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HomeMy WebLinkAbout2634 GATEWAY RD; ; FPC2018-0027; PermitPERMIT REPORT city of Carlsbad Print Date: 10/18/2021 Permit No: FPC2018-0027 Job Address: 2634 GATEWAY RD, CARLSBAD, CA 92009 Status: Closed - Finaled Permit Type: FIRE-Construction Commercial Work Class: Fire Sprinklers Parcel #: 2132621900 Track #: Applied: 01/24/2018 Valuation: $2,368,710.82 Lot #: Issued: 04/03/2018 Occupancy Group: Project #: DEV12023 Finaled Close Out: 05/26/2021 #of Dwelling Units: Plan #: Bedrooms: Construction Type: Bathrooms: Orig. Plan Check #: Inspector: Plan Check #: Final Inspection: Project Title: UPTOWN BRESSI RANCH Description: SPROUTS FARMERS MARKET -NEW SPRINKLER SYSTEM (459 HEADS) Applicant: FPContractor: CAL-WEST FIRE PROTECTION SPECIALIST CAL-WEST FIRE PROTECTION GONZALO PENA 8361 COMMONWEALTH AVE 8361 COMMONWEALTH AVE BUENA PARK, CA 90621-2525 BUENA PARK, CA 90621-2525 (714) 912-4552 (714) 912-4552 FEE AMOUNT FIRE NFPA 13 System> 100 heads (includes 1 riser) $832.00 FIRE Plan Resub (3rd&Subsequent Submittal/hr) $132.00 Total Fees: $964.00 Total Payments To Date: $964.00 Balance Due: $0.00 Fire Department Page 1 of 1 1635 Faraday Avenue, Carlsbad CA 92008-7314 1 760-602-4665 1 760-602-8561 f I www.carlsbadca.gov A. V. SCHWAN & ASSOCIATES, INC. CONSULTING ENGINEERS b. I 6000 E. Thomas Road, Suite I 4JJ)) Scottsdale, Arizona 85251-7572 JAlE IZ. Phone 602-265-4331 Fax 480-663-1788 STEPHEN A. SCHWAN, P.E., PRESIDENT MO KATEEB, P.E. NATHAN L. KLINE, P.E. March 13, 2018 Dennis Grubb and Associates, LLC Attn: D. Grubb Building Plan Reviewer Project: Sprouts Farme/s Market 2634 Gateway Rd. Carlsbad, CA DGA#:C8043 AVS#: 7077 Carlsbad Permit#: FPC2018-0027 Mr. Grubb, In response to comment #15 per your Fire Sprinkler system review, I received the shop drawings prepared by Fire Protection, sealed by CAL-West Fire Protection (Lic# 870249) and dated 08/17/17. These shop drawings specify a 4 inch main pipe along gridline A and 3 inch pipe along Gridline E. The branches are 1 ¼" pipes. Per note Q on sheet S 1.0, the roof structure is designed to support the loads from sprinkler piping based on a schedule 10 pipe no larger than 6 inches nominal diameter. Therefore, the provided pipes (4 inches and less in diameter) are within the limits of the roof design dead load. Please feel free to contact our office if you have any questions. Best regards, Mo Kateeb, P.E. 6' C70215 CD M rn Exp.090' - - Fire-Protection by Computer Design Cal-West Fire Protection 1113 N Gates St. Santa Ana, Ca. 92703 866-374-9378 Job Name : Sprouts Design Area #1 "Sales Floor" Building Sprouts Farmers Market Location : El Fuerte St. & Gateway Rd. System 1 Contract : 18-010 Data File : Design Area #1 - Sales Floor.WXF Computer Programs by Hydratec Inc. Revision: 50.52.1 / Cal-West Fire Protection Page 1 Sprouts Design Area #1 Sales Floor" Date 1.23.18 HYDRAULIC CALCULATIONS for Project name: Sprouts Design Area #1 Sales Floor" Location: El Fuerte St. & Gateway Rd. Drawing no: Sprouts Farmers Market Date: 1.23.18 Design Remote area number: 1 Remote area location: Sales Floor Occupancy classification: O.H. Grp. 2 Density: .26 - Gpm/SqFt Area of application: 2000-SqFt Coverage per sprinkler: 130 - SqFt Type of sprinklers calculated: SR 8.0K SSU 200 deg. No. of sprinklers calculated: 18 In-rack demand: n/a - GPM Hose streams: 500 - GPM Total water required (including hose streams): 1135.03 -GPM @ 76.18 - Psi Type of system: Wet Grid Volume of dry orpreaction system: n/a - Gal Water supply information Date: 1.11.18 Location: On-Site Source: Carlsbad ED Name of contractor: Cal-West Fire Protection Address: 1113 N Gates St. I /Santa Ana, Ca. 92703 Phone number: 866-374-9378 Name of designer: Cal-West Authority having jurisdiction: Carlsbad FD Notes: (Include peaking information or gridded systems here.) See Peaking Sheets Computer Programs by Hydratec Inc. Revision: 50.52.1 Water Supply Curve C Cal-West Fire Protection Page 2 Sprouts Design Area #1 "Sales Floor" Date 1.23.18 City Water Supply: Demand: Cl - Static Pressure : 116.1 Dl - Elevation : 9.961 C2 - Residual Pressure: 20 D2 - System Flow : 635.04 C2 - Residual Flow : 8000 D2 - System Pressure : 76.182 Hose ( Demand) : 500 D3 - System Demand :1135.04 Safety Margin : 37.325 150 140 130 p120 :1 R 11 E100 S 90 S 80 U7O f ____________ R6° E5° 40 30 C2 20 i11__ 10 . 10002000 3000 4000 5000 6000 7000 8000 9000 FLOW( N"1.85) Computer Programs by Hydratec Inc. Revision: 50.52.1 Fittings Used Summary Cal-West Fire Protection Page 3 Sprouts Design Area #1 Sales Floor" Date 1.23.18 Fitting Legend Abbrev. Name % % 1 1'/ 11/2 2 21h 3 3% 4 5 6 8 10 12 14 16 18 20 24 B NFPA 13 Butterfly Valve 0 0 0 0 0 6 7 10 0 12 9 10 12 19 21 0 0 0 0 0 E NFPA 1390 Standard Elbow 1 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 F NFPA 1345Elbow 1 1 1 1 2 2 3 3 3 4 5 7 9 11 13 17 19 21 24 28 Fsp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow G NFPA 13 Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 S NFPA 13 Swing check o 0 5 7 9 11 14 16 19 22 27 32 45 55 65 T NFPA 139O Flow thruTee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Units Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with * The fittings marked with a * show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a * will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Revision: 50.52.1 Pressure / Flow Summary - STANDARD Cal-West Fire Protection Page 4 Sprouts Design Area #1 Sales Floor' Date 1.23.18 Node No. Elevation K-Fact Pt Actual Pn Flow Actual Density Area Press Req. 1A 20.0 8 20.64 na 36.34 0.26 130 7.0 1 20.0 8 19.57 na 35.39 0.26 130 7.0 IC 20.0 8 19.36 na 35.2 0.26 130 7.0 1D 20.0 8 19.39 na 35.23 0.26 130 7.0 1E 20.0 8 19.98 na 35.76 0.26 130 7.0 1 20.0 8 21.73 na 37.29 0.26 130 7.0 202 20.0 39.16 na 203 20.0 39.24 na 204 20.0 39.43 na 205 20.0 39.81 na 206 20.0 40.22 na 207 20.0 40.66 na 208 20.0 41.12 na 209 20.0 41.62 na 210 20.0 42.16 na 211 20.0 42.73 na 212 20.0 43.35 na 213 20.0 43.95 na 214 20.0 44.45 na 215 20.0 45.05 na 216 20.0 45.78 na TOR 20.0 54.32 na BOR 0.5 73.64 na UG1 -3.0 75.45 na 500.0 UG2 -3.0 75.69 na UG3 -3.0 75.9 na TEST -3.0 76.18 na UG5 -3.0 75.48 na UG6 -3.0 75.57 na 102 20.0 37.17 na 103 20.0 37.21 na 104 20.0 37.47 na 105 20.0 38.13 na 106 20.0 38.7 na 107 20.0 39.2 na 108 20.0 39.63 na 109 20.0 40.0 na 110 20.0 40.3 na 111 20.0 40.56 na 112 20.0 40.75 na 113 20.0 40.88 na 114 20.0 40.94 na 115 20.0 40.97 na 116 20.0 41.01 na 101 20.0 37.21 na 100 20.0 37.21 na 200. 20.0 39.12 na 201 20.0 39.12 na 1G 20.0 8 19.41 na 35.24 0.26 130 7.0 1H 20.0 8 18.17 na 34.11 0.26 130 7.0 11 20.0 8 17.85 na 33.8 0.26 130 7.0 11 20.0 8 17.85 na 33.8 0.26 130 7.0 11K 20.0 8 18.24 na 3416 0.26 130 7.0 IL 20.0 8 19.58 na 35.4 0.26 130 7.0 1M 20.0 8 20.17 na 35.93 0.26 130 7.0 iN 20.0 8 19.38 na 35.22 0.26 130 7.0 10 20.0 8 19.2 na 35.05 0.26 130 7.0 1P 20.0 8 19.25 na 35.1 0.26 130 7.0 10 20.0 8 19.65 na 35.46 0.26 130 7.0 1R 20.0 8 20.9 na 36.57 0.26 130 7.0 The maximum velocity is 16.97 and it occurs in the pipe between nodes 1 and 202 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams Cal-West Fire Protection Page 5 Sprouts Design Area #1 Sales Floor" Date 1.23.18 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C' or Ftrig's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 1A -61.30 1.682 0.0 10.250 20.636 K Factor =8.00 to 120.0 0.0 0.0 0.0 1 -61.3 -0.1037 0.0 10.250 -1.063 Vel = 8.85 1 35.39 1.682 0.0 10.250 19.573 K Factor =8.00 to 120.0 0.0 0.0 0.0 1C -25.91 -0.0211 0.0 10.250 -0.216 Vel= 3.74 1C 35.20 1.682 0.0 10.250 19.357 K Factor =8.00 to 120.0 0.0 0.0 0.0 1D 9.29 0.0031 0.0 10.250 0.032 Vel = 1.34 1D 35.22 1.682 0.0 10.250 19.389 K Factor =8.00 to 120.0 0.0 0.0 0.0 1E 44.51 0.0574 0.0 10.250 0.588 Vel = 6.43 1E 35.76 1.682 0.0 10.250 19.977 K Factor =8.00 to 120.0 0.0 0.0 0.0 1 80.27 0.1707 0.0 10.250 1.750 Vel = 11.59 1 F 37.29 1.682 T 9.9 40.500 21.727 K Factor = 8.00 to 120.0 0.0 9.900 0.0 202 117.56 0.3458 0.0 50.400 17.430 Vel = 16.97 202 45.19 4.26 0.0 11.500 39.157 to 120.0 0.0 0.0 0.0 203 162.75 0.0069 0.0 11.500 0.079 Vel = 3.66 203 104.89 4.26 0.0 11.500 39.236 to 120.0 0.0 0.0 0.0 204 267.64 0.0171 0.0 11.500 0.197 Vel= 6.02 204 113.27 4.26 0.0 11.500 39.433 to 120.0 0.0 0.0 0.0 205 380.91 0.0330 0.0 11.500 0.379 Vel= 8.57 205 17.45 4.26 0.0 11.500 39.812 to 120.0 0.0 0.0 0.0 206 398.36 0.0358 0.0 11.500 0.412 Vel= 8.97 206 16.48 4.26 0.0 11.250 40.224 to 120.0 0.0 0.0 0.0 207 414.84 0.0386 0.0 11.250 0.434 Vel= 9.34 207 16.13 4.26 0.0 11.250 40.658 to 120.0 0.0 0.0 0.0 208 430.97 0.0414 0.0 11.250 0.466 Vel = 9.70 208 16.34 4.26 0.0 11.250 41.124 to 120.0 0.0 0.0 0.0 209 447.31 0.0444 0.0 11.250 0.499 Vel = 10.07 209 17.10 4.26 0.0 11.250 41.623 to 120.0 0.0 0.0 0.0 210 464.41 0.0476 0.0 11.250 0.535 VeI= 10.45 210 18.39 4.26 0.0 11.250 42.158 to 120.0 0.0 0.0 0.0 211 482.8 0.0511 0.0 11.250 0.575 Vel = 10.87 211 20.02 4.26 0.0 11.250 42.733 to 120.0 0.0 0.0 0.0 212 502.82 0.0550 0.0 11.250 0.619 Vel = 11.32 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams Cal-West Fire Protection Page 6 Sprouts Design Area #1 Sales Floor' Date 1.23.18 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 212 22.05 4.26 0.0 10.000 43.352 to 120.0 0.0 0.0 0.0 213 524.87 0.0597 0.0 10.000 0.597 Vel = 11.81 213 24.13 4.26 0.0 7.750 43.949 to 120.0 0.0 0.0 0.0 214 549.0 0.0648 0.0 7.750 0.502 Vel= 12.36 214 25.96 4.26 0.0 8.500 44.451 to 120.0 0.0 0.0 0.0 215 574.96 0.0706 0.0 8.500 0.600 Vel = 12.94 215 28.13 4.26 0.0 9.500 45.051 to 120.0 0.0 0.0 0.0 216 603.09 0.0772 0.0 9.500 0.733 Vel = 13.58 216 31.95 4.26 4E 52.668 48.000 45.784 to 120.0 0.0 52.668 0.0 TOR 635.04 0.0848 0.0 100.668 8.541 Vel = 14.29 TOR 0.0 4.26 Fsp 0.0 0.0 54.325 to 120.0 B 15.8 92.768 11.445 **Fixed Loss .3 BOR 635.04 0.0848 5 28.968 92.768 7.871 Vel = 14.29 BOR 0.0 7.98 G 6.041 53.000 73.641 to 150.0 1 52.855 58.895 1.516 UG1 635.04 0.0026 0.0 111.895 0.295 Vel = 4.07 UG1 18.54 11.65 2F 34.882 500.000 75.452 Qa=500 to 150.0 0.0 34.883 0.0 UG2 653.58 0.0004 0.0 534.883 0.236 Vel = 1.97 UG2 481.46 11.65 0.0 175.000 75.688 to 150.0 0.0 0.0 0.0 UG3 1135.04 0.0012 0.0 175.000 0.214 Vel = 3.42 UG3 0.0 11.65 G 8.05 140.000 75.902 to 150.0 T 80.498 88.547 0.0 TEST 1135.04 0.0012 0.0 228.547 0.280 Vel= 3.42 0.0 1135.04 76.182 KFactor= 130.04 UG1 481.46 11.65 1 80.498 35.000 75.452 to 150.0 0.0 80.498 0.0 UG5 481.46 0.0003 0.0 115.498 0.029 Vel = 1.45 UG5 0.0 11.65 T 80.498 290.000 75.481 to 150.0 0.0 80.498 0.0 UG6 481.46 0.0003 0.0 370.498 0.093 Vel = 1.45 UG6 0.0 11.65 T 80.498 375.000 75.574 to 150.0 0.0 80.498 0.0 UG2 481.46 0.0003 0.0 455.498 0.114 Vel= 1.45 0.0 481.46 75.688 K Factor= 55.34 1A 97.64 1.682 1 9.9 57.500 20.636 to 120.0 0.0 9.900 0.0 102 97.64 0.2453 0.0 67.400 16.534 Vel = 14.10 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams Cal-West Fire Protection Page 7 Sprouts Design Area #1 Sales Floor" Date 1.23.18 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C' or Ftngs Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 102 -45.18 3.26 0.0 11.500 37.170 to 120.0 0.0 0.0 0.0 103 52.46 0.0030 0.0 11.500 0.035 Vel = 2.02 103 101.61 3.26 0.0 11.500 37.205 to 120.0 0.0 0.0 0.0 104 154.07 0.0228 0.0 11.500 0.262 Vel = 5.92 104 100.06 3.26 0.0 11.500 37.467 to 120.0 0.0 0.0 0.0 105 254.13 0.0573 0.0 11.500 0.659 Vel = 9.77 105 -17.45 3.26 0.0 11.500 38.126 to 120.0 0.0 0.0 0.0 106 236.68 0.0503 0.0 11.500 0.579 Vel = 9.10 106 -16.48 3.26 0.0 11.250 38.705 to 120.0 0.0 0.0 0.0 107 220.2 0.0440 0.0 11.250 0.495 Vel = 8.46 107 -16.13 3.26 0.0 11.250 39.200 to 120.0 0.0 0.0 0.0 108 204.07 0.0382 0.0 11.250 0.430 Vel= 7.84 108 -16.34 3.26 0.0 11.250 39.630 to 120.0 0.0 0.0 0.0 109 187.73 0.0327 0.0 11.250 0.368 Vel= 7.22 109 -17.10 3.26 0.0 11.000 39.998 to 120.0 0.0 0.0 0.0 110 170.63 0.0275 0.0 11.000 0.302 Vel= 6.56 110 -18.39 3.26 0.0 11.500 40.300 to 120.0 0.0 0.0 0.0 111 152.24 0.0223 0.0 11.500 0.256 Vel= 5.85 111 -20.02 3.26 0.0 11.500 40.556 to 120.0 0.0 0.0 0.0 112 132.22 0.0171 0.0 11.500 0.197 Vel = 5.08 112 -22.05 3.26 0.0 10.000 40.753 to 120.0 0.0 0.0 0.0 113 110.17 0.0122 0.0 10.000 0.122 Vel= 4.23 113 -24.13 3.26 0.0 7.750 40.875 to 120.0 0.0 0.0 0.0 114 86.04 0.0077 0.0 7.750 0.060 Vel= 3.31 114 -25.96 3.26 0.0 8.500 40.935 to 120.0 0.0 0.0 0.0 115 60.08 0.0040 0.0 8.500 0.034 Vel= 2.31 115 -28.14 3.26 T 20.159 9.500 40.969 to 120.0 0.0 20.159 0.0 116 31.94 0.0012 0.0 29.659 0.037 Vel = 1.23 116 0.0 1.682 T 9.9 144.000 41.006 to 120.0 0.0 9.900 0.0 216 31.94 0.0310 0.0 153.900 4.778 Vel = 4.61 0.0 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams Cal-West Fire Protection Page 8 Sprouts Design Area #1 Sales Floor' Date 1.23.18 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C' or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 31.94 45.784 K Factor = 4.72 102 45.19 4.26 2E 26.334 29.000 37.170 to 120.0 0.0 26.334 0.0 101 45.19 0.0006 0.0 55.334 0.035 Vel = 1.02 101 -22.10 4.26 T 26.334 8.000 37.205 to 120.0 0.0 26.334 0.0 100 23.09 0.0002 0.0 34.334 0.006 Vel = 0.52 100 0.0 1.682 T 9.9 102.000 37.211 to 120.0 0.0 9.900 0.0 200 23.09 0.0170 0.0 111.900 1.905 Vel = 3.33 200 0.0 4.26 0.0 8.000 39.116 to 120.0 0.0 0.0 0.0 201 23.09 0.0002 0.0 8.000 0.002 Vel = 0.52 201 22.10 4.26 2E 26.334 34.910 39.118 to 120.0 0.0 26.334 0.0 202 45.19 0.0006 0.0 61.244 0.039 Vel = 1.02 0.0 45.19 39.157 K Factor = 7.22 1G -66.37 1.682 0.0 10.250 19.406 K Factor =8.00 to 120.0 0.0 0.0 0.0 1H -66.37 -0.1201 0.0 10.250 -1.231 Vel = 9.58 1H 34.10 1.682 0.0 10.250 18.175 K Factor =8.00 to 120.0 0.0 0.0 0.0 ii -32.27 -0.0316 0.0 10.250 -0.324 Vel = 4.66 ii 33.80 1.682 0.0 10.250 17.851 K Factor= 8.00 to 120.0 0.0 0.0 0.0 11 1.53 0.0001 0.0 10.250 0.001 Vel = 0.22 11 33.80 1.682 0.0 10.250 17.852 K Factor= 8.00 to 120.0 0.0 0.0 0.0 1K 35.33 0.0374 0.0 10.250 0.383 Vel= 5.10 1K 34.17 1.682 0.0 10.250 18.235 K Factor =8.00 to 120.0 0.0 0.0 0.0 1L 69.5 0.1308 0.0 10.250 1.341 Vel = 10.04 1L 35.39 1.682 4E 19.799 40.500 19.576 K Factor =8.00 to 120.0 T 9.9 29.699 0.0 203 104.89 0.2801 0.0 70.199 19.660 Vel = 15.15 0.0 104.89 39.236 K Factor = 16.75 1G 101.61 1.682 T 9.9 57.500 19.406 to 120.0 0.0 9.900 0.0 103 101.61 0.2641 0.0 67.400 17.799 Vel = 14.67 0.0 101.61 37.205 K Factor= 16.66 1M -64.13 1.682 0.0 7.000 20.169 K Factor =8.00 to 120.0 0.0 0.0 0.0 1 -64.13 -0.1127 0.0 7.000 -0.789 VeI= 9.26 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams Cal-West Fire Protection Page 9 Sprouts Design Area #1 "Sales Floor" Date 1.23.18 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. C or Ftngs Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn iN 35.22 1.682 0.0 7.000 19.380 K Factor =8.00 to 120.0 0.0 0.0 0.0 10 -28.91 -0.0259 0.0 7.000 -0.181 Vel = 4.17 10 35.05 1.682 4E 19.799 13.000 19.199 K Factor =8.00 to 120.0 0.0 19.799 0.0 1P 6.14 0.0015 0.0 32.799 0.048 Vel= 0.89 1P 35.10 1.682 0.0 8.000 19.247 K Factor =8.00 to 120.0 0.0 0.0 0.0 1Q 41.24 0.0499 0.0 8.000 0.399 Vel = 5.95 1Q 35.46 1.682 0.0 8.000 19.646 K Factor = 8.00 to 120.0 0.0 0.0 0.0 1R 76.7 0.1569 0.0 8.000 1.255 Vel = 11.07 1 R 