphasis on the cost of unaccount-able water: incorporates a meter which allow the water utility to: Detect leaks mat historically create great annual cost due to waste. It provides a detection point for unauthorized use. it can help locate illegal taps. Modular check design concept facilitates maintenance and assembly a c - cess. All sizes are standardly equipped with AWWA epoxy coated, 111/ FM listed OS&Y resilient seated gate valves, CFM (cubic feet per minute) or GPM (gallon per minute) meter and bail type test cocks. A press u r e differential relief vale is located in a zone between the check valve s . Features a modular design concept which facilitates maintenance a n d assembly access. All sizes are standardly equipped with gate valves and ball type test cocks. Body construction fused epoxy coated cast Iron Replaceable bronze seats Maximum flow at low pressure drop Compact for economy combined with performance Design simplicity for easy maintenance Furnished with Is x 3/4 (16 x 19mm) racordall meter Model 25, bronze NO SPECIAL TOOLS REQUIRED Suffix: OSY with outside stem & yoke resilient seated gate valves CFM- with cubic feet per minute meter GPM - with gallons per minute meter IF - less gate valves (4- 10)(100•250mm) A Reduced Pressure Detector Check Valve/Backflow Preventer shal l b e installed on fire protection systems when connected to a public wat e r supply. Degree of hazard present is determined by the local au t h o r i t y "........ having jurisdiction. The unit shall be a complete assembly includ i n g UL listed OS&Y shutoff valves with FM approval. Including an auxi l i a r y line consisting of an approved backflow preventer and water m e t e r . Inc assembly shall meet the requirements of ASSE No. 1047; AW W A C511-92: UL Classified File No. EX3185; CSA 864 and USC Ma n u a l Bin. 'Edition. Watts Regulator Co. Series 909RPOA. - :. 1'. ••••_1 First Check Relief Valve Module A econd Check fsy oef A'00~ule Assy. / A £E4DS' FM VALVE rscNwOLecv WATTS 1XVIE-CIULATOR ..,.5l.co 1074 Watts Industries. Iflc, Water Products DivisIon Safety & Control Valves U II I III I I I ! I [I II U UI_I I II • IlI I I _----- bars psi 2.1 30 1.7 25 1.4 20 1.0 15 .7 10 .3 5 00 bars PSI W' n4qprLaIA1 * 1.7 1.4 1,0 .7 .3 0 .!b/1'1 1:30 213-724-5227 DELCO SALES PAGE 84 *Typical maximum flow rate (7.5 feet/sec.) bars j 21/2" 9O9RPDA * bars psi 34 909RPDA • o 20 40 60 80 100 120 140 100 110 200 220 240 GPM 0 30 60 90 120 150 180 210 240 270 300 330360 GPM 0 76 152 221 304 360 456 532 606 684 760 838 012 LPM 0 114 226 342 456 $70 614 796 912 1021 1140 1254 ii LPM 5 7.5 10 16 FPS 5 7.5 10 15 FPS 1.8 2.3 3_0 4.9 MPS 1.5 2.3 3.0 i.5 MPS bars psi 4" 9O9RPDA * + I F1-F !i444. f 1 H 0 60 100 150 200. 