36.57 1.682 T 9.9 47.500 20.901 K Factor = 8.00 to 120.0 0.0 9.900 0.0 204 113.27 0.3229 0.0 57.400 18.532 Vel = 16.36 0.0 113.27 39.433 K Factor= 18.04 1M 100.06 1.682 T 9.9 57.500 20.169 to 120.0 0.0 9.900 0.0 104 100.06 0.2566 0.0 67.400 17.298 Vel = 14.45 0.0 100.06 37.467 K Factor= 16.35 101 22.10 1.682 2T 19.799 102.000 37.205 to 120.0 0.0 19.799 0.0 201 22.1 0.0157 0.0 121.799 1.913 Vel= 3.19 0.0 22.10 39.118 K Factor = 3.53 105 17.44 1.682 2T 19.799 146.500 38.126 to 120.0 0.0 19.799 0.0 205 17.44 0.0101 0.0 166.299 1.686 Vel= 2.52 0.0 17.44 39.812 K Factor = 2.76 106 16.49 1.682 2T 19.799 146.500 38.705 to 120.0 0.0 19.799 0.0 206 16.49 0.0091 0.0 166.299 1.519 Vel = 2.38 0.0 16.49 40.224 K Factor = 2.60 107 16.13 1.682 2T 19.799 146.500 39.200 to 120.0 0.0 19.799 0.0 207 16.13 0.0088 0.0 166.299 1.458 Vel = 2.33 0.0 16.13 40.658 K Factor= 2.53 108 16.34 1.682 2T 19.799 146.500 39.630 to 120.0 0.0 19.799 0.0 208 16.34 0.0090 0.0 166.299 1.494 Vel = 2.36 Computer Programs by Hydratec Inc. Revision: 50.52.1 Final Calculations - Hazen-Williams Cal-West Fire Protection Page 10 Sprouts Design Area #1 "Sales Floor' Date 1.23.18 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. I.G. or Ftngs Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 0.0 16.34 41.124 KFactor= 2.55 109 17.10 1.682 2T 19.799 146.500 39.998 to 120.0 0.0 19.799 0.0 209 17.1 0.0098 0.0 166.299 1.625 Vel= 2.47 0.0 17.10 41.623 KFactor= 2.65 110 18.38 1.682 2T 19.799 146.500 40.300 to 120.0 0.0 19.799 0.0 210 18.38 0.0112 0.0 166.299 1.858 Vel = 2.65 0.0 18.38 42.158 KFactor= 2.83 111 20.03 1.682 2T 19.799 146.500 40.556 to 120.0 0.0 19.799 0.0 211 20.03 0.0131 0.0 166.299 2.177 Vel= 2.89 0.0 20.03 42.733 K Factor 3.06 112 22.05 1.682 2T 19.799 146.500 40.753 to 120.0 0.0 19.799 0.0 212 22.05 0.0156 0.0 166.299 2.599 Vel = 3.18 0.0 22.05 43.352 K Factor = 3.35 113 24.14 1.682 2T 19.799 146.500 40.875 to 120.0 0.0 19.799 0.0 213 24.14 0.0185 0.0 166.299 3.074 Vel = 3.49 0.0 24.14 43.949 K Factor = 3.64 114 25.95 1.682 21 19.799 146.500 40.935 to 120.0 0.0 19.799 0.0 214 25.95 0.0211 0.0 166.299 3.516 Vel = 3.75 0.0 25.95 44.451 K Factor = 3.89 115 28.14 1.682 2T 19.799 146.500 40.969 to 120.0 0.0 19.799 0.0 215 28.14 0.0245 0.0 166.299 4.082 Vel = 4.06 0.0 28.14 45.051 KFactor= 4.19 Computer Programs by Hydratec Inc. Revision: 50.52.1 AutoPeaking Summary Cal-West Fire Protection Sprouts Design Area #1 "Sales Floor' Auto Peaking Summary - List of Pipes for Area Calculated Left Right Side Side From To Length From To Length 1A 102 57.500 1 202 40.500 1G 103 57.500 1L 203 40.500 1M 104 57.500 1R 204 47.500 Flow Safety Pressure Required Margin Differential Left 10.250 I 1132.606 37.583 -0.259 Area Calculated I 1135.039 37.325 0.000 Right 10.250 I 1138.756 37.411 -0.087 Typical Distance Between Heads = 10.250 Split Point Used in Worst Area Peaked = II Computer Programs by Hydratec Inc. Revision: 50.52.1 Page 11 Date 1.23.18 No. 135 0 CARLSBAD FIRE DEPARTMENT Fire Prevention Division 1635 Faraday Avenue - Carlsbad, CA 92008 760.602.4665 WATER AVAILABILITY FORM SECTION A: TO BE COMPLETED BY CUSTOMER PROJECT NAME: Sprouts Farmers Market SR#: (Assigned upon plan submittal) PROJECT ADDRESS: 6217 El Fuerte St CITY: Carlsbad PHONE: (714) 914-4552 (Cal-West Fire) FAX NUMBER: ( 714 ) 912-4641 Largest Building (ft.2): 26,000 Sprinkled? Yes Construction Type: UNK SECTION B: TO BE COMPLETED BY LOCAL WATER COMPANY. CUSTOMER TO PROVIDE RESULTS TO CFD. Water Purveyor: City of Carlsbad Location of test (reference map required): El Fuerte St north of Gateway Rd TEST INFORMATION IS VALID FOR 6 MONTHS FROM DATE PERFORMED Flow Test Results Static pressure: 129 PSI Hydrant Number (if applicable):H20910 Elevation of test: 402 Feet Main Size: 24 INCH Pressure Zone: 700 Feet Date/TimeofTest. - - Pot Tube Reading: PSI Corespondglow GPM Total Flow: 8,000 GPM Residual Pressure 110 PSI Atpeakdemand, this water system is capable of providing a fire flow discharge at 20 psi in excess of 8,000 gpm. Note: If the water availability information was obtained in a manner other than a flow test (i.e. computer modeling), fill out the information above as applicable and check here: x Name: Jennifer _R.Mael,P.E. Eng. Lic. No. (if applicable): C69606 Signature:_________________________________________ Title/Org(._iectManager Date: 01/11/2018 30. 30 30" 8" _____ 8" f I a I I N + Legend I w_Hydrant Pipe ZONE 8 -550 -700 a 1%" Fire Flow Test j Q. Location H20910 " 120 12 w LEIGHTON C a LL?TINGTONWY Cr IU 8 a ALAMEDA CR HANCOCKC 4WN GARDEN RD 12" -t a F-1 7 GATEWAYRD 12" a 12' Sprouts Farmers Market - Fire Flow Analysis ES-A-I n Building Riser Series IBR In-Building Risers Sizes: 4' - 10' (100— 250mm) = ow lmctug ;) A A M E FIRE &WATERWORKS Features Cost savings Corrosion resistant stainless steel construction, type 304 Ease of installation and light weight allows one person to position and handle the riser Minimal site preparation; joint restraint one-piece construction reduces time and labor; no missing parts, no leaks; easily identifiable for approvals Includes Test Cap and Coupler UL/FM approved Sizes: available in 4 - 10' (100-250mm) with various lengths to meet all local requirements Designed to meet NFPA 24-2007 Section 10.6.5 AWWA C900 Inlet/DIP AWWA C606 Outlet I,,I, I.....,.. uvu Ia, I IC Job Location Engineer Approval Series IBR In-Building Risers are used to connect the main fire supply to the building overhead fire system. The fitting passes under the foundation without joints and extends up through the floor. Provided with installation tabs, the unit has a CIPS (Cast Iron Pipe Size) coupler for easy connec- tion to the underground supply (AWWA C900 PVC and Ductile Iron Pipe) and industry standard grooved-end connection (AWWA C606) on the building side for easy connection to the overhead fire sprinkler system. Ames In-Building Risers are precision engineered and manufactured to provide exceptional reliability and reduce installation time & labor costs associated with field assembly. In accordance with NFPA 24-2007, the UL/FM approved In-Building Risers replace numerous fittings, elbows & spools and reduces the possibility of leaks or failure in comparison to traditional installation methods and materials. Factory tested integrity ensures the highest quality installation. The use of stainless steel signifi- cantly increases the reliability and life of the riser. The wetted surface of this product contacted by consumable water contains less than one quarter of one percent (0.25%) of lead by weight. Ut,, ILl autul Approval Contractor's P.O. No. Representative Ames product specifications in U.S. customary units and metric are approximate and are presided for reference only. For precise measurements, please contact Ames Technical Service. Ames reserves the right to change or modify product design, construction, specifications, or materials without prior notice and without incurring any obligation to make such changes and modifications on Ames products previously or subsequently sold. www.amesftrewater.com Specifications In-Building Riser shall be installed as indicated on the plans. Riser shall be composed of a single extended 90 degree fitting of fabricated 304 stainless steel tub- ing, maximum working pressure 200psi (14 bar). The fitting shall have a grooved-end connection on the outlet (building) side and a CIPS coupler on the inlet (underground) side. The grooved end shall include a coupler and cap to facilitate testing of the underground piping. The In-Building Riser shall be an Ames Fire & Waterworks Series IBR. Approvals Fittings FM class 1920 UL HKQA (4-10) < SFM > Sh Dimensions - Weights — A J7 Grooved End (Flange Optional) CIPS Coupling Bracket Ila C in. mm A(OD) in. mm B It cm C It. cm lbs. kg 4 100 41/2 114 6 183 6 183 71 32 6 150 6% 168 6 183 6 183 98 44 8 200 1 85/8 219 6 183 1 6 183 129 59 10 250 1 10/4 273 6 183 1 6 183 202 92 Consult factory for custom leg dimensions. Standards NFPA - Designed to allow the contractor to conform to NFPA 24-2007 Section 10.6.5: Where a riser is close to building foundations, under- ground fittings of proper design and type shall be used to avoid pipe joints being located under the foundations. NFPA 24-2007,10.1.1, 10.6.7 End Connections Horizontal End: Mates with Ductile Iron Pipe and AWWA C900 Pipe (PVC Pipe with Ductile Iron Pipe Equivalent OD's) Utilizes Gasket conforming to UL 157 with "Lock in" gasket configuration 141(!1j 1IItLlhl ,]I in. mm in. mm 4 100 4.8 122 6 150 6.9 175 8 200 9.1 230 10 250 1 11.1 282 Testing Welds are 100% leak tested at the factory SIZE DESIGN PROOF PRESSURE in. mm psi bar 4 100 1000 70 6 150 1000 70 8 200 800 56 in 2!fl Rflfl Vertical End: Meets AWWA C-606 dimensions for roll grooved pipe Meets AWWA C-207 class D for flanges Ratings Meets AWWA C-900 pressure class 200, DR 14 Pipe IMPORTANT: Inquire with governing authorities for local installation requirements. A A M E S FIRE & WATERWORKS wWW.amesfirewater.com A Watts Water Technologies company USA: Backflow- 1427 N. Market Blvd • Suite 119 • Sacramento, CA 95834 • T: 916-928-0123 • F: 916-928-9333 Control Valves- 18550 Hansen Road • Houston, D( 77075 • T: 713-943-0688 • F: 713-944-9445 Canada: 5435 North Service Rd. • Burlington, ONT. L7L 5H7• T: 905-332-4090 • F: 905-332-7068 ES-A-InBuildirtgRiser 0935 © 2009 Ames Fire & Waterworks PACIFIC STATES CAST IRON PIPE COMPANY DIVISION OF MCWANE. INC. P.O. BOX 1219, PROVO, UTAH 84603 TELEPHONE (AREA CODE 801) 373-6910 STANDARDS In each of the following, standards are developed by committees consisting of consumer, general interest and manufacturing members: American National Standards Institute (ANSI) American Water Works Association (AWWA) American Society for Testing and Materials (ASTM) Underwriters Laboratories (UL) MH16433(N) National Fire Protection Association (NFPA) National Sanitation Foundation (NSF) 61-1989 Factory Mutual (FM) J12VOA8.AH For ready reference, standards for ductile iron pipe are listed below: Standard Designation ANSI/AWWA C150/A2 1.50 ANSI/AWWA C151/A21.51 ANSI/AWWA C110/A21.10 ANSI/AWWA C153/A21.53 ANSI/AWWA Cil l/A21.1 1 ANSI/AWWA C115/A21.I5 ANSI/AWWA C104/A21.4 ANSI/AWWA C105/A21.5 & ASTM A674 ANSI/AWWA C600 ASTM A746 NFPA Outside Protection 24 Subject Covered Design Water Pipe Fittings - Cast Iron Fittings - Ductile Iron Rubber - Gasket Joints Flanged Pipe Cement - Mortar Linings Polyethylene Encasement for Ductile Iron Pipe Installation Gravity Sewers Fire Protection Piping Pacific States ductile iron pipe meets and exceeds the requirements of all of the above national standards relating to pipe manufacture and performance. PACIFIC STATES CAST IRON PIPE COMPANY OMSION OF MCWANE, INC. P.O. BOX 1219, PROVO, UTAH 84603 TELEPHONE (AREA CODE 801) 373-6910 FAX: (801) 377-0338 EMAIL: sales@pscipco.com WEBSITE: www.psdpco.com Thickness, Dimensions and Weights of Mechanical Joint Ductile Iron Pipe by Size for Each Thickness. Nominal Wt. of Barrel Mechanical Joint Wt. of Wt. Per Avg. Wt. Thickness Thickness OD* Per Ft. t Bell Lgth.t Per Ft.t Size Class In. In. Lb. Lb. Lb. Lb. 3 53 .31 3.96 10.90 11 230 11.4 4 53 .32 4.80 13.80 16 290 14.6 6 53 .34 6.90 21.40 18 405 22.4 8 53 .36 9.05 30.10 24 565 31.4 10 53 .38 11.10 39.20 31 735 40.9 12 53 .40 13.20 49.20 37 925 51.3 tincluding bell; calculated weight of pipe rounded off to the nearest 51b *Tolerances of OD of spigot end; 3-12 in. ±0.06 in. Including bell; average weight per foot, based on calculated weight of pipe before rounding. Back Two I1and Three-Way 4" x 2'/2" x 21/2' Connections 1 5V2" 8V8" El 63 14* o 6315* Angle 4" x 21/2" x 21/2" 1 8'Ia 8I4" O 6324 Back 4" x 2V2" x 2V2" 2 7'/4" 10'I2" El 6325 Angle 4" x 21/2" x 21/2" 2 8'/4" 10'/2 El 6326 Back 6" x 21/2" x 21/2" 2 7'/4" 10'I2" fl 6327 Angle 6"x 21I2" x 21/2" 2 10" 10'/2" El 6336 Back 6"x 2'/2" x 21/2" x 21h" 3 10'I2 13/4" E] 6337 Angle 6" x 21/2" x 2'/2" x 21/2" 3 11V2" 141/2" Body Lettering 0 AUTO SPKR El STANDPIPE El Blank (unlettered) 6315 1632416326 I JVJLGUARDIAN Ph. FIRE EQLPMENT,INC. DETAIL AND SUBMITTAL SHEET MIAMI, FIL 00.327.6584 Fax 800.827.3869 *I'I'Series - Fire IiP1. Inl IConnections - F Bodies Project/Location: Date: Architect/Engineer: Qty: Contractor: IIAppropriate Selection Used as auxiliary connections through which the fire department can pump water to supplement existing water supplies. Provides 250 GPM flow (minimum), per 21/2" inlet. Two and three-way - inlet connections feature clappered brass bodies (straight or angle pattern), with female hose thread swivel inlets and female outlets. Cast brass construction, standard. *Auto Spkr lettering only Optional Finish: 0-B Polished Brass Threads: 0-c Rough Chrome Plated DNST C3 -D Polished Chrome Plated 0 Other H LU 632516327 Plugs with Chains and Break Caps - Used to keep fire dept. inlet connections free of debris and protect female threads. Break Caps fl1) 06406 2V2"IAluminum 0 6407 2'/2" j Plastic Threads: Adjustable Plugs DNST JY4 DOther 0 6408 2'/2" Aluminum 0 6409 2'/2" Plastic Contact factory for current listings and approvals Plugs with Chains lEl 6404 [2'/l" I Brass I Optional Finish: 0-B Polished 0-C Rough Chrome Plated D-D Polished Chrome Plated Ii' 6336 ff',~ B 6337 ES-F-LF876V Job Name Contractor Job Location Approval Engineer Approval MasterSeries® LF876V Double Check Detector Backflow Prevention Assemblies (Type II) Size: 21/2" - 8" (65mm - 200mm) The FEBCO MasterSeries LF876V Double Check Detector Assembly is specifically designed to protect against possible backpressure and backsiphonage conditions for non-health hazard (i.e., pollutant) application in accordance with Local Governing Water Utility Code. This Backflow Assembly is primarily used on potable drinking water systems and fire sprinkler systems, where Local Governing Code mandates protection from non-potable quality water being pumped or siphoned back into the potable water system. Features Main Valve: Inline Serviceable Assembly Horizontal 'N-Pattern" Installations Vertical-Up "Z-Pattern" Installations No Special Tools Required for Servicing Captured Modular Spring Assembly Reversible & Replaceable Discs Field Replaceable Seats Ductile Iron Valve Body Design Stainless Steel Check Components Winterization feature with disc retainers and valve body drain ports Clapper Check Assembly Commonality between 1st & 2nd Check Components Captured 0-ring Design Auxiliary Bypass: Compact Bypass Design; Remains within Main Valve Assembly Profile Inline Serviceable 3/4" Backflow Assembly No Special Tools Required for Servicing Field Replaceable Seats & Discs Contractor's P.O. No. Representative Model LF876V Double Check Detector Assembly Specifications The FEBCO MasterSeries LF876V Double Check Detector Valve Assembly shall be installed on the potable water supply and at each point of cross-connection to protect against possible backpressure and backsiphonage conditions for non-health hazard (i.e., pollutant) applications. The assembly shall consist of a main line valve body composed of two (2) independently acting approved clapper style check modules with replaceable seats and disc rubbers. Servicing of both check modules does not require any special tools and are accessed through independent top entry covers. This assembly shall be fitted with approved UL/ FM inlet/outlet resilient seated shutoff valves and contain four (4) properly located resilient seated test cocks as specified by AW\NA Standard 0510. The auxiliary bypass line contains a %"x3/4" Water Meter that complies with ANSI/A\MNA Standard 0700 coupled with an approved check assembly. The bypass line is designed to detect leaks or unauthorized water usage of the water system while protecting against possible backpressure and backsiphonage conditions for non-health hazard (i.e., pollutant) application. The assembly shall be approved for horizontal and/or vertical-up installations while meeting the requirements of AVWrIA Standard 0510 flow and pressure loss performance parameters. i!(1111D1 The information contained herein is not intended to replace the full product installation and safety information available or the experience of a trained product installer. You are required to thoroughly read all installation instructions and product safety information before beginning the installation of this product. 11119=11111111 Inquire with governing authorities for local installation requirements Detect Potential Underground Water Leaks *The wetted surface of this product contacted by consumable Detect Unauthorized Water Usage water contains less than 0.25% of lead by weight. Fi7FEBCO product specifications in U.S. customary units and metric are upproalmate and are provided for reference only. For precise measurements, please contact FEBCO Technical Service. FEBCO reserves the right to change or modify product design, construction, specifications, or materials with- out prior notice and without incurring any obligation to make such changes and modifications on FEBCO products previously or subsequently sold. A WATTS Brand Options — Suffix OSY: ULJFM Approved OS&Y Gate Valves [ANSI/AWWA 0515 Compliant] CFM: Totalizing Cubic feet/min %"x 3/4 ' Water Meter [ANSI! AWWA 0700 Compliant] GPM: Totalizing Gallons/mm 5/e"x 3/4" Water Meter [ANSI! AWWA 0700 Compliant] LG: Less Shutoff valves; This is NOT an APPROVED ASSEMBLY Example Ordering Description: 4" LF876V-OSY-GPM - Valve Assembly fitted with OS&Y Shutoff Valves & Gallons per Minute Water Meter 4' LF876V-OSY-CFM - Valve Assembly fitted with OS&Y Shutoff Valves & Cubic Feet per Minute Water Meter Available Components Wye Strainer FDA Approved [ASME B16.1 Class 125 & AWWA Class D Flange] Series 611 Valve Setter MJ x MJ - Mechanical Joint x Mechanical Joint [AWWA C111/A21.11] MJ x FL - Mechanical Joint x Range [AWWAC111/A21.11; ASME B16.1 Class 125/AWWA Class D Flange] FL x FL - Range x Range [ASME 1316.1 Class 125 &AWWA Class D Flange] Materials Below is a general materials list of the Model LF876V. Al assemblies size 21/2" through 8' is similar in materials and construction. Please contact your local FEBCO Representative if you require further information. Main Valve Body: Ductile iron Grade 65-45-12 Coating: Fusion epoxy coated internal and external A'MNA 0550-90 Shutoff Valves: OSY resilient wedge gate valve A\MNA C515 (tJL/Rvl) Check Seats: Stainless Steel Disc Holder: Stainless Steel Elastomer Disc: Silicone Spring: Stainless Steel Clamp: AWWA 0606 Approvals — Standards: Approved by the Foundation for Cross-Connection Control and Hydraulic Research at The University of Southern California [FCCCHR-USC] ASSE 1048 Listed —UL Classified [US & Canada] FM Approved IAPMO!cUPC AWWA Standard 0510 Compliant End Connections: Compliant to ASME B16.1 Class 125 & AWWA Class D Range -Assembly configured with UL/FM Approved OS&Y RW Gate Valves. Less gate valve assemblies are not UL/FM approved configurations. Assembly Flow Orientation: Horizontal (N-Pattern 21/2" - 8") - Approved by FCCCHR-USC, ASSE, cULus, FM, IAPMO/cUPC Vertical Up (Z-Pattern 21/2" - 8") - Approved by FCCCHR-USC, ASSE, cULus, FM, IAPMO/cUPC E!E ®C 0 ® osife — &; Approved C 1048 B64.5 Pressure - Temperature Max. Working Pressure: 175p5i (12.1 bar) Min. Working Pressure: lOpsi (0.7 bar) Hydrostatic Test Pressure: 350p5i (24.1 bar) Hydrostatic Safety Pressure: 700p5i (48.3 bar) Temperature Range: 33°F - 140°F [0.5°C- 60°C] Continuous mb Cock 94 Dimensions - Weights Size: 21/2"- 8" Below are the nominal dimensions and physical weights for the Model LF876V size 21/2" through 8'. Allowances must be made for normal manufacturing tolerances. Please visit our websfte to download a copy of this product's installation instructions, or contact your local FEB00 Representative for more information. Model LF876V Standard Orientation (N-Pattern) Model LF876V Vertical Orientation (Z-Pattern) Note: The Series LF876V is shipped in the standard (N-Pattern) orientation as shown above. Gate Valve Side View Clearance LF876V DIMENSIONS WEIGHT ] in. mm A in. mm B in. mm C in. mm D in. mm E in. mm F in. mm G in. mm in. H mm I in. mm J in. mm in. mm L in. mm 05Y lbs. kg. 2Y2 65 29Y8 740 121/2 318 61/4 159 251/4 642 171/2 445 13% 346 27V4 692 51/2 140 11½ 283 3/2 89 16% 416 111/2 292 216 98 3 80 29Y8 740 121/2 318 61/4 159 25Y4 654 173/4 451 141A 359 28/4 718 5½ 140 11½ 283 33/4 95 221/4 565 11½ 292 242 110 4 100 31Y8 791 14 356 7 178 27Y4 705 18% 476 151h 394 31 787 6 152 11½ 283 41/2 114 231/4 591 13 330 347 157 6 150 35% 908 16 406 8 203 32Y4 831 221/8 562 18% 473 37Y4 946 71/4 184 121h 316 51/2 140 301/a 765 13 330 529 240 8 200 40Y4 1035 181/2 470 1 9¼ 235 1 36Y4 933 251/8 638 203/4 527 1 411/2 10541 8½ 216 1 14 356 1 63/4 172 37% 959 141/2 368 1 827 375 Notes: * Indicates nominal dimensions with OSY Gate Valves (Full Open Position) Indicates weight of complete Backtlow Assemblies with specified Gate Valves Standard Orientation *N-Pattern" Row curve N Pipe Support (furnished by customer) for valve weight only. te1icsi Orientation 2-Pattern Flow curve z Performance Flow capacity chart identifies valve performance based upon rated water Velocity up to 20fps Maximum service flow rate is determined by maximum rated Velocity of 7.5fps. A'MNA Manual M-22 (Appendix C) recommends that the maximum water Velocity in the services be not more than 1 0fps. UL flow rate is determined by typically rated Velocity of 15 feet/sec. Capacity N-Pattern Pern 2½" LF876V PSI Service flow Rated flow *UL Rated flow 22 20 18 12 10 14 I I q 0 25 50 75 100 125 150 175 200 225 250 215 300 325 350gpm 284 588 852 1136 1pm 7.5 14.7 22.0 fps LF876V PSI Service Row Rated flow *UL Rated Flow 22 20 I 18 16 I I I 3 14 I I 12 I I US U to I - 41 I I (I I 0 50 100 150 200 250 300 350 400 450 500 gpm 379 757 1136 1514 1pm 75 145 22.0 fps 4" LF876V PSI Service flow Rated flow UL Rated Flow I I I 18 I I 16 I I 14 I I I 12 I I 10 I I 8 "- 6 t-. 4 I I I I I I 2 I 0 . I o 100 200 300 400 500 600 700 800gpm 379 1136 1893 2650 1pm 7.5 12.8 19.1 fps 6" LF876V PSI Service flow Rated flow *UL Rated flow 18 IC I I 1 I I I I I I 1 10 I I I 8 us _ - 0 200 480 757 600 800 1080 1200 2271 3785 7.5 11.4 1400 1600gpm 5300 1pm 17.0 fps 8" LF876V PSI 18 16 14 12 10 03 q 0 400 800 1200 1600 2000 2480 9pm 1514 3028 4543 6057 7571 9085 1pm 7.5 10.5 15.3 fps Service flow Rated flow *UL Rated flow A WATTS Brand ES-F-LF876V 1515 USA- Tel: (800) 767-1234 • Fax: (800) 788-4491 • FEBcoorrline.com Canada: Tel: (905) 332-4090 • Fax: (905) 332-7068 " FEBcoonline.ca Latin America: (52) 81-1001-8600" Fax: (52) 81-8000-7091 • FEBcoonline.com © 2017 FEB00 JMagle Building essentials for a better tomorrow' no] i Lolls 0 16,01 1 61M Ito SUBMITTAL AND DATA SHEET I.D. : Inside Demeter O.D. Outside Diameter T. Wall Thickness D° Bell Outside Diameter E: Distance between Assembly Mark to the end of spigot. D9 PIPE SIZE (IN) AVERAGE O.D. (IN) NOM. I.D. (IN) MIN. T. (IN) MIN. E (IN) APPROX. D9 (IN) APPROX. WEIGHT (LBS/Fl) PRESSURE CLASS 165 psi (DR 25) 4 4.80 4.39 0.192 5.25 5.57 1.9 6 6.90 6.31 0.276 6.40 8.00 3.9 8 9.05 8.28 0.362 7.05 10.50 6.7 10 11.10 10.16 0.444 8.20 12.88 10.1 12 13.20 12.08 0.528 8.80 15.31 14.4 PRESSURE CLASS 235 psi (DR 18)* 4 4.80 4.23 0.267 5.25 5.87 2.6 6 6.90 6.09 0.383 6.40 8.43 5.3 8 9.05 7.98 0.503 7.05 11.06 9.2 10 11.10 9.79 0.617 8.20 13.57 13.9 12 13.20 11.65 0.733 8.80 16.13 19.7 PRESSURE CLASS 305 psi (DR 14)* 4 4.80 4.07 0.343 5.25 6.17 3.2 6 6.90 5.86 0.493 6.40 8.87 6.7 8 9.05 7.68 0.646 7.05 11.63 11.6 10 11.10 9.42 0.793 8.20 14.27 17.6 12 13.20 11.20 0.943 8.80 16.97 25.1 Consult JM Eagle" for GSA and other listing availability prior to shipment. Note: *FM Approvals Pressure Glass 150 psi for DR 18 and 200 psi for DR 14. * Contact your JM eagleTM sales representative for location availability. Assembly Mark Product Standard: ANSI/AWWA C900 Pipe Compound: ASTM Dl 784 Cells Class 12454 Gasket: ASTM F477 Integral Bell Joint: ASTM D3139 Certifications: ANSI/NSF Standard 61 UL Standard 1285 Pipe Length: 20 feet laying length Installation: AWWA C605 JM Eaglet" Installation Guide JM EagleTM also manufactures this pipe in green for sewer force main applications and purple, specifically for reclaimed water systems. This pipe is made to the same requirements as our standard products. The only difference is that the pigment used is green or purple. These products will not be marked with UL or NSF listing marks. Additionally, the green pipe will be marked "Forced Sewer" and the purple pipe will be marked: "Reclaimed Water... Do Not Drink." 2" THROUGH 12" MODEL KS-FW AWWA C-509 AWWA c550 CER11RED PROUDLY MADE IN ELMIRA. NEW YORK USA (Revised 03-27-2011) During the decade of the 1980's, the waterworks industry was introduced to the Resilient Seated Gate Valve, a design principle that is dominant in preference for use in distribution systems. Kennedy Company was at the forefront in this industry-wide movement by introducing the Ken Seal Series, our AWWA C509 Resilient Seated Gate Valve. In 2002, with the end user in mind, Kennedy redesigned the Ken Seal Series introducing the model KS-FW. The goal of the redesign was to eliminate the customer need for any anti- rotational bolts. Kennedy did this by designing a machined elliptical bolthole in place of an as-cast opening. This elliptical design allows valve installers to slide a standard sized bolt into the slot, therefore eliminating the need to have two different types of bolts on the installation. RECOMMENDED SPECIFICATIONS FOR C-509 CAST IRON RESILIENT WEDGE GATE VALVES KENNEDY VALVE COMPANY Valves shall conform to the latest revision of AWWA Standard C-509 covering resilient seated gate valves for all water supply service. The valves shall have a cast iron body, bonnet, and 0-ring plate. The wedge shall be totally encapsulated with rubber. The sealing rubber shall be permanently bonded to the wedge per ASTM D429. Valves shall be supplied with 0-ring seals at all pressure retaining joints. No flat gaskets shall be allowed. Blind bolts shall not be allowed. The valves shall be either non-rising stem or rising stem, opening by turning left or right, and provided with 2" square operating nut or a handwheel with the word "Open" and an arrow to indicate the direction to open. Stems for NRS assemblies shall be cast bronze with integral collars in full compliance with AWWA. OS&Y (rising stems) shall be bronze. All stems shall operate with bronze stem nuts independent of wedge and of stem (in NRS valves). Stainless stems are available but not standard. NRS stems shall have two 0-rings located above thrust collar and one 0-ring below. Stem 0-rings shall be replaceable with valve fully opened and subjected to full pressure. The NRS stems on 2"-12" shall also have two low torque thrust bearings located above and below the stem collar to reduce friction during operation. Waterway shall be smooth, unobstructed and free of all pockets, cavities and depressions in the seat area. Tapping valves 4" and larger shall accept a full size tapping cutter. The body, bonnet, and 0-ring plate shall be fusion-bond epoxy coated, both interior and exterior on body and bonnet. Epoxy coating shall be NSF 61 certified and applied in accor- dance with AWWA C550. Each valve shall have manufacturers name, pressure rating, and year in which it was manu- factured cast in the body. Prior to shipment from the factory, each valve shall be tested by hydrostatic pressure equal to the requirements of AWWA C-509 (and UL/FM where applicable). Valves shall have all component parts cast and assembled in the USA and shall be manufactured by the Kennedy Valve Company. (Revised 03-27.2011) Features and Benefits DELRIN THRUST BEARINGS ABOVE AND BELOW THE THRUST COLLAR REDUCE FRICTION AND MINIMIZE OPERATING TORQUES LONG, TROUBLE FREE LIFE WITH HIGH STRENGTH, NON-CORRO- SIVE BRONZE STEM AND STEM NUT. ALL NRS STYLE VALVES ARE STAIN- LESS THE OPERATING MECHANISM IS TRIPLE 0-RING SEALED TO COMPLETELY SEAL AGAINST LEAKAGE PAST THE STEM. TWO 0-RINGS ARE PROVIDED ABOVE THE THRUST COLLAR AND ONE BELOW. UPPER 0-RINGS CAN BE REPLACED UNDER PRESSURE WITHOUT REMOVING THE STEM WHEN THE VALVE IS FULLY OPENED. 0-RING SEALS AT STUFFING BOX AND BONNET TO BODY FLANGES TO ENSURE THE BEST POSSIBLE SEAL. NO FLAT GASKETS. 