250 300 350 400 450 500 560 500 GPM 0 190 360 570 700 960 1140 1330 1520 1710 1900 2060 2280 LPM 5 7.5 10 15 FPS 1.6 2.3 3.0 4.1 MPS bars psi en 909RPDA * 2.1 80 1.7 25 1.4 20 11 15 .7 10 .3 5 00 0 200 400 500 800 1000 1200 1400 1600 GPM 0 760 1520 2280 3040 3800 4660 $320 5080 LPM 5 7.5 10 15 FPS 1.5 2.3 3.0 4.6 MPS 0 200 400 800 600 1000 1200 1400 1600 1800 2000 GP M 0 250 500 750 1000 1250 1500 1750 2000 2250 2500 2750 3000 GPM 0 760 1520 2280 3040 3800 4560 5320 5080 6640 7100 LPM 0 950 1150 2150 3100 0752 0720 1650 7000 1550 9500 10462 11100 LPM 5 7.5 10 15 FPS $ 7.5 10 FPS 1.5 2.3 3.0 4.6 MPS 1.5 2.3 3.0 MPS Waits product specifications in U.S. customary Units and metric are approximate and are provided for reference only. For precis e m e a s u r e m e n t s , please contact Watts Technical Service. Watts reserv e s t h e r i g h t t o c h a n g e o r m o d i f y p r o d u c t d e s i g n , c o n s t r u c t i o n , s p e c i f i c a t i o n s , o r m a t e r i a l s w i t r i - out prior notice and without incurring any obligation to ma k e s u c h c h a n g e s a n d m o d i f i c a t i o n s o n W a t t s p r o d u c t s , p r e v 1 0 u 3 1 y o r s u b s e q u e n t l y s o l d . NOTE: Piping for 3 909 will start from 01 gate valve and connect at 12 check valve, /b/ib 1b:30 213-724-5227 DELCO SALES PAGE @3 Size 2%' to 10 (64.250mm) have epoxy coated cast iron body, bronze seat and disc holder stainless steel trim and durable, tight-seating rubber check valve discs. All sizes furnished with bronze body ball valve test cocks. Furnished with out- side stem and yoke (OSY) gate valves UL/FM listed. No. 909RPDA bypass line unit consists of an approved No. 909 reduced pressure backflow proven- ter assembly and CFM % a V4 (16 xl 9mm) water meter. STANDARDS ASSE No. 1047: AWWA C511.92: CSA 964 UL Classified File No. EX3185; UI/FM. USC Manual for Cross-connection Control, 8th Edition APPROVALS (E; ®dJIF$lIIáIWuPSd ASSE; UL/FM Approved by the foundation for Cross-Connection Control and Hydraulic Research at the University of Southern California. 1iuJ;1-i1i'I:VMI1;1_- Sizes 2½' through 10' (64-250mm) are suitable for supply pressures up to 175 PSI (12.1 bars) and water temperatures to 1401 (60C) maximum. Series 909AG AIR GAPS When Installing a drain tine, use .Series 909 air gaps on No. 909 back- flow preventers. Air Gap Dimensions iron Body - For N.. Drain Oullil Diminsion, No. 90981208 size I A I In, mm weight in. mm In. mm In. I mm lbs. I age. 909AG4 214,3 1 84.76 2 51 4% 111 6M. 172 :3.3 1.5 909A0-i( 4-6 102-152 3 76 6V. 160 83is 243 1 6.3 2.8 909A0-M 8-10 203-25' 4 102 7%e 186 11'h 286 15.5 7.0 poxy 003150 A (9090S&Y, 909NRS) I H- C Open Dimensions SI:. A C P 0: E. E, F. 0 1 N I T Weight In. mm l. I mm in. I mm I in. I mm I in. mm In. I mm In. I mm I In. mm I in. I mm In. I mm In. I mm in. mm lbs. I kgi. 2%,3 64.76 421A 1070 18¼ 470 S'/. 133 4!.', 114 12 305 8 203 7 178 26'/s 864 14 356 9 229 7% 19' 230. 104 4 102 55½ 1400 23% 603 6 152 5% 149 17 432 9 229 914 241 37 940 15 381 13% 346 11% 299 470 213 6 152 65½ 1664 32¼ 826 6 152 6 152 20% 527 10½ 267 14¼ 368 44' .j 1130 16 406 1334346 11% 299 798 352 8 203 78". 1988 39!.'. 997 9% 248 8%219 28 660 11½ 292 18½ 470 551'. 1403 17 432 18½ 470 15% 416 1456 660 10 254_- 93% 2378 48 1219 9% 248 8% 219 32 813 13 330 21½ 548 67¼ 1715 18 457 18% 47016% 415 2230 1012 i