00% EPDM COATED WEDGE WITH TWIN SEAL DESIGN ENSURES BUBBLE- TIGHT SEAL UP TO 250 PSI EVERY TIME. ELLIPTICAL BOLT HOLE DESIGN ELIMINATES THE NEED FOR ANTI-ROTATION BOLTS KENNEDY CORROSION RESISTANT FUSION- BONDED EPDXY COATING, CONFORMING TO AWWA C-550 AND NSF61 CERTIFIED, PROTECTS BOTH INSIDE AND OUTSIDE OF VALVE. SMOOTH, UNOBSTRUCTED PADS ON THE BOTTOM OF FULL SIZE WATERWAY IS ALL VALVES KEEP VALVE FREE OF POCKETS, CAVI- IN UPRIGHT POSITION TIES, AND DEPRESSIONS FOR EASIER STORAGE ALLOWING FOR MINIMAL AND PROTECTION FROM FLOW LOSS AND LOWER THE ELEMENTS. PUMPING COSTS. ALL TAPPING VALVES ACCEPT FULL SIZE TAPPING CUTTER. ALL VALVES ARE RATED AT 250 PSI FOR AWWA SERVICE AND 200 PSI FOR ULFM SERVICE. ALL VALVES ARE HYDROSTATICALLY TESTED TO 500 PSI. 10 YEAR LIMITED WARRANTY (Revised 03-27-2011) kill I- 8571 8561 8057 8572 MECHANICAL JOINT ENDS FLANGED ENDS THREADED ENDS FLANGED X MJ 2" 12" 2"" 12" 2'.3- 3"'12" ke, 7-1 8597 8576 8901 8701 PUSH-ON FOR PVC MECHANICAL TYTON ENDS FLANGED ENDS 2..S. CUTTING-IN JOINT PUSH-ON FOR (D.I. & C900) POST INDICATOR VALVE (PIV) 4" • 12" 4" • 12" 3" • 12" F T 0 a E (OPEN~ cl — 1 A —J 8902 8950 8071 8068 FLANGED & TYTON JOINT TAPPING X MJ MECHANICAL JOINT FLANGED ENDS PUSH-ON FOR (D.I. & C900) TAPPING VALVE POST INDICATOR VALVE (PIV) OS&Y CONSTRUCTION 4" • 12" 4" • 12" 3" • 12" 21/2" • 12" A B C D E G H P Q P S U V 2" 7 31/4 - 51/4 107/8 - - 3 - - 7114 - - 4 3/4 2 1/2" 7 1/2 - - 7 11 3/8 - - 3 1/4 163/8 13 7/8 71/4 - - 51/2 3" 8 31/2 - 7 1/8 123/8. - 53/4 31/2 187/8 15 5/8 10 - - 10 4 9 41/2 63/4 - 143/4 41/2 63/4 41/2 223/4 18 1/4 10 .6 3/4 93/4 131/2 6" 101/2 5 77/8 - 19 51/4 73/4 5 301/8 23 3/4 12 75/8 113116 19 1/2 81 111/2 51/2 81/2 - 221/2 55/8 8 1/2 51/2 373/4 291/4 14 81/2 113/4 251/2 10" 13 7 10 - 261/2 7 10 - 453/4 353/8 18 10 131/2 311/2 IT 14 63/4 111/4 - 30 81/2 1 107/81 - 531/8 405/8 r,8 1 11 1 143/4 1373/4 V KENNEDY VALVE /V Ii A DIVISION OF MCWANE. INC. www.kennedyvalve.com 2007 1021 E. Water Street Elmira, New York 14901 P.O. Box 981 Phone (607) 734-2211 Fax 1-607-734-3288 (Revised 03-27-2011) OD IAh TRANSITION IMECHANICAL-JOINT GASKET NOM. PIPE A B C(REF) øD E F G SIZE O.D. ±1 % 2 2.375 0.56 0.66 0.31 2.32 0.12 0.21 1.10 3 3.500 0.72 0.64 0.34 3.43 0.12 0.38 1.10 4 4.500 0.76 0.73 0.33 4.43 0.20 0.37 1.26 6 6.625 0.75 0.73 0.32 6.53 0.20 0.36 1.25 8 8.625 0.82 0.73 0.34 8.50 0.20 0.43 1.27 10 10.750 0.79 0.75 0.31 10.59 0.20 0.39 1.26 12 12.750 0.84 0.75 0.33 12.56 0.20 0.44 1.28 MJ Accessories ANSI/AWWA CII 1/A21.11 Page 17 REGISTERED TRADEMARK OF STAR PIPE PRODUCTS STAR PIPE PRODUCTS HOUSTON CORPOE4ATE TOLL FREE I-E).999.3()9 FAX 251-558.9000 1pipprodl50rn MJ Accessories ANSI/AWWA C111/A21.11 BI p . I1JIFDYLGL!KS] NOM. SIZE O.D. A B C I.D. B.C. BOLT HOLE BOLT QTY WT (LBS.) 2 6.12 0.62 1.18 3.40 2.61 4.75 00.75 2 1 4.06 3 7.69 0.62 1.37 4.84 6.19 00.75 4 5 4 9.12 0.75 1.50 5.92 4.90 7.50 00.88 4 6 6 11.12 0.88 1.63 8.02 7.00 9.50 00.88 6 10 8 13.37 1.00 1.75 10.17 9.15 11.75 00.88 6 14 10 15.62 1.00 1.75 12.22 11.20 14.00 00.88 8 -20- 12 17.88 1.00 1.75 14.32 13.30 16.25 00.88 8 24 14 20.25 1.25 2.00 16.40 15.44 18.75 00.88 10 45 16 22.50 1.31 2.06 18.50 17.54 21.00 00.88 12 55 18 24.75 1.38 2.13 20.60 19.64 23.25 00.88 12 55 20 27.00 1.44 2.19 22.70 21.74 25.50 00.88 14 66 24 31.50 1.56 2.31 26.90 25.94 30.00 00.88 16 90 30 39.12 2.00 2.75 33.29 32.17 36.88 01.13 20 220 36 46.00 2.00 2.75 39.59 38.47 43.75 01.13 24 286 42 53.12 2.00 2.75 45.79 44.67 50.62 01.38 28 288 48_ 60.00 2.00 2.75 52.09 50.97 57.50 01.38 32 400 VA NOW O.D. A B C I.D. BC BOLT BOLT WT SIZE . . HOLE QTY (LBS.) 4 9.12 0.75 1.50 5.92 5.10 7.50 00.88 4 3 6 11.12 0.88 1.63 8.02 7.20 9.50 00.88 6 5 8 13.37 1.00 1.75 10.17 9.40 11.75 00.88 6 6 10 15.62 1.00 1.75 12.22 11.50 14.00 00.88 8 8 12 17.88 1.00 1.75 14.32 13.60 16.25 00.88 8 9 16 22.50 1.31 1 2.06 18.50 17.94 1 21.00 00.88 12 14 Page 15 REGISTERED TRADEMARK OP STAR PIPE PRODUCTS START PIPE PRODUCTS HOUSTON CORPOIATE TOLL FREE I.ROD-999.3419 FAX ZSI-SSS.9000 aurpIpcpmthcacam ii!JR !JR. ! I -- • - . MJ x Mj NOM. SIZE BENDS T A 90o BENDS Mj x Mj Q/4) R WT (LBS.) 45, Mj x Mj BENDS A R WT (LBS.) 22 A BENDS '/2- Mj x Mj (1,46) R WT (LBS.) 11 '/4- Mj X Mj BENDSQ/a2) A R WT (LBS.) 2 0.39 3.25 2.25 14 1.80 1.96 13 1.80 4.02 13 1.80 8.12 13 3 4 0.48 5.50 4.00 35 4.50 55 3.00 4.00 3.62 30 4.81 50 3.00 7.56 30 10.06 50 3.00 15.25 30 0.52 6.50 4.00 4.00 - 20.31 50 6 0.55 8.00 6.00 85 5.00 7.25 75 5.00 15.06 75 5.00 30.50 75 35.50 110 45.69 160 8 0.60 9.00 7.00 125 5.50 8.44 110 5.50 17.62 110 5.50 10 0.68 11.00 9.00 190 6.50 10.88 155 6.50 22.62 160 6.50 12 0.75 12.00 10.00 255 7.50 13.25 215 7.50 27.62 220 7.50 55.81 220 14 0.66 14.00 11.50 340 12.50 430 7.50 8.00 12.06 270 7.50 8.00 25.12 275 7.50 8.00 50.75 275 55.81 345 16 0.70 15.00 13.25 340 27.62 345 18 0.75 16.50 14.00 545 8.50 14.50 420 8.50 30.19 430 8.50 60.94 430 20 0.80 18.00 15.50 680 9.50 16.88 530 9.50 35.19 535 9.50 71.06 540 24 0.89 1.03 22.00 18.50 1025 21.50 1690 11.00 18.12 755 27.75 1380 11.00 37.69 765 57.81 1400 11.00 76.12 770 116.75 1410 30 25.00 15.00 15.00 15.00 36 42 1.15 28.00 24.50 2475 27.50 3410 18.00 35.00 2095 42.25 2955 18.00 72.88 2135 18.00 147.25 2145 1.28 31.00 21.00 21.00 88.00 3020 21.00 24.00 177.69 3035 48 1.42 34.00 30.50 4595 24.00 49.50 4080 24.00 103.06 4170 208.12 4190 U NOM. T SIZE A B R I I WI (LBS.) A I B R WT (LBS.) I A B It WT (LBS.) A B R - - WT (LBS.) 3 0.48 5.50' 6.50 13.50 4.00 14.50 4.50 35 3.00 11.00 3.62 30 3.00 4.00 11.00 7.56 30 3.00 4.00 5.00 11.00 15.25 30 0.52 0.55 50 4.00 12.00 4.81 45 7.25 70 12.00 10.06 13.00 15.06 45 70 12.00 20.31 45 70 - 6 8.00 16.00 6.00 80 5.00 13.00 5.00 13.00 30.50 8 0.60 0.68 9.00 11.00 17.00 7.00 19.00 9.00 120 190 5.50 6.50 13.50 14.50 8.44 105 10.88 155 5.50 6.50 13.50 17.62 14.50 22.62 105 160 5.50 6.50 13.50 35.50 14.50 45.69 105 160 10 12 0.75 12.00 20.00 22.00 10.00 11.50 255 325 7.50 7.50 15.50 15.50 13.25 12.06 13.25 215 255 7.50 7.50 15.50 27.62 15.50 25.12 220 7.50 15.50 55.81 15.50 50.75 16.00 55.81 19.00 76.12 220 260 14 0.66 14.00 260 7.50 8.00 16 0.70 15.00 23.00 12.50 410 8.00 11.00 16.00 19.00 23.00 320 8.00 16.00 27.62 325 325 730 24 0.89 22.00 30.00 18.50 985 18.12 715 11.00 19.00 37.69 725 1295 11.00 30 1.03 1.15 25.00 28.00 33.00 36.00 21.50 24.50 1 1585 2310 15.00 27.75 35.00 1275 1930 15.00 18.00 23.00 57.81 26.00 72.88 29.00 88.00 15.00 18.00 21.00 23.00 116.75 1305 36 18.00 21.00 26.00 1970 26.00 147.25 29.00 177.69 1980 42 1.28 31.00 39.00 27.50 3200 29.00 42.25 2745 21.00 2810 2825 UCA'T,I4,0I REGII.~11RE13TRADEAMILK OF SIAR PIPE PRODULII SiRE PIPE PRODUCTS HOUSTON CORPORATE ITOLI. FREE 1.900.999.3W9 MX 211.558-SORE pippodMA.on Page 22 MJ Accessories ANSI/AWWA C111/A21.11 1-Bolts, Double Ended Rods & Nuts HSLA STEEL SPECIFICATIONS: Bolts & Nuts are manufactured in accordance with ANSI / AWWA C 11 / A21.1 1. Material is High Strength Low Alloy Steel per ANSI/AWWA Cl 1 1/A21.1 1. Threads per ASME B1.1 unified standard coarse (Class 2A & 2B) MECHANICAL PROPERTIES yield Strength 45000 PSI (min) Elongation in 2in. 20% (mm) CHEMICAL PROPERTIES Carbon 0.20% Max Manganese 1.25% Max Sulfur 0.05% Max Nickel 0.25% Mm Copper 0.20% Mm Combined 1.25% Mm (Ni. Cu. Cr) BLUE BOLT/NUT/ROD T-Bolts. Rods & Nuts have fluoropolymer coating material which is VOC-compliant, resin-bonded, thermally cured and dry lubricant. COATING PHYSICAL PROPERTIES Film Thickness: 0.3 to 0.4 mil per coat Number of Coats: 3 to 4 coats Adhesion: 1 mm cross hatch test + 5 Pulls. Good knife resistance Cure Test: 50+Rubs with MEK. No substrate exposure Pencil Hardness: Pencil Hardness: 4-6H Volatile Organic Compounds 2.741bs/gal Stainless Steel 1-Bolts & Nuts ALLOYS SS 304 & SS 316 PER ASTM F593 SPECIFICATIONS: T-bolt dimensions are manufactured in accordance with ANSI / AWWA Cli 1 / A21.1 1. T-bolt alloys SS 304 and SS 316 per ASTM F593 Heavy Hex Nut Alloys SS 304 & SS 316 per ASTM F594. MECHANICAL PROPERTIES Tensile Strength: 85.000 PSI to 140.000 PSI Yield Strength: 45,000 PSI (mm) COATING SPECIFICATION Nuts have fluoropolymer coating material which is VOC-Compliant, resin-bonded, thermally cured and dry lubricant. COATING PHYSICAL PROPERTIES Film Thickness: 0.3 to 0.4 mil per coat • Pencil Hardness: 4-6H Number of Coats: 3 to 4 coats • Volatile Organic Compounds 2.74 lbs/gal Adhesion: 1 m cross hatch test + 5 Tape Pulls. • Continous use temperature - 356°F Cure Test: 50+ Rubs with MEK, no substrate exposure • Color: SS 304 is green. SS 316 is red A. AWWA MEMBER UCAT. 4 0! REUIOTEREDIRADEMARX OF ETA!! PIPE PRODUCTS STAR PIPE PRODUCTS HOUSTON CORPORATEITOU. FREE I.8(R.999.3059 FAX 181.558.9000 wwplp•pod,!!.•° Page 18 Accessories ANSI/AWWA C1111/A21.11 C Minimum 1/16-in x450hamf. ANN- MECHANICAL JOINT lBOLT IfTORQUE PIPE SIZE (IN) BOLT SIZE (IN) RANGE OF TORQUE (FT-LBS) 2-3 5/8 45-60 4-24 3/4 75-90 30-36 1 100-120 42-48 11/4 120-150 'These torque ranges are requirements ofAWWA C600 :s,ui1 (LOW iius' STEEL) BOLT I1Si NOM. SIZE A B C D THREADS PERIN. F H R 'Ax3 1.50 0.625 3.00 2.00 11 0.625 1.062 0.625 0.312 1/8x3½ 1.50 0.625 3.50 2.70 11 0.625 1.062 0.625 0.312 1/4x3½ 1.75 0.750 3.50 2.50 10 0.750 1.250 0.750 0.375 -Y4x4 1.75 0.750 4.00 300 10 0.750 1.250 0.750 0.375 3/4x4½ 1.75 0.750 4.50 3.00 10 0.750 1.250 0.750 0.375 '/4x5 1.75 0.750 5.00 3.00 10 0.750 1.250 0.750 0.375 10 3/4 x 5½ 1.75 0.750 5.50 3.70 0.750 1.250 0.750 0.375 lx 5½ 2.25 1.000 5.50 3.00 8 1.000 1.625 1.000 0.500 1 x6 2.25 1.000 6.00 3.00 8 1.000 1.625 1.000 0.500 2.000 1.250 1 V4 x6 2.50 1.250 6.00 3.00 7 1.250 0.625 1'/ax6½ 2.50 1.250 6.50 8.50 3.50 3.50 7 1.250 2.000 1.250 0.625 1 1/4 x 8½ 2.50 1.250 7 1.250 2.000 1.250 0.625 ---Minimum 1/16-in x 45Chamfer. 8/2 NINE ANTI-ROTATION T-H B ALLOY STEEL) C Ij,kI •LSj D E THREADS F H R NOM. A SIZE PERIN. 1.50 0.625 3.00 2.00 0.63 11 0.625 1.062 0.625 0.312 Vs x 3½ 1.50 0.625 3.50 230 0.63 ii 0.625 1.062 0.625 0.312 Y4x3½ 1.75 1.75 0.750 0.750 3.50 4.00 2.50 3.00 0.63 0.63 10 10 0.750 0.750 1.250 1.250 0.750 0.750 0.375 0.375 ~x4 1/4x4½ 1.75 0.750 4.50 3.00 0.63 10 0.750 1.250 0.750 0.375 Y4x5 1 1.75 1 0.750 5.00 1 3.00 1 0.63 1 10 1 0.750 1 1.250 0.750 0.375 #1 Page 19 RECISTEREDTR/DEMAP.K OF STAR PIPE PRODUCTS STAR PIPE PRODUCTS HOUSTON CORPOEATE TOIL FREE ,.SOU.999.3t*I9 FAX 181.555.9000 .ww.epippnduco.com FB HAH WAFER CHECK VALVE WEIGHTS 4 6 8 Lb 15.75 22.50 36.50 Kg 7.14 10.21 16.56 C.1 WAFER CHECK VALVES Rev. 2-03 Mueller Co.] UL /FM FIRE PROTECTION PRODUCTS A-21 02 Wafer Check Valve 4", 6", 8" 175 psi (1207 kPa) Working Pressure 350 psi (2413 kPa) Test Pressure Listed by Underwriters Laboratories, Inc. and Approved by Factory Mutual Research Corporation. PARTS LIST Catalog Parts Description Number Material Material Standard CW-1 Seat Ring Cast Bronze ASTM B584 CW-2 Body Cast Iron ASTM AI26 CW-3 0-Ring (2 req'd) Buna-N ASTM D2000 CW-4 Clapper Cast Bronze ASTM B584 CW-5 Bushing (2 req'd) Brass ASTM B16 CW-6 Spring Stainless Steel Type 302 CW-7 Hinge Pin Stainless Steel 1 Type 303 CW-8 Seal, Seat EP Rubber I ASTM D2000 CW-2 CW-1 CW- DIMENSIONAL INFORMATION FOR WAFER CHECK VALVES Size DIMENSIONS In. A (mm) In. B (mm) C In. (mm) In. D (mm) In. E (mm) 4 3.75 (95) 1.34 (34) 6.88 (175) 3.00 (76) 4.03 (102) 6 3.75 (95) 1.53 (39) 8.75 (222) 4.56 (116) 6.06 (154) 8 1 4.25 (108) 1.92 (49) 11.00 (279) 6.00 (152) 7.98 (203) WAFER CHECK VALVE ORDERING INFORMATION Specify: Quantity, Size and Catalog Number. WAFER CHECK VALVE PARTS ORDERING INFORMATION Specify: Quantity, Catalog Number, Part Name, Size of Valve, Catalog Number of Valve and Year Date of Valve. Page C-1-6 SPROUTS FARMERS MARKET UPTOWN BRESSI PROJECT IN THE CITY OF CARLSBAD FIRE SERVICE HYDRAULIC CALCULATIONS FROM THE STREET TO THE BASE OF RISER February 13, 2018 Prepared by: Dexter Wilson Engineering, Inc. 2234 Faraday Avenue Carlsbad, CA 92008 (760) 438-4422 Job No. 505-134 DEXTER WILSON ENGINEERING, INC. -cpvor:c Fi'-ii-Ic..- f' c P4L Ay- /0-0 C4.7DJ (s_atV.c IV_ d) ia., a- I /, 673 y b7 /ô rrs,- = 2-f Ad cv1t fy& aifev- 3" fl 11, S Lf 5 £ i (S .) /0 91 b(bD...) (') 4'- * 0 04t) ( tz.cc) (i, '.-73) 3fJet= f.3'1 Lcj- 1&.( e ' 13 fecc Lf87't/ 17 ,flS ,/Af'rJ.rA ((' /0 is NO. -- I uB.NCT I2-/-1t I DATE DEXTER WILSON ENGINEERING, INC. 3) LOSE y4e$ o/2 5J ai'r bfc s_crr /ç Ij -i , .L 5adJi 114) VO4L ( / 'a e/4— (vc:,e 17iTi4-L r if) 22- 21 aS4(( fafS •it - 'uz/ .0 /2z e•ef o, c) To M. L 19--e-fsfM vp L oJ- /.3 - 10 - - o•g_ F, py-cJ1j.< AV A.4(4 7 ,s /.. 3 D.S, 4V0 (f JOE NO. Ej&JACT DATE SHEET NO. I t. Y' 13-20 P. E. (Civil) License Review Manual, Volume V 'Ible 2.2 also shows the equivalent length of pipe for various fittings in a tabular form. 1b1e 2.2 Equivalent Length of Pipe for Various Fittings FW P1 Pip. MmW Um E6m LmO W Pip., Fl. ISli. 1. B1. Zh. 31.. 41.. 11. $1. 131.. 121.. 111.. 111.. 111.. 201.. lS 301.. $1.. 421.. 411.. Csslv,,. U 03 0.1 12 Li 2.3 U Ii 53 U U 10 10 Il 14 17 20 23 27 G. vIv,, 15 go 11 11 20 31 50 67 100 120 110 190 230 m = VS (00 500 600 710 790 GI. vals, oM II 17 43 54 00 110 160 210 504 350 AD 00 550 510 570 630 1.000 1,200 1,300 1015 272042 Si 00110140100150 VS M 2103444205W 5W 690 U 6.5111412 20105151 77 90110 M 150150200250 VS VS Raid.3.4 5.701211 27344451 67 15 00 120113130170200240270 lirdE In, .., 23 5.7 I 12 17 27 34 44 51 57 75 50 100 110 110 170 VS 240 273 aIdEi. ,L1 12223.59.15311 14 IS 2027 27 10 3442 52 61 72 42 50' E1b. dd. 1.5 LI 4.1 5.4 5.1 11 Il 21 50 31 31 42 11 52 63 90 90 110 130 IF E11. Ion rIia 1.1 1.1 U 33 5.1 53 U 14 13 20 27 27 70 31 42 52 61 7? 52 IW ROM MW U 6.110 IS U 50 1100 72 63120 113175150130170 VS 320 4? Eft.. U U U 2.5 3.7 5.0 7.4 10 13 15 17 11 21 27 50 31 44 52 00 1.52.33.04353101215 112027 275020 *5 526110 &dN 1/0 - I/l U Li 44 5.1 5.1 11 Ii 21 50 31 31 42 10 52 13 00 50 itO 120 4 1/0.12 LOU LI U4.3 5.3131315 11 21 24 50 3120 41 X90 11 1/0.3/4 0.3S$03121.7 U 33 ISiS U U 1013 1211 11 302727 5s CONMIN 1/0.1/4 031.2 U 233.7107.41013 15 17 15 23 2750 31 44 5200 030312 13 325.7735.712 33 15 17 1121 27 27 4055 1/0.314 13 03 03 I.? Li 2.3 33 43 U 53 5.4 10 10 12 14 11 20 20 (Ref Gallant, Robert N., "Sizing Pipe for Liquids and Vapors", Chemical Engineering, Page 104, February 24, 1969.) 9, ir n ! li 8:92 0 95 91 2° 00 oE 91 9" 0O ow r o Ot ! SPROUTSFARMERSMARKET BUILDTOSUITEPROJECT 0 7m > 0 Nm 'SPR FIRE PROTECTION PLAN b - -------- '-'th ,.. 10+62.04 PVT. DR. AISLE 'N'r +0 .00 P .DR.AlSLL 0 10+62. 4-3.001R PVT. DR. AISLE 'N' 10+03.00 PVT. DR. AISLE '0' LOT LINE 8"X8'%8"FLG TEE to Cj WI TB. (3) 8"GV, CD co 00 cli u- fn 2"BO & (2)2"MAR - - 70 LIJ 2 co 3c ——y ---r — (I) - - w 2 IN I — w LOT k L NE N , 47 BOUNDARY TT X ------------ BIC Lo I BLDG. A I d - I ~ 11 ~" "\ Ul II i od Ecli à I BLDG. B I cr OD—i a ., '- - SEE '' I I cn (1) $ !SHEET 10 ro " PLAN:PRIVATE DRIVE AISLE 'N' - (54 5JI : o TL • < - - - .—I >(j- q 0 V) —I0 Z. ) CONSTRUCTION NOTES J. ('4 - (13 SEE PLUMBING PLAN FOR CONTINUATION NOTE: FOR PERMITTED ENCROACHMENTS OF c GREASE INTERCEPTOR PER SEPARATE - PRIVATE STORM DRAIN sFwR BALCONIES PLUMBING PERMIT STAIRS, WALLS & ENHANCED PAVING. NOTE: REFER TO ENCROACHMENT AGREEMENT. EAGREE 2017-012 ON FILE WITH THE CITY. (1) THIS WATER PIPE SEGMENT INCLUDES 66.00 LF OF 8" STEEL PIPE PER CMWD W-34 (2) THIS WATER PIPE SEGMENT INCLUDES 43.62 LF OF 8" STEEL PIPE PER CMWD W-34 I S62O FRIARS ROAD J-17169-A (3) INSTALL TRACER WIRE CONTINUOUSLY ALONG WATER MAIN SAN DIEGO, CA921)0 PER SDRSD WP-01 619.291.0707 30 15 0 30 60 90 (FAX)619.291.4 165 PANY ,ickengineerinfi.com GRAPHIC SCALE 1' = 30' Rh.erslde. Orange- San LaIr Obirpo - Bakersfield- Sacramento - Plroe,nn - Tacron -5'SC,nIISre.tflS,.mnnma,,t FI,,slrl6gtlpl.Stacr WATER DATA NO. DELTA OR BRG. RADIUS LENGTH REMARKS 1 w8417'24'E 34JC' if' P/C C-900 (DR-18) 2 N724'WW 39062' 8'PVC C-900 (OR-18) 3_ N29'24'00"E 48.98' 8" P/C C-900 (DR-18) 4 N05423694' 110.29' 8"PVC C-900 (DR-18) 5 N0542'36W 175.25' 12' P/C C-900 (OR-IS) 505134SP.OUT ys'Si' FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIG A SUMMARY OF THE ORIGINAL DATA FOLLOWS PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE (FEET) (INCHES) 5 0 6 200.0 30.0 120.0 .00 680.00 9 6 10 300.0 24.0 120.0 .00 11 10 12 110.0 24.0 120.0 .00 101 10 122 140.0 12.0 120.0 .00 105 102 118 400.0 8.0 120.0 .00 109 118 114 180.0 8.0 120.0 .00 113 114 110 190.0 8.0 120.0 .00 117 110 176 140.0 8.0 120.0 .00 121 176 180 210.0 8.0 120.0 .00 125 176 172 240.0 8.0 120.0 .00 129 172 168 220.0 8.0 120.0 .00 133 164 168 200.0 8.0 120.0 .00 137 160 164 150.0 8.0 120.0 .00 141 156 160 90.0 8.0 120.0 .00 145 156 152 200.0 8.0 120.0 .00 149 148 152 280.0 8.0 120.0 .00 153 144 148 330.0 8.0 120.0 .00 157 140 144 100.0 8.0 120.0 .00 161 136 140 90.0 8.0 120.0 .00 165 134 136 40.0 8.0 120.0 .00 169 130 134 400.0 8.0 120.0 .00 171 126 130 180.0 8.0 120.0 .00 175 122 126 140.0 12.0 120.0 .00 179 102 122 110.0 12.0 120.0 .00 183 102 106 80.0 8.0 120.0 .00 187 106 110 170.0 8.0 120.0 .00 191 188 176 180.0 8.0 120.0 .00 195 126 184 260.0 8.0 120.0 .00 199 184 188 120.0 8.0 120.0 .00 203 188 156 200.0 8.0 120.0 .00 207 188 134 290.0 8.0 120.0 .00 211 136 154 180.0 8.0 120.0 .00 215 154 152 260.0 8.0 120.0 .00 301 12 102 140.0 12.0 120.0 .00 JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES 6 .00 .00 5 9 10 .00 .00 9 11 101 12 ;oo .00 11 301 102 1.50 428.00 105 179 183 301 106 1.50 424.00 183 187 110 1.60 419.00 113 117 187 114 1.50 420.00 109 113 118 1.50 419.00 105 109 122 1.50 426.00 101 175 179 126 1.50 423.00 171 175 195 130 1.50 423.00 169 171 Page 1 169 207 165 211 161 157 153 149 215 215 145 203 141 137 133 129 121 125 191 199 199 203 207 505 1345P.OUT 134 1.50 421.00 165 136 1.50 420.00 161 140 1.50 421.00 157 144 1.50 419.00 153 148 1.50 415.00 149 152 1.50 413.00 145 154 1.50 417.00 211 156 1.50 410.00 141 160 1.50 413.00 137 164 1.50 411.00 133 168 1.50 409.00 129 172 1.50 413.00 125 176 1.60 419.00 117 180 1.50 418.00 121 184 1.50 421.00 195 188 1.60 420.00 191 OUTPUT SELECTION: ALL RESULTS ARE OUTPUT EACH PERIOD 5 VALUES ARE OUTPUT FOR MAXIMUM AND MINIMUM PRESSURES THIS SYSTEM HAS 34 PIPES WITH 27 JUNCTIONS , 7 LOOPS AND 1 FGNS A SUMMARY OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS THE DEMANDS ARE CHANGED FROM ORIGINAL VALUES BY A FACTOR = 1.65 THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE JUNCTION NUMBER DEMAND 134 1073.00 THE RESULTS ARE OBTAINED AFTER 4 TRIALS WITH AN ACCURACY = .00498 Sprouts Fire Sprinkler Flow Analysis File: 5051345P Maximum Day Demands plus 1073 gpm at Nodes 134 for Sprouts PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 5 0 6 1130.42 .01 .00 .00 .51 .04 9 6 10 1130.42 .04 .00 .00 .80 .13 11 10 12 551.67 .00 .00 .00 .39 .03 101 10 122 578.75 .15 .00 .00 1.64 1.07 105 102 118 143.18 .23 .00 .00 .91 .58 109 118 114 140.70 .10 .00 .00 .90 .56 113 114 110 138.23 .10 .00 .00 .88 .54 117 110 176 394.35 .53 .00 .00 2.52 3.78 121 176 180 2.47 .00 .00 .00 .02 .00 125 176 172 139.09 .13 .00 .00 .89 .55 129 172 168 136.61 .12 .00 .00 .87 .53 133 164 168 -134.14 -.10 .00 .00 -.86 -.51 137 160 164 -131.66 -.07 .00 .00 -.84 -.50 141 156 160 -129.19 -.04 .00 .00 -.82 -.48 145 156 152 305.98 .47 .00 .00 1.95 2.36 149 148 152 -128.45 -.13 .00 .00 -.82 -.47 Page 2 JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE 6 .00 679.99 10 .00 679.95 12 .00 679.95 102 2.47 679.81 428.00 109.12 106 2.47 679.67 424.00 110.79 110 2.64 679.38 419.00 112.83 114 2.47 679.48 420.00 112.44 _- 118 2.47 679.58 419.00 112)2- 122 , 2.47 679.80 426.00 iU9.98 126 2.47 679.58 423.00 U.18 130 2.47 678.91 423.O04 110.90- 134 1073.00 677.46 421.00 111.13 136 4 2.47 677.54 420.00 111.60 140 /' 2.47 617.58 421.00 111.18 144 / 2.47 677.62 419.00 112.07 148 / 2.47 677.77 415.00 113.87 152 2.47 677.91 413.00 114.79 154 j 2.47 °V 677.69 417.00 112.97 156 I 2.47 678.38 410.00 116.30 160 2.47 678.42 413.00 115.02 164 2.47 678.50 411.00 115.92 168 2.47 678.60 409.00 116.83 172 2.47 678.72 413.00 115.14 176 2.64 678.85 419.00 112.60 180 2.47 678.85 418.00 113.03 184 2.47 678.88 421.00 111.75 188 2.64 678.56 420.00 112.04 MAXIMUM PRESSURES 168 2.47 678.60 409.00 116.83 156 2.47 678.38 410.00 116.30 164 2.47 678.50 411.00 115.92 172 2.47 678.72 413.00 115.14 160 2.47 678.42 413.00 115.02 MINIMUM PRESSURES 102 2.47 679.81 428.00 109.12 122 2.47 679.80 426.00 109.98 106 2.47 679.67 424.00 110.79 130 2.47 678.91 423.00 110.90 134 1073.00 677.46 421.00 111.13 Page 3 505134sP. OUT 153 144 148 -125.97 -.15 .00 .00 -.80 -.46 157 140 144 -123.50 -.04 .00 .00 -.79 -.44 161 136 140 -121.02 -.04 .00 .00 -.77 -.42 165' 134 136 -291.13 -.09 .00 .00 -1.86 -2.16 169 130 134 386.85 1.46 .00 .00 2.47 3.65 171 126 130 389.32 .66 .00 .00 2.48 3.69 175 122 126 721.05 .22 .00 .00 2.05 1.60 179 102 122 144.78 .01 .00 .00 .41 .08 183 102 106 261.24 .14 .00 .00 1.67 1.76 187 106 110 258.76 .29 .00 .00 1.65 1.73 191 188 176 -250.15 -.29 .00 .00 -1.60 -1.63 195 126 184 329.26 .70 .00 .00 2.10 2.71 199 184 188 326.78 .32 .00 .00 2.09 2.67 203 188 156 179.27 .18 .00 .00 1.14 .88 207 188 134 395.02 1.10 .00 .00 2.52 3.79 211 136 154 -172.58 -.15 .00 .00 -1.10 -.82 215 154 152 -175.06 -.22 .00 .00 -1.12 -.84 301 12 102 551.67 .14 .00 .00 1.56 .98 505134SP.OuT THE NET SYSTEM DEMAND = 1130.42 SUMMARY OF INFLOWS(+) AND OUTFLOWS(-) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE 5 1130.42 THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 1130.42 THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = .00 Page 4 @5/1 L i / / I - - z I ' 0 H z EL _ I I : a LiJ w I \\ 0 /• / I §NO \ç —!! 179 \\\/ t2 — I CL 113 PAD / II 1121 co L 5,J J .11 191 t I! " co \ - Ln 441 141 ' fit / # t PAD 00 Al 'I/I /I " - /— 'IL k4i6.33iI ., PADrt \ '9 _41fl3 YOV7c[ 1700 Lj En / / ES-F-LF876V Job Name Job Location Engineer Approval MasterSeri es® LF876V Double Check Detector Backflow Prevention Assemblies (Type II) Size: 21/2" - 8" (65mm - 200mm) The FEBCO MasterSeties LF876V Double Check Detector Assembly is specifically designed to protect against possible backpressure and backsiphonage conditions for non-health hazard (i.e., pollutant) application in accordance with Local Governing Water Utility Code. This Back-flow Assembly is primarily used on potable drinking water systems and fire sprinkler systems, where Local Governing Code mandates protection from non-potable quality water being pumped or siphoned back into the potable water system. Features Main Valve: Inline Serviceable Assembly Horizontal "N-Pattern" Installations Vertical-Up 'Z-Pattern" Installations No Special Tools Required for Servicing Captured Modular Spring Assembly Reversible & Replaceable Discs Field Replaceable Seats Ductile Iron Valve Body Design Stainless Steel Check Components Winterization feature with dc retainers and valve body drain ports Clapper Check Assembly Commonality between 1st & 2nd Check Components Captured 0-ring Design Auxiliary Bypass: Compact Bypass Design; Remains within Main Valve Assembly Profile Inline Serviceable 3/4' Backfiow Assembly No Special Tools Required for Servicing Field Replaceable Seats & Discs Contractor Approval Contractor's P.O. No. Representative Model LF876V Double Check Detector Assembly Specifications The FEBCO MasterSeries LF876V Double Check Detector Valve Assembly shall be installed on the potable water supply and at each point of cross-connection to protect against possible backpressure and backsiphonage conditions for non-health hazard (he., pollutant) applications. The assembly shall consist of a main line valve body composed of two (2) independently acting approved clapper style check modules with replaceable seats and disc rubbers. Servicing of both check modules does not require any special tools and are accessed through independent top entry covers. This assembly shall be fitted with approved UL/ FM inlet/outlet resilient seated shutoff valves and contain four (4) properly located resilient seated test cocks as specified by AWWA Standard C510. The auxiliary bypass line contains a 5/8"x3/4" Water Meter that complies with ANSl/AWrNA Standard C700 coupled with an approved check assembly. The bypass line is designed to detect leaks or unauthorized water usage of the water system while protecting against possible backpressure and backsiphonage conditions for non-health hazard (i.e., pollutant) application. The assembly shall be approved for horizontal and/or vertical-up installations while meeting the requirements of AV\ANA Standard C510 flow and pressure loss performance parameters. i'TS1ttD1 The information contained herein is not intended to replace the full product installation and safety information available or the experience of a trained product installer. You are required to thoroughly read all installation instructions and product safety information before beginning the installation of this product. t(l1tfOl Inquire with governing authorities for local installation requirements Detect Potential Underground Water Leaks "The wetted surface of this product contacted by consumable Detect Unauthorized Water Usage water contains less than 0.25% of lead by weight. FEBCO product specifications in U.S. customary units and metric are approdmate and are provided for reference only. For precise measurements, please contact FEBCO Technical Service. FEBCO reserves the right to change or modify product design, construction, specifications, or materials with- out prior notice and without incurring any obligation to make such changes and modifications on FEBCO products previously or subsequently sold. A WATTS Brand Options - Suffix OSY: UL!FM Approved OS&Y Gate Valves [ANSI/AWWA 0515 Compliant] CFM: Totalizing Cubic feet/mm 5/8"x 3/4" Water Meter [ANSI! AWWA 0700 Compliant] GPM: Totalizing Gallons/mm %x 3/4" Water Meter [ANSI! A\MNA C700 Compliant] LG: Less Shutoff valves; This is NOT an APPROVED ASSEMBLY Example Ordering Description: 4" LF876V-OSY-GPM - Valve Assembly fitted with OS&Y Shutoff Valves & Gallons per Minute Water Meter 4" LF876V-OSY-CFM - Valve Assembly fitted with OS&Y Shutoff Valves & Cubic Feet per Minute Water Meter Available Components Wye Strainer FDA Approved [ASME 616.1 Class 125 & AWWA Class D Flange] Series 611 Valve Setter MJ x MJ - Mechanical Joint x Mechanical Joint [AWWA C111/A21.11] MJ x FL - Mechanical Joint x Range [AWWA C111!A21.11; ASME 616.1 Class 125/AWWA Class D Flange] FLxFL— Rangex Flange [ASME B16.1 Class 125 & AWWA Class D Range] Materials Below is a general materials list of the Model LF876V. All assemblies size 21h" through 8" is similar in materials and construction. Please contact your local FEB00 Representative if you require further information. Main Valve Body: Ductile iron Grade 65-45-12 Coating: Fusion epoxy coated internal and external AWWA 0550-90 Shutoff Valves: OSY resent wedge gate valve AV\ANA 0515 PL/FM) Check Seats: Stainless Steel Disc Holder: Stainless Steel Elastomer Disc: Silicone Spring: Stainless Steel Clamp: AWWA 0606 Approvals — Standards: Approved by the Foundation for Cross-Connection Control and Hydraulic Research at The University of Southern California [F000HR-USC] ASSE 1048 Listed **UL Classified [US & Canada] **FM Approved IAPMO/cUPC AWWA Standard 0510 Compliant End Connections: Compliant to ASME 816.1 Class 125 & AWWA Class D Flange **Assembly configured with UL/FM Approved OS&Y RW Gate Valves. Less gate valve assemblies are not UL/FM approved configurations. Assembly Flow Orientation: Horizontal (N-Pattern 21/2" - 8") - Approved by F000HR-USC, ASSE, cULus, FM, IAPMO!cUPC Vertical Up (Z-Pattern 21/2' - 8') - Approved by F000HR-USC, ASSE, cULus, FM, IAPMO!cUPC ® <8:; Approved C (,) US 1048 B64.5 Pressure - Temperature Max. Working Pressure: 175psi (12.1 bar) Mm. Working Pressure: lOpsi (0.7 bar) Hydrostatic Test Pressure: 350ps1 (24.1 bar) Hydrostatic Safety Pressure: 700psi (48.3 bar) Temperature Range: 33°F - 140°F [0.5°C- 60°C] Continuous Cock 14 Dimensions - Weights Size: 21/2" - 8" Below are the nominal dimensions and physical weights for. the Model LF876V size 2W through 8. Allowances must be made for normal manufacturing tolerances. Please visit our websfte to download a copy of this products installation instructions, or contact your local FEBCO Representative for more information. Model LF876V Standard Orientation (N-Pattern) Model LF876V Vertical Orientation (Z-Pattern) Note: The Series LF876V is shipped in the standard (N-Pattern) orientation as. shown above. Gate Valve Side View Clearance LF876V DIMENSIONS WEIGH—T!-1 in. mm A in. mm B in. mm 0 in. mm 0 in. mm in. E mm F in. mm G in. mm in. H mm in. I mm J in. mm in. mm L in. mm OSY lbs. kg. 21h 65 291A 740 121h 318 6¼ 159 251/4 642 17½ 445 13% 346 271/4 692 5½ 140 11% 283 3½ 89 16% 416 11112 292 216 98 3 80 29½ 740 121h 318 61/4 159 25% 654 17Y4 451 14½ 359 28¼ 718 5½ 140 11½ 283 33/4 95 221/4 565 1116 292 242 110 4 100 31½ 791 14 356 7 178 271/4 705 183/4 476 15½ 394 31 787 6 152 111h 283 46 114 231/4 591 13 330 347 157 6 150 3534 908 16 406 8 203 32% 831 221A 562 18% 473 37Y4 946 71/4 184 12½ 316 5½ 140 301A 765 13 330 529 240 8 200 403/4 1035118V2 470 91/4 235 36% 933 25½ 638 203/4 527 141½ 10541 81h 216 14 356 1 61/4 172 371/4 959 1 14h 368 827 375 Notes: Indicates nominal dimensions with OSY Gate Valves (Full Open Position) Indicates weight of complete Backf low Assemblies with specified Gate Valves 6" 1F876V psi Service flow Rated flaw UL Rated flaw logpm 1pm fps Service flow Rated Row *Ul. Rated flow _ 400 800 1200 1600 2000 2400 gpm 1514 3028 4543 6057 7571 9085 1pm 7.5 10.5 15.3 fps 1,073 gpm Performance Flow capacity chart identifies valve performance based upon rated water Velocity up to 20fp5 Maximum service flow rate is determined by maximum rated Velocity of 7.5fps. A\MNA Manual M-22 (Appendix C) recommends that the maximum water Velocity in the services be not more than 1 Ofps. UL flow rate is determined by typically rated Velocity of 15 feet/sec. Capacity N-Pattern Pat em 2½" 1F876V PSI Service flow Rated flow IJL Rated flow 32 20 I I 18 I I 16 14 I I 2 12 1 I 10US i 0 25 50 75 100 125 150 175 200 225 250 275 300 325 350gpm 284 568 852 1136 1pm 7.5 14.7 22.0 fps psi 1F876V Service flow Rated flow *UL Rated flew 22 20 I I I 18 I I I 16 I I .5 14 I I I D 12 I 1 I 6 41 - I I I o I 0 psi 50 100 1F876V 379 150 200 250 757 7.5 Service flow 300 350 400 1136 1514 14.5 Rated flaw 450 500 gpm 1pm 22.0 foe 16 psi los *UL Rated flow 18 - 16 14 12 10 "- 6 - 2 o I I I I I 100 379 200 300 400 1136 - 7.5 500 600 1893 12.8 700 800gpm 2650 1pm 19.1 fps Pipe Support I (furnished by customer) for valve weight only. Vertical Orientation Z-Pattem" Flow curve Z Standard Orrentation N-Pattern Flow Curve N A WATTS Brand ES-F-LF876V 1515 USA. Tel: (800) 767-1234 • Fax: (800) 788-4491 • FEacoonline.com Canada: Tel: (905) 332-4090 • Fax: (905) 332-7068 • FEBcoonne.ca Latin America: (52)81-1001-8600 - Fax: (52) 81-8000-7091 • FEBcOonline.com © 2017 FEBCO / SEE SHEET 11 W. 41i ':/' \L LOT 3 PER MAP NO. DC. B FF-423. 10 I / / ti 147\ñ 1 /'4Zhi II'!! ft l ITEB csoDa I_________ II LOT 29 OF L(UOVTS I I rASH COMPACTOR 1'° / LOT2 FF I PROP RTY STOP DRAW SEE DVGLND.5Q2-0& FOR PUBLIC CH-SIrt VATE AHD At ; ---- — — - N_ LOTI CONSTRUCTION NOTES PER SEPARATEPLLW.%G PERMIT I I 6Q ®"DOUBLE CHECK DETECTOR NRXIMS MODEL 4O OA1 PER ?D22 ID 01 20 40 LtI WITH BC FLANGE Co"'ECTIO' PER CRAPHC SCALE 2W :IseDAGG RISER ! ZI RILL ow. all( t,'o Job Name - Job Location Engineer - Approval - Contractor Approval Contractor's P.O. No. Representative ES-A-lnBuildinqRiser Series IBR In-Building Risers Customizable Sizes: 4" -10" (100-250mm) Tr5T CAP 01 6'x6' standard length (custom lengths from 3'— 20' available) Features Cost savings Corrosion resistant stainless steel construction, type 304 Ease of installation and light weight allows one person to position and handle the riser Minimal site preparation; joint restraint one- piece construction reduces time and labor; no missing parts, no leaks; easily identifiable for approvals Includes Test Cap and Coupler ULJFM approved Sizes: available in 4' - 10" (100-250mm) with various lengths to meet local require- ments Series IBR In-Building Risers are used to connect the main fire supply to the building overhead fire system. The fitting passes under the foundation without joints and ex- tends up through the floor. Provided with installation tabs, the unit has a CIPS (Cast Iron Pipe Size) coupler for easy connection to the underground supply (AVW'JA C900 PVC and Ductile Iron Pipe) and industry standard grooved-end connection (A\/W\IA C606) on the building side for easy connection to the overhead fire sprinkler system. The IBR features Lead Free* construction to comply with Lead Free* installation requirements. Ames In-Building Risers are precision engineered and manufactured to provide exceptional reliability and reduce installation time & labor costs associated with field assembly. In accordance with NFPA 24, the UL/FM approved In-Building Risers replace numerous fittings, elbows & spools and reduces the possibility of leaks or failure in comparison to traditional installation methods and materials. Factory tested integrity ensures the highest quality installation. The use of stainless steel significantly increases the reliability and life of the riser. The wetted surface of this product contacted by consumable water contains less than 0.25% of lead by weight. Designed to meet NFPA 24 AV\M/A C900 Inlet/DIP AWWA C606 Outlet Ames Fire & Waterworks product specifications in U.S. customary units and metric are appmslmate and are prodded for reference only. For precise measure- ments, please contact Ames Fire & Waterworks Technical Service. Ames Fire & Waterworks reserves the right to change or modify product design, construction, specifications, or materials without prior notice and without incurring any obligation to make such changes and modifications on Ames Fire & Waterworks products previously or subsequently sold. Is FIRE &WATERWORKS A WATTS Brand Specifications In-Building Riser shall be installed as indicated on the plans. Riser shall be composed of a single extended 90 degree fitting of fabricated 304 stainless steel tubing, maximum working pressure 200p5i (14 bar). The fitting shall have a grooved-end connection on the outlet (building) side and a ClPS coupler on the inlet (underground) side. The grooved end shall include a coupler and cap to facilitate testing of the underground pip- ing. The In-Building Riser shall be an Ames Fire & Waterworks Series IBR. Approvals Fittings FM class 1920 UL HKQA (4-10") < aFM > SUL Dimensions - Weights A J7 Grooved End (Flange Optional) I CIPS Coupling Bracket C SIZE (ON) WEIGHT in. mm A(OD) in. tern B ft cm C ft cm lbs. kg 4 100 4'/2 114 6 183 6 183 71 32 6 150 61/8 168 6 183 6 183 98 44 8 200 1 8/t 219 6 183 1 6 183 1 129 59 10 250 1 103/4 273 6 183 1 6 183 1 202 92 Each B (vertical) and C (horizontal) leg is customizable aoorovals. Consuit with your factory reoresentabve from 3' to 20' with UL/FM for details. A A M E S FIRE & WATER WORKS A WATTS Brand Standards NFPA - Designed to allow the contractor to conform to NFPA 24 Where a riser is close to building foundations, underground fittings of proper design and type shall be used to avoid pipe joints being located under the foundations. End Connections Horizontal End: Mates with Ductile Iron Pipe and A"IWVA C900 Pipe (PVC Pipe with Ductile Iron Pipe Equivalent OD's) Utilizes Gasket conforming to UL 157 with "Lock in" gasket configuration .1PAt) MATING PIPE in. mm in. mm 4 100 4.8 122 6 150 6.9 175 8 200 9.1 230 10 250 11.1 282 Vertical End: Meets AWINA C-606 dimensions for roll grooved pipe Meets AWVA C-207 class D for flanges Ratings Meets AWWA C-900 pressure class 200, DR 14 Pipe Testing Welds are 100% leak tested at the factory SIZE DESIGN PROOF in. mm psi bar 4 100 1000 70 6 150 1000 70 8 200 800 56 10 250 1 800 56 Inquire with governing authorities for local installation requirements NOTICE The information contained herein is not intended to replace the full product installation and safety information available or the experience of a trained product installer. You are required to thoroughly read all installation instructions and product safety information before beginning the installation of this product. USA: Backflow Tel: (978) 689-6066 • Fax: (978) 975-8350 • PmesFirewater.com USA: Control Valves Tel: (713) 943-0688 • Fax: (713) 944-9445 • AmesFireWater.com Canada: Tel: (905) 332-4090 • Fax: (905) 332-7068 • A:nesRreWater.ca Latin America: Tel: (52) 81-1001-8600 • Fax: (52) 81-8000-7091 • AmesFireWater.com ES-A-lnBuildingRiser 1626 © 2016 Ames Fire & Waterworks Job Name Contractor Job Location Approval ES-F Engineer Approval MasterSeries® LF876V Double Check Detector Backflow Prevention Assemblies (Type II) Size: 21/2" - 8" (65mm - 200mm) The FEBCO MasterSenes LF876V Double Check Detector Assembly is specifically designed to protect against possible backpressure and backsiphonage conditions for non-health hazard (i.e., pollutant) application in accordance with Local Governing Water Utility Code. This Backflow Assembly is primarily used on potable drinking water systems and fire sprinkler systems, where Local Governing Code mandates protection from non-potable quality water being pumped or siphoned back into the potable water system. Features Main Valve: Inline Serviceable Assembly Horizontal"N-Pattern" Installations Vertical-Up '2-Pattern" Installations No Special Tools Required for Servicing Captured Modular Spring Assembly Reversible & Replaceable Discs Field Replaceable Seats Ductile Iron Valve Body Design Stainless Steel Check Components Winterization feature with disc retainers and valve body drain ports Clapper Check Assembly Commonality between 1st & 2nd Check Components Captured 0-ring Design Auxiliary Bypass: Compact Bypass Design; Remains within Main Valve Assembly Profile Inline Serviceable 3/4' Backflow Assembly Contractor's P.O. No. Representative Model LF876V Double Check Detector Assembly Specifications The FEBCO MasterSeries LF876V Double Check Detector Valve Assembly shall be installed on the potable water supply and at each point of cross-connection to protect against possible backpressure and backsiphonage conditions for non-health hazard (i.e., pollutant) applications. The assembly shall consist of a main line valve body composed of two (2) independently acting approved clapper style check modules with replaceable seats and disc rubbers. Servicing of both check modules does not require any special tools and are accessed through independent top entry covers. This assembly shall be fitted with approved UL/ FM inlet/outlet resilient seated shutoff valves and contain four (4) properly located resilient seated test cocks as specified by AWVVA Standard 0510. The auxiliary bypass line contains a 5/8"x3/4" Water Meter that complies with ANSI/AWWA Standard C700 coupled with an approved check assembly. The bypass line is designed to detect leaks or unauthorized water usage of the water system while protecting against possible backpressure and backsiphonage conditions for non-health hazard (i.e., pollutant) application. The assembly shall be approved for horizontal and/or vertical-up installations while meeting the requirements of AWNA Standard C51 0 flow and pressure loss performance parameters. I NOTICE I The information contained herein is not intended to replace the full product installation and safety information available or the experience of a trained product installer. You are required to thoroughly read all installation instructions and product safety information before beginning the installation of this product. No Special Tools Required for Servicing 11111ROMM Field Replaceable Seats & Discs Inquire with governing authorities for local installation requirements Detect Potential Underground Water Leaks *The wetted surface of this product contacted by consumable Detect Unauthorized Water Usage water contains less than 0.25% of lead by weight. FEBCO product specifications in U.S. customary units and metric are approximate and are provided for reference only. For precise measurements, please contact FEBCO Technical Service. FEBCO reserves the right to change or maCfly product design, construction, specifications, or materials with- out prior notice and without incurring any obligation to make such changes and modifications on FEBCO products previously or subsequently sold. A WAITS Brand Options - Suffix OSY: ULJFM Approved OS&Y Gate Valves [ANSI/AVWIA 0515 Compliant] CFM: Totalizing Cubic feet/min %"x 3/4" Water Meter [ANSI! A\MNA 0700 Compliant] GPM: Totalizing Gallons/mm 5/8"x 3/4' Water Meter [ANSI! AWNA C700 Compliant] LG: Less Shutoff valves; This is NOT an APPROVED ASSEMBLY Example Ordering Description: 4" LF876V-OSY-GPM - Valve Assembly fitted with OS&Y Shutoff Valves & Gallons per Minute Water Meter 4" LF876V-OSY-CFM - Valve Assembly lifted with OS&Y Shutoff Valves & Cubic Feet per Minute Water Meter Available Components Wye Strainer FDA Approved [ASME B1 6.1 Class 125 & AWvVA Class D Range] Series 611 Valve Setter MJ x MJ - Mechanical Joint x Mechanical Joint [AWWAC111/A21.111 MJ x FL - Mechanical Joint x Flange [A'MNAC111/A21.11; ASME B16.1 Class 125!A'MNA Class D Flange] FL x FL - Flange x Range [ASME B16. 1 Class 125 & AWWA Class D Range] Materials Below is a general materials list of the Model LF876V. All assemblies size 21/2 through 8" is similar in materials and construction. Please contact your local FEB00 Representative if you require further information. Main Valve Body: Ductile iron Grade 65-45-12 Coating: Fusion epoxy coated internal and external Approvals - Standards: Approved by the Foundation for Cross-Connection Control and Hydraulic Research at The University of Southern California [FCCCHR-USC] ASSE 1048 Listed -UL Classified [US & Canada] **FM Approved IAPMO/cUPC A'MNA Standard C510 Compliant End Connections: Compliant to ASME B16.1 Class 125 & AVWVA Class D Flange Assembly configured with UL/FM Approved OS&Y RW Gate Valves. Less gate valve assemblies are not UL/FM approved configurations. Assembly Flow Orientation: Horizontal (N-Pattern 21/2" - 8') - Approved by FCCCHR-USC, ASSE, cULus, FM, IAPMO/cUPC Vertical Up (Z-Pattern 21/2" —8") - Approved by F000HR-USC, ASSE, cULus, FM, IAPMO/cUPC C) ® <e;:; \ssI Approved cus 1048 864.5 Pressure - Temperature Max. Working Pressure: 175p5i (12.1 bar) Min. Working Pressure: lOpsi (0.7 bar) Hydrostatic Test Pressure: 350psi (24.1 bar) Hydrostatic Safety Pressure: 700psi (48.3 bar) Temperature Range: 33°F - 140°F [0.5°C- 60°C] Continuous Shutoff Valves: Check Seats: Disc Holder: Elastomer Disc: Spring: Clamp: AWNA 0550-90 OSY resilient wedge gate valve AVWVA 0515 (UL/FM Stainless Steel Stainless Steel Silicone Stainless Steel A\MNA 0606 Dimensions - Weights Size: 21/211 - 81 Below are the nominal dimensions and physical weights for the Model LF876V size 21/2' through 8". Allowances must be made for normal manufacturing tolerances. Please visft our websfte to download a copy of this products installation instructions, or contact your local FEBCO Representative for more information. Model LF876V Standard Orientation (N-Pattern) Model LF876V Vertical Orientation (Z-Pattern) Note: The Senes LF876V is shipped in the standard (N-Pattern) orientation as shown above. Gate Valve Side View Clearance LF876V [SIZE (ON) DIMENSIONS WEIGHT"1 in. mm A in. mm B In. mm c in. mm 0 in. mm E in. mm F in. mm .6 in. mm in. H mm in. I mm J in. mm in. mm L in. mm OSY lbs. kg. 2½ 65 29½ 740 12½ 318 6¼ 159 25Y4 642 17Y2 445 13% 346 27¼ 692 51/2 140 11¼ 283 3½ 89 16% 416 111/2 292 216 98 3 80 29¼ 740 121/2 318 61/4 159 25Y4 654 17% 451 14½ 359 28/4 718 5½ 140 11½ 283 3Y4 95 221/4 565 111/2 292 242 110 4 100 31Y8 791 14 356 7 178 273/4 705 18/4 476 15½ 394 31 787 6 152 11½ 283 41/2 114 23/4 591 13 330 347 157 6 150 35Y4 908 16 406 8 203 32Y4 831 22½ 562 18% 473 371/4 946 71/4 184 12½ 316 51/2 140 30¼ 765 13 330 529 240 8 200 4034 1035118'/2 470 1 9¼ 235 1 36% 933 1 25/8 638 i 2034 527 1 41½ 1054 8½ 216 1 14 356 6Y4 172 3734 959 14½ 368 827 375 Notes: * Indicates nominal dimensions with OSY Gate Valves (Full Open Position) Indicates weight of complete Backflow Assemblies with specified Gate Valves Standard Orientation N-Pottern Row Curve N Pipe Support (furnished by customer) for valve weight only. vertical Cuenlaflon Z-Pattern Row Curve Z Performance Flow capacity chart identifies valve performance based upon rated water Velocity up to 20fps Maximum service flow rate is determined by maximum rated Velocity of 7.5fps. AWWA Manual M-22 (Appendix C) recommends that the maximum water Velocity in the services be not more than 1 Ofps. UL flow rate is determined by typically rated Velocity of 15 feet/sec. Capacity N-Pattern 2½" 1F876V PSI Service flow Rated Row lii Rated flow 22 20 I I 18 I I 10 025 SO 75100125150175200225250275300325350gpm 284 568 852 1136 (pm 7.5 14.7 22.0 fps 1F876V PSI Service Row Rated flow *UL Rated Flow 22 20 18 I - 16 I - 8.S 14 I - 01 U 12 I 10 - 0 O 50 100 379 1F876V psi 150 200 757 7.5 Service flow 250 300 350 400 1136 1514 14.5 Rated flow - 450 500 gpm 1pm 22.0 fps lii Rated flow 18 16 I I 14 I I I 12 1O : Vi o 100 200 300 379 1136 7.5 400 500 600 1893 12.8 700 800gpm 2650 1pm 19.1 fps 6" 1F876V psi Service Flow Rated flow *UL Rated flow 18 16 I I 14 I I I I 12 10 I I I H : 4. -- 2 I I 0 I I I I 0 200 400 757 600 800 1000 1200 2271 3785 7.5 11.4 1400 1600 gpm 5300 (pm 17.0 fps 8" LF876V psi Service flow Rated flow UL Rated flow 18 16 14 12 10 015 8 6 4 0 0 400 800 1200 16010 2000 2400 gpm 1514 3028 4543 6057 7571 9085 1pm 75 10.5 153 fps )Pmff~rjw A WATTS Brand ES-F-LF876V 1515 USA- Tel: (800) 767-1234 • Fax: (800) 788-4491 • FEBCOonIine.com Canada: Tel: (905) 332-4090 • Fax: (905) 332-7068 • FEBCOonhine.ca Latin America: (52) 81-1001-8600 • Fax: (52) 81-8000-7091 • FEBCOonhine.com ©2O17FEBCO tElgian® ENGINEERING & CONSULTING' ENGINEERS I CONSULTANTS I ANALYSTS I ASSESSORS October 6, 2017 Min Kang, Project Manager Shea Properties 130 Vantis, Suite 200 Aliso Viejo, CA 92656 Email: min.kang@sheaproperties.com RE: Shea Properties - NE Corner of Gateway Rd. & El Fuerte St. Water Supply Test and Site Flow Analysis Carlsbad, CA Dear Mr. Kang: The requested updated water supply test and site flow analysis for the subject project are detailed in this report and submitted for review and posting. SUMMARY OF RESULTS BUILDING B (CONCLUSION Cl-B - AS DESIGNED) Fireline Base of Riser (BOR) static pressure at Finish Floor Elevation (FFE): 103.5 psi Fireline BOR high static pressure at FFE: 120.5 psi Fireline BOR residual pressure at FFE: 102 psi @ 600 gpm Assumed Fireline BOR FFE: 423-ft. AMSL Safety Factor Utilized in Calculations: 10% = -13.0 psi Fireline Backflow Preventer Required: Double Check Detector Type Backflow Preventer Located Above Ground At The Property Line to the building (6-inch AMES 3000 SS is assumed for calculations). A fire pump WILL NOT be required for fire sprinkler demands. A water storage tank WILL NOT be required for fire sprinkler demands. TELGIAN ENGINEERING & CONSULTING ENGINEERS • CONSULTANTS • ANALYSTS • ASSESSORS EMERGENCY MANAGEMENT & OPERATIONS CONTINUITY • ENGINEERING, DESIGN & CONSTRUCTION ENVIRONMENTAL, HEALTH & SAFETY • FIRE PROTECTION ENGINEERING • RISK MANAGEMENT & LOSS CONTROL • SECURITY RISK CONSULTING 4001 Kennett Pike, Suite 308, Wilmington, Delaware 19807 www.telgian.Com WATER SUPPLY SITE SURVEY REPORT SHEA PROPERTIES NE CORNER OF GATEWAY RD. & EL FUERTE ST. CARLSBAD, CA SUMMARY OF RESULTS BUILDING A (CONCLUSION Cl-A - AS DESIGNED) Fireline Base of Riser (BOR) static pressure at Finish Floor Elevation (FFE): Fireline BOR high static pressure at FFE: Fireline BOR residual pressure at FFE: Assumed Fireline BOR FFE: Safety Factor Utilized in Calculations: TEST DATE: 02/24/17 104 psi 121 psi 103 psi @ 600 gpm 421-ft. AMSL 10% = -13.0 psi Fireline Backflow Preventer Required: Double Check Detector Type Backflow Preventer Located Above Ground At The Property Line to the building (6-inch AMES 3000 SS is assumed for calculations). Afire pump WILL NOT be required for fire sprinkler demands. A water storage tank WILL NOT be required for fire sprinkler demands. SUMMARY OF RESULTS BUILDING C (CONCLUSION Cl-C - AS DESIGNED) Fireline Base of Riser (BOR) static pressure at Finish Floor Elevation (FFE): 102.5 psi Fireline BOR high static pressure at FFE: 119.5 psi Fireline BOR residual pressure at FFE: 99.0 P51 @ 600 gpm Assumed Fireline BOR FFE: 425-ft. AMSL Safety Factor Utilized in Calculations: 10% = -13 psi Fireline Backflow Preventer Required: Double Check Detector Type Backflow Preventer Located Above Ground At The Property Line to the building (6-inch AMES 3000 SS is assumed for calculations. A fire pump WILL NOT be required for fire sprinkler demands. A water storage tank WILL NOT be required for fire sprinkler demands. SUMMARY OF RESULTS BUILDING H (CONCLUSION Cl-H - AS DESIGNED) Fireline Base of Riser (BOR) static pressure at Finish Floor Elevation (FFE): 104 psi Fireline BOR high static pressure at FFE: 121 psi Fireline BOR residual pressure at FFE: 102 psi @ 600 gpm Assumed Fireline BOR FFE: 422-ft. AMSL Safety Factor Utilized in Calculations: 10% = 13 psi Fireline Backflow Preventer Required: Double Check Detector Type Backflow Preventer Located Above Ground At The Property Line to the building (6-inch AMES 3000 SS is assumed for calculations). A fire pump WILL NOT be required for fire sprinkler demands. A water storage tank WILL NOT be required for fire sprinkler demands. TELGIAN ENGINEERING & CONSULTING ENGINEERS • CONSULTANTS • ANALYSTS • ASSESSORS EMERGENCY MANAGEMENT & OPERATIONS CONTINUITY • ENGINEERING, DESIGN & CONSTRUCTION ENVIRONMENTAL, HEALTH & SAFETY • FIRE PROTECTION ENGINEERING • RISK MANAGEMENT & LOSS CONTROL • SECURITY RISK CONSULTING 4001 Kennett Pike, Suite 308, Wilmington, Delaware 19807 www.telgian.com WATER SUPPLY SITE SURVEY REPORT SHEA PROPERTIES NE CORNER OF GATEWAY RD. & EL FUERTE ST. CARLSBAD, CA SUMMARY OF RESULTS BUILDING G (CONCLUSION C1-G - AS DESIGNED) Fireline Base of Riser (BOR) static pressure at Finish Floor Elevation (FFE) Fireline BOR high static pressure at FFE: Fireline BOR residual pressure at FFE: Assumed Fireline BOR FFE: Safety Factor Utilized in Calculations: TEST DATE: 02/24/17 104.5 psi 121.5 psi 101 psi @ 600 gpm 420-ft. AMSL 10% = -13.0 psi Fireline Backflow Preventer Required: Double Check Detector Type Backflow Preventer Located Above Ground At The Property Line to the building (6-inch AMES 3000 SS is assumed for calculations). A fire pump WILL NOT be required for fire sprinkler demands. A water storage tank WILL NOT be required for fire sprinkler demands. SUMMARY OF RESULTS BUILDING D (CONCLUSION C1-D - AS DESIGNED) Fireline Base of Riser (BOR) static pressure at Finish Floor Elevation (FFE): 104.5 psi Fireline BOR high static pressure at FFE: 121.5 psi Fireline BOR residual pressure at FFE: 101 psi @ 600 gpm Assumed Fireline BOR FFE: 420-ft. AMSL Safety Factor Utilized in Calculations: 10% =.-13.0 psi Fireline Backflow Preventer Required: Double Check Detector Type Backflow Preventer Located Above Ground At The Property Line to the building (6-inch AMES 3000 SS is assumed for calculations). A fire pump WILL NOT be required for fire sprinkler demands. A water storage tank WILL NOT be required for fire sprinkler demands. SUMMARY OF RESULTS BUILDING E (CONCLUSION C1-E - AS DESIGNED) Fireline Base of Riser (BOR) static pressure at Finish Floor Elevation (FFE): 104.5 psi Fireline BOR high static pressure at FFE: 121.5 psi Fireline BOR residual pressure at FFE: 101 psi @ 600 gpm Assumed Fireline BOR FFE: 420-ft. AMSL Safety Factor Utilized in Calculations: 10% = -13.0 psi Fireline Backflow Preventer Required: Double Check Detector Type Backflow Preventer Located Above Ground At The Property Line to the building (6-inch AMES 3000 SS is assumed for calculations). A fire pump WILL NOT be required for fire sprinkler demands. A water storage tank WILL NOT be required for fire sprinkler demands. TELGIAN ENGINEERING & CONSULTING ENGINEERS • CONSULTANTS • ANALYSTS • ASSESSORS EMERGENCY MANAGEMENT & OPERATIONS CONTINUITY • ENGINEERING, DESIGN & CONSTRUCTION ENVIRONMENTAL, HEALTH & SAFETY • FIRE PROTECTION ENGINEERING • RISK MANAGEMENT & LOSS CONTROL • SECURITY RISK CONSULTING 4001 Kennett Pike, Suite 308, Wilmington, Delaware 19807 www.telgian.com WATER SUPPLY SITE SURVEY REPORT SHEA PROPERTIES NE CORNER OF GATEWAY RD. & EL FUERTE ST. CARLSBAD, CA SUMMARY OF RESULTS BUILDING F (CONCLUSION Cl-F - AS DESIGNED) Fireline Base of Riser (BOR) static pressure at Finish Floor Elevation (FFE) Fireline BOR high static pressure at FFE: Fireline BOR residual pressure at FFE: Assumed Fireline BOR FFE: Safety Factor Utilized in Calculations: TEST DATE: 02/24/17 107 psi 124 psi 103 psi @600gpm 415-ft. AMSL 10% = -13.0 psi Fireline Backflow Preventer Required: Double Check Detector Type Backflow Preventer Located Above Ground At The Property Line to the building (6-inch AMES 3000 SS is assumed for calculations). A fire pump WILL NOT be required for fire sprinkler demands. A water storage tank WILL NOT be required for fire sprinkler demands. Information Gathered: Jennifer R. Mael, PE, Mission Consulting performed a hydraulic simulation of Carlsbad Municipal Water District's distribution system. This analysis is based on results from that model. Water main sizes and layout were provided by Rick Engineering. The drawing C-4, dated June 11/24/14 with revisions dated 5/27/2016. Telgian was unable to obtain information on backflow prevention requirements from the City of Carlsbad Fire Department, however based on previous waterflow analysis completed in the city, the backflow preventer for fire service required is a double check detector assembly (AMES 3000 SS). This device is to be located above ground at the property line. The Site: This site is located in the southeast portion of Carlsbad, along the west side of El Fuerte St, northeast of Gateway Road. A 24-inch PVC water main is located on El Fuerte St. and it is assumed that it is to supply a 12-inch loop around the property. The arrangement of these lines in the immediate vicinity of the property is shown on Attachment #1 - Location Sketch. Additional details on water mains serving the area are contained on the enclosed Attachment #2 - Area Water Map. It is assumed sprinkler protection for each building will be provided by a 6-inch lead-in from the 12-inch and 8-inch fire line, east of the property, as shown on Attachment #1. The Public System: The City of Carlsbad is provided water by the Carlsbad Municipal Water District, however due to a heightened level of security, specific information regarding the distribution system would not be provided. Through material gathered online in the 2015 Urban Water Management Plan, it was determined that the Carlsbad Municipal Water District (CMWD) currently receives 100% of its potable water supply from San Diego County Water Authority (SDCWA) through four treated waterturnouts. Two of the turnouts, Connections No. land No. 2, are direct connections to SDCWA's Second Aqueduct. Connection No. 1 supplies only CMWD, and Connection No. 2 supplies CMWD, Vallecitos Water District (VWD), and Olivenhain Municipal Water District (CMWD). Water supply to CMWD TELGIAN ENGINEERING & CONSULTING ENGINEERS • CONSULTANTS • ANALYSTS • ASSESSORS EMERGENCY MANAGEMENT & OPERATIONS CONTINUITY • ENGINEERING, DESIGN & CONSTRUCTION ENVIRONMENTAL, HEALTH & SAFETY • FIRE PROTECTION ENGINEERING • RISK MANAGEMENT & LOSS CONTROL • SECURITY RISK CONSULTING 4001 Kennett Pike, Suite 308, Wilmington, Delaware 19807 www.telgian.com WATER SUPPLY SITE SURVEY REPORT SHEA PROPERTIES NE CORNER OF GATEWAY RD. & EL FUERTE ST. CARLSBAD, CA TEST DATE: 02/24/17 from Connection No. 2 is delivered through a VWD transmission main. Connections No. 3 and No. 4 are on SDCWA's Tr-Agency Pipeline (TAP), which is also supplied from the Second Aqueduct. The TAP also serves the City of Oceanside and Vista Irrigation District (VID). Potable water is delivered within the CMWD service area through 450 miles of pipeline, 17 pressure zones, 57 pressure regulating stations, five pump stations, ten storage tanks, and one reservoir. The CMWD water distribution system is flexible in that supply from the four aqueduct connections can be routed to different parts of the distribution system, as needed. The total operational storage for CMWD is 245.5 million gallons (MG), which includes the 195 MG Maerkle Dam Reservoir. Water Flow Test Data: The following summarizes the hydraulic simulation results: Static and residual pressures were reported to be recorded on El Fuerte St., prior to the 12-inch main loop around the building. A simulated flow of 8000 gpm at a residual pressure of 109 psi was reported. Static pressure was reported to be 126 psi. Static and residual pressure readings were reported to be taken at an elevation of 410 ft., AMSL, which is 13 ft., 11 ft., 15 ft., 10 ft., 12 ft., 10 ft., 10 ft., and 5 ft., below the finish floor elevations of building's B, A, C, G, H, D, E and F respectively. This test is effective at the model simulation point for friction loss purposes. Please see enclosed Attachment #3 for a graphical representation of this model and necessary calculations. * Adjustments were made for assumed pipe friction loss to the building B site entry point, (-5.5 psi), elevation change (-2.5 psi), and a backflow prevention device (-3.0 psi). A 10% deduction (-13.0 psi) for a safety buffer has been taken. See following comments for additional information. * Adjustments were made for assumed pipe friction loss to the building A site entry point, (-5.0 psi), elevation change (-2.0 psi), and a backflow prevention device (-3.0 psi). A 10% deduction (-13.0 psi) for a safety buffer has been taken. See following comments for additional information. * Adjustments were made for assumed pipe friction loss to the building C site entry point, (-6.5 psi), elevation change (-4.5 psi), and a backflow prevention device (-3.0 psi). A 10% deduction (-13.0 psi) for a safety buffer has been taken. See following comments for additional information. * Adjustments were made for assumed pipe friction loss to the building G site entry point, (-4.5 psi), elevation change (-4.5 psi), and a backflow prevention device (-3.0 psi). A 10% deduction (-13.0 psi) for a safety buffer has been taken. See following comments for additional information. * Adjustments were made for assumed pipe friction loss to the building H site entry point, (-5.0 psi), elevation change (-3.0 psi), and a backflow prevention device (-3.0 psi). A 10% deduction (-13.0 psi) for a safety buffer has been taken. See following comments for additional information. * Adjustments were made for assumed pipe friction loss to the building D site entry point, (-4.5 psi), elevation change (-4.5 psi), and a backflow prevention device (-3.0 psi). A 10% deduction (-13.0 psi) for a safety buffer has been taken. See following comments for additional information. * Adjustments were made for assumed pipe friction loss to the building E site entry point, (-4.5 psi), elevation change (-4.5 psi), and a backflow prevention device (-3.0 psi). A 10% deduction (-13.0 psi) for a safety buffer has been taken. See following comments for additional information. TELGIAN ENGINEERING & CoNsucriNG ENGINEERS • CONSULTANTS • ANALYSTS • ASSESSORS EMERGENCY MANAGEMENT & OPERATIONS CONTINUITY • ENGINEERING, DESIGN & CONSTRUCTION ENVIRONMENTAL, HEALTH & SAFETY • FIRE PROTECTION ENGINEERING • RISK MANAGEMENT & LOSS CONTROL • SECURITY RISK CONSULTING 4001 Kennett Pike, Suite 308, Wilmington, Delaware 19807 www.telgian.com WATER SUPPLY SITE SURVEY REPORT SHEA PROPERTIES NE CORNER OF GATEWAY RD. & EL FUERTE ST. CARLSBAD, CA TEST DATE: 02/24/17 * Adjustments were made for assumed pipe friction loss to the building F site entry point, (-2.0 psi), elevation change (-5.0 psi), and a backflow prevention device (-3.0 psi). A 10% deduction (-13.0 psi) for a safety buffer has been taken. See following comments for additional information. Additional Comments: The fire sprinkler demand of 600 gpm at 35 psi is estimated based on the requirements for an Ordinary Hazard Group Ii occupancy (standard mercantile). This criteria requires a density of 0.2 gpm/sqft over the remote 1500 sqft with 250 gpm hose stream allowance. This density is taken from the 2013 NFPA 13 11.2.3.1.1 and Figure 11.2.3.1.1. These demands are only to be used for estimation purposes and should not be considered the exact demands. Fire sprinkler design and calculations will be required to determine an exact hydraulic demand for this facility. Information could not be obtained regarding MIC testing within the water system. It is assumed there has been no evidence of MIC within this area. The public system can be considered a reliable supply with respect to proposed retail store duration requirements. This acceptability is based upon the system capability to maintain the required fire flow for the design 120 minute duration. Telgian was unable to make contact with Carlsbad Fire Department, however based on a previous waterflow analysis in the area, a 50% reduction for fully sprinklered buildings is acceptable in the determination of fire flows in accordance with the California Fire Code, Appendix B. Based upon the proposed size of the building and its assumed classification as a Type VB per the California Building Code, the required flow rate reduces to 2625 gpm at 20 psi, No further calculations were performed, as the observed flow rate exceeds this requirement. Conclusions: Cl-B. FIRE WATER SUPPLY: The available public supplies combined with the assumed fire protection lead-in sizing and arrangement, as shown on Attachment #1, should yield a base of riser supply of 103.5 psi static and 600 gpm flowing at a 102 psi residual. This supply is downstream of a 6-inch, Ames 3000SS, double check detector type backflow preventer. This esceeds the minimum target demand of 600 gpm at 35.0 psi for the supply of sprinkler protection without a pump. See Attachment #313 for a graphical representation and necessary calculations. Cl-A. FIRE WATER SUPPLY: The available public supplies combined with the assumed fire protection lead-in sizing and arrangement, as shown on Attachment #1, should yield a base of riser supply of 104 psi static and 600 gpm flowing at a 103 psi residual. This supply is downstream of a 6-inch, Ames 3000SS, double check detector type backflow preventer. This exceeds the minimum target demand of 600 gpm at 35 psi for the supply of sprinkler protection without a pump. See Attachment #3A for a graphical representation and necessary calculations. Cl-C. FIRE WATER SUPPLY: The available public supplies combined with the assumed fire protection lead-in sizing and arrangement, as shown on Attachment #1, should yield a base of riser supply of 102.5 psi static and 600 gpm flowing at a 99 psi residual. This supply is downstream of a 6-inch, Ames 3000SS, double check detector type backflow preventer. This exceeds the minimum target demand of 600 gpm at 35 psi for the supply of sprinkler protection without a pump. See Attachment #3C for a graphical representation and necessary calculations. Cl-H. FIRE WATER SUPPLY: The available public supplies combined with the assumed fire protection lead-in sizing and arrangement, as shown on Attachment #1, should yield a base of riser supply of 104 psi static and 600 gpm flowing at a 102 psi residual. This supply is downstream of a 6-inch, Ames 3000SS, double check detector type TELGIAN ENGINEERING & CONSULTING ENGINEERS • CONSULTANTS • ANALYSTS • ASSESSORS EMERGENCY MANAGEMENT & OPERATIONS CONTINUITY • ENGINEERING, DESIGN & CONSTRUCTION ENVIRONMENTAL, HEALTH & SAFETY • FIRE PROTECTION ENGINEERING • RISK MANAGEMENT & LOSS CONTROL • SECURITY RISK CONSULTING 4001 Kennett Pike, Suite 308, Wilmington, Delaware 19807 www.telgian.com WATER SUPPLY SITE SURVEY REPORT SHEA PROPERTIES NE CORNER OF GATEWAY RD. & EL FUERTE ST. CARLSBAD, CA TEST DATE: 02/24/17 backflow preventer. This exceeds the minimum target demand of 600 gpm at 35 psi for the supply of sprinkler protection without a pump. See Attachment #3H for a graphical representation and necessary calculations. C1-G. FIRE WATER SUPPLY: The available public supplies combined with the assumed fire protection lead-in sizing and arrangement, as shown on Attachment #1, should yield a base of riser supply of 104.5 psi static and 600 gpm flowing at a 101 psi residual. This supply is downstream of a 6-inch, Ames 3000S5, double check detector type backflow preventer. This exceeds the minimum target demand of 600 gpm at 35 psi for the supply of sprinkler protection without a pump. See Attachment #3G for a graphical representation and necessary calculations C1-D. FIRE WATER SUPPLY: The available public supplies combined with the assumed fire protection lead-in sizing and arrangement, as shown on Attachment #1, should yield a base of riser supply of 104.5 psi static and 600 gpm flowing at a 101 psi residual. This supply is downstream of a 6-inch, Ames 3000SS, double check detector type backflow preventer This exceeds the minimum target demand of 600 gpm at 35 psi for the supply of sprinkler protection without a pump. See Attachment #31) for a graphical representation and necessary calculations. C1-E. FIRE WATER SUPPLY: The available public supplies combined with the assumed fire protection lead-in sizing and arrangement, as shown on Attachment #1, should yield a base of riser supply of 104.5 psi static and 600 gpm flowing at a 101 psi residual. This supply is downstream of a 6-inch, Ames 3000SS, double check detector type backflow preventer This exceeds the minimum target demand of 600 gpm at 35 psi for the supply of sprinkler protection without a pump. See Attachment #3E for a graphical representation and necessary calculations. Cl-F. FIRE WATER SUPPLY: The available public supplies combined with the assumed fire protection lead-in sizing and arrangement, as shown on Attachment #1, should yield a base of riser supply of 107 psi static and 600 gpm flowing at a 103 psi residual. This supply is downstream of a 6-inch, Ames 300055, double check detector type backflow preventer This exceeds the minimum target demand of 600 gpm at 35 psi for the supply of sprinkler protection without a pump. See Attachment #3F for a graphical representation and necessary calculations. This analysis assumes that the installation meets the design parameters and information stated herein. If changes are made, they should be analyzed to determine resultant effects on the water supply. If you need additional information, please feel free to contact us. Sincerely, Pamela Reno Senior Fire Protection Consultant ATTACHMENTS: Attachment #1- Location Sketch Attachment #2 - Area Water Maps Attachment #3B - Water Supply Plot - Fire Calculations Attachment #3A - Water Supply Plot - Fire Calculations Attachment #3C - Water Supply Plot - Fire Calculations Attachment #3H - Water Supply Plot - Fire Calculations Attachment #3G - Water Supply Plot - Fire Calculations Attachment #3D - Water Supply Plot - Fire Calculations Attachment #3E - Water Supply Plot - Fire Calculations Attachment #3F - Water Supply Plot - Fire Calculations TELGIAN ENGINEERING & CONSULTING ENGINEERS • CONSULTANTS • ANALYSTS • ASSESSORS EMERGENCY MANAGEMENT & OPERATIONS CONTINUITY • ENGINEERING, DESIGN & CONSTRUCTION ENVIRONMENTAL, HEALTH & SAFETY • FIRE PROTECTION ENGINEERING • RISK MANAGEMENT & LOSS CONTROL • SECURITY RISK CONSULTING 4001 Kennett Pike, Suite 308, Wilmington, Delaware 19807 www.telgian.com I IATTACHMENT #2 Gateway Road at El Fuerte Street - Fire Flow Analysis . 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IIljjjj II .11111 140 130 120 110 100 90 80 70 60 50. 40 30 20 10 A Observed Flow Test Poin - - - - Raw Water Flow Test - #4 Below - - #7 Below #9 Below Target Demand Flow Rate (gpm) 0 600 I Static (psi) Residual (psi) Pressure available at test 126 126.0 Elevation Adjustment -5.5 -5.5 Pressure loss due to friction 0 -2.5 Pressure at base of riser upstream of BFP & meter 120.5 118.0 S. BFP loss/preload -4 -3 Water meter loss 0 0 Pressure at base of riser downstream of BFP & meter 116.5 115 Safety factor -13 -13 Total base of riser pressure 103.5 102 gpm psi Calculated Demands 600 I 35 Additional Demands I Pump Test I I ATTACHMENT # 3B PAGE 1 OF WATER SUPPLY SITE SURVEY PROJECT: Shea Properties FIRE SPRINKLER DEMAND LOCATION: Building B CITY/STATE: Carlsbad, CA Static (psi) Residual (psi) Flow (gpm) 126 109 8000 Gauge Hydrant Building FFE Elevation (ft) (ft) 410 423 Outlet Diameter #1 (in) Hydrant . Coefficient #1 Pitot #1 (psi) Outlet Diameter #2 (in) Hydrant Coefficient #2 Pitot 42 (psi) Outlet Diameter #3 . (in) Hydrant Coefficient #3 Pitot #3 (psi) Outlet Diameter #4 (in) Hydrant Coefficient #4 Pitot #4 (psi) Gauge Hydrant Location: Flow test results provided by computer modeling Flow Hydrant Location: See Report for Results Test By: Carlsbad Fire Prevention Division IDate: 2/24/2017 ITime: N/A Backflow Prevention: Size: 6-inch Type: Double Check Detector Mfg: AMES Model: 300OSS Mfg: Model: 0 1000 4000 5000 L. Flow (gpm) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGB) .SDF JOB TITLE: SheaProperties Building A_Carlsbad_CA - Attachment #3 NFPA WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 126.0 109.0 8000.0 125.9 600.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 600.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 600.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 0.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE NOTES (FT) (PSI) (GPM) 1 410.0 - - - - 125.9 - - - 2 425.0 - - - - 119.3 - - - 3 426.0 - - - - 118.8 - - - 4 426.0 - - - - 118.7 - - - 5 426.0 - - - - 118.6 - - - 6 425.0 - - - - 119.0 - - - 7 425.0 - - - - 117.9 - - - BOR1 423.0 HOSE STREAM 117.7 600.0 8 422.0 - - - - 120.3 - - - 9 422.0 - - - - 120.3 - - - 10 421.0 - - - - 120.7 - - - BOR2 421.0 - - - - 120.7 - - - bA 420.0 - - - - 121.2 - - - 11 419.0 - - - - 121.6 - - - 12 419.0 - - - - 121.6 - - - 13 418.0 - - - - 122.0 - - - 14 420.0 - - - - 121.2 - - - SOURCE 410.0 SOURCE 125.9 600.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGB) .SDF JOB TITLE: SheaProperties Building A_Carlsbad_CA - Attachment #3 NFPA PIPE DATA Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node/ Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot.(Q) Disch Act ID (ft.) T Pf/ft. (Pf) Pipe: 1 Source 0.0 1.00 150 0.0 SOURCE 410.0 125.9 600.0 2 D12.00 ---- 0.00 0.0 1 410.0 125.9 600.0 12.460 1.00 0.000 0.0 Pipe: 2 0.0 0.0 125.00 150 6.6 1 410.0 125.9 600.0 3 D12.00 T:111.3 111.34 6.5 2 425.0 119.3 600.0 12.460 236.34 0.000 0.1 Pipe: 3 0.0 0.0 95.00 150 0.5 2 425.0 119.3 600.0 4 D12.00 E:50.0 161.33 0.4 3 426.0 118.8 600.0 12.460 T:111.3 256.33 0.000 0.1 Pipe: 4 0.0 0.0 250.00 150 0.1 3 426.0 118.8 600.0 5 D12.00 T:111.3 111.34 0.0 4 426.0 118.7 600.0 12.460 361.34 0.000 0.1 Pipe: 5 0.0 0.0 95.00 150 0.0 4 426.0 118.7 600.0 6 D12.00 E:50.0 84.07 0.0 5 426.0 118.6 600.0 12.460 L:34.1 179.07 0.000 0.0 Pipe: 6 0.0 0.0 195.00 150 -0.4 5 426.0 118.6 600.0 7 D12.00 T:111.3 111.34 -0.4 6 425.0 119.0 600.0 12.460 306.34 0.000 0.1 Pipe: 7 0.0 0.0 75.00 140 1.1 6 425.0 119.0 600.0 BOR1 D6.000 T:47.0 52.00 0.0 7 425.0 117.9 600.0 6.280 G: 5.0 127.00 0.009 1.1 Pipe: 8 H.S. 600.0 Disch 75.00 140 0.2 7 425.0 117.9 0.0 D6.000 T:47.0 47.00 -0.9 BOR1 423.0 117.7 600.0 6.280 122.00 0.009 1.1 Pipe: 9 0.0 0.0 600.00 150 1.3 8 422.0 120.3 0.0 D12.00 T:111.3 111.34 1.3 6 425.0 119.0 0.0 12.460 711.34 0.000 0.0 Pipe: 10 0.0 0.0 115.00 150 0.0 9 422.0 120.3 0.0 D12.00 E:50.0 84.07 0.0 8 422.0 120.3 0.0 12.460 L:34.1 199.07 0.000 0.0 Pipe: 11 0.0 0.0 55.00 140 0.4 10 421.0 120.7 0.0 D6.000 T:47.0 52.00 0.4 9 422.0 120.3 0.0 6.280 G: 5.0 107.00 0.000 0.0 Pipe: 12 0.0 0.0 25.00 140 0.0 BOR2 421.0 120.7 0.0 D6.000 T:47.0 47.00 0.0 10 421.0 120.7 0.0 6.280 72.00 0.000 0.0 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGB) .SDF JOB TITLE: SheaProperties Building A_Carlsbad_CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 13 0.0 0.0 225.00 150 0.9 10A 420.0 121.2 0.0 D12.00 T:111.3 111.34 0.9 9 422.0 120.3 0.0 12.460 336.34 0.000 0.0 Pipe: 14 0.0 0.0 725.00 150 0.4 11 419.0 121.6 0.0 D12.00 T:111.3 111.34 0.4 bA 420.0 121.2 0.0 12.460 836.34 0.000 0.0 Pipe: 15 0.0 0.0 115.00 150 0.0 12 419.0 121.6 0.0 D12.00 T:111.3 111.34 0.0 11 419.0 121.6 0.0 12.460 226.34 0.000 0.0 Pipe: 16 0.0 0.0 95.00 150 0.4 13 418.0 122.0 0.0 D12.00 T:111.3 111.34 0.4 12 419.0 121.6 0.0 12.460 206.34 0.000 0.0 Pipe: 17 0.0 0.0 125.00 150 0.9 13 418.0 122.0 0.0 D12.00 T:111.3 111.34 0.9 14 420.0 121.2 0.0 12.460 236.34 0.000 0.0 NOTES (HASS) Calculations were performed by the HASS 8.7 computer program in accordance with NFPA13 (2017) under license no. 2704110710 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.018 gpm and a maximum imbalance at any node of 0.154 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.2 ft/sec at pipe 8. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SOURCE under full flow conditions is 125.86 psi with a flow of 600.04 gpm. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGB).SDF JOB TITLE: SheaProperties Building A_Carlsbad_CA - Attachment #3 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 12.460 44.00 98.00 30.00 107.00 34.00 10.00 98.00 ATTACHMENT U 3A PAGE 1OF WATER SUPPLY SITE SURVEY PROJECT: Shea Properties FIRE SPRINKLER DEMAND LOCATION: Building A CITY/STATE: Carlsbad, CA Static (psi) Residual (psi) Flow (gpm) 126 109 8000 Gauge Hydrant Building FFE Elevation (ft) (ft) 410 421 Outlet Diameter #1 (in) Hydrant Coefficient #1 . Pitot #1 (psi) Outlet Diameter #2 (in) Hydrant .. Coefficient #2 . . . Pitot #2 (psi) Outlet . Diameter #3 (in) Hydrant Coefficient #3 Pitot#3 (psi) Outlet Diameter #4 (in) Hydrant Coefficient #4 Putot#4 (psi) - Gauge Hydrant Location: Flow test results provided by computer modeling Flow Hydrant Location: See Report for Results Test By: Carlsbad Fire Prevention Division IDate: 2/24/2017 lIme: N/A Backflow Prevention: Size: 6-inch Type: Double Check Detector Mfg: AMES Model: 3S Mfg: Model: 150 140 I If 11 111 fill A Observed Flow Test Point 130 120 110 fl I ....... - - -. Raw Water Flow Test loo 90 III if I II - #4 Below 80 70 60 11111111111111 111 1 if 111111 - —#7 Below 50 fill 40 ______ #9 Below 30 1 4 4111 IIIIIi if 1. 20 _______ 10 If 11111 11 1111 11 • Target Deman 11, 111 d 0 - I 11E -_______ 0 1000 2000 3000 4000 5000 6000 7000 8000 Flow (gpm) 111 11 I II I Ill 111111 I III III "I'll, II I I I Ill 111111 I lii 111f,11 111111 ll1flIJ_llll.l I 1111111111111 Ill I II II I II Ill 11(11 lllllllj Ill 11111 lull Ill Ill Ill I Ill 1111111 lii lit II 111111111 lIl I 111111 liii tij.LljjiIjjlll Ill lllllljJlj1(jJJfl tJj_l_IjjJlll I lllllIIllIiiJ_iiJlII III IlIllIlIlil [lJllll_i_jjJjjlljjjl 111111111] i1il1fl 1111111 .......................................................... •..TuIil1Ti ii 1 ILQ1TITII Fill 11 11IITIIIUIU1TIQI j(]) ulljJJ_lj.1I1_I__iJlljJJJjj)$JJlI II II I IiIljjj_lIl_liii_II_ 'L!JjjlIlljjJlll II III III I I II III IIJ.JJJJJJJ.IIJJJJJ.ID 111111 l.1lJ.1lII111UJ.I.III...II ..JIIJIIJJJJIJJ_JJ.JJIJJJIIIIJJJJJ ,. I FIJIUJIJJJJIJ1!IJJ 1111 IlIIlljjljj UJJJJJJIJJ.IIJJJ II (jjJjjJjjjJ II 11111 1111 I II1jjJ1ijjjjjItil: I II.1i ,Ill4jl..IIllJ 11111 IUJJ.IUJJJJJ.IJ__J.I IIIIJ 11111...II. IJJJJLJJJJJ.I1J IlJIiI!IillIIlUI 1IIiII1IIIIIIII I1TIF1If1itIn1rHu 1 III1Ih n1if!ijfllIi full III ill Ii111IIffI1i1 111 11111 d11iIID_1]i11IFII1f 111*tf11 if}ff-fli-ffftflfF If1II111*- ii1 ll4fli.f I (flu III 1* II Ii ii iFhT1if11TiIf} 1f1flfh cbi IiJ.J1[lItlLJJi1.Ll jJjljljjllll I ll 1411, I HIll M11, UUI1I.11' ljjjlllljjjjl II ljjiIIullIlLIlIIl IIJjjjiIUliIllIIul I liii 111111111 11IIllIjJJ DJJJJLIJLIIWJJJJII. JJJIIJIJW.IjiTlil1l1I .1wuaujjjlil.. ..... ujirJlrlrr.11ff..LLI!.IJ. IJ33jj1J.111jI1Th_Illllh1II11Ill_1IIIIIII1i1ilIIf 11 ft1fll1I}1 1.11t iii I I ITFIII II I 'uu'tl}PcIifllf I1ffi11 III 11011V 600gpm @ 35p s1 fiif[fliHft Ih1 fH1{1ii1 ll1H1fftlli% ' IIi1!IWIIIII 11111111 II II I II_1)111111__I_1111 10111 IlIulIllIl_lill ill 1111111 1111 IiIlII III II II Ili 'II II II 111111111 1111111111111111111 IlIlili 11111111 1%, IlIlIlIIllIIlIlIllIluiliT1,Iltl,lIIIIlIIIIIIIIllIlIlIII1ItlIIIIIIIlIllIulII 1If}rll1ITllI1i_II_I1Ill-i-II-Fll Ill iI.11i.11fIII.i '-Illflflu1-f *-U{fll-fll-F -}i-1-Ift1-1I-fF*I_111_lift f1-H-ll-Fi-1 1*1-1-11 ..I_li}ffiflJff I_I_II_iff jiiuuuuiHL9i 4thi 11111 35 Flow Rate (gpm) 0 600 Static (psi) Residual (psi) Pressure available at test 126 126.0 Elevation Adjustment .5 -5 3 Pressure loss due to friction 0 -2 4. Pressure at base of riser upstream of BFP & meter 121 119.0 S. BFP loss/preload -4 -3 Water meter loss 0 0 Pressure at base of riser downstream of BFP & meter 117 116 Safety factor -13 -13 Total base of riser pressure 104 103 Calculated Demands 600 I Additional Demands F Pump Test SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/11/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGA).SDF JOB TITLE: SheaProperties Building A_Carlsbad_CA - Attachment #3A NFPA WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 126.0 109.0 8000.0 125.9 600.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 600.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 600.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 0.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE NOTES (FT) (PSI) (GPM) 1 410.0 - - - - 125.9 - - - 2 425.0 - - - - 119.3 - - - 3 426.0 - - - - 118.8 - - - 4 426.0 - - - - 118.7 - - - 5 426.0 - - - - 118.6 - - - 6 425.0 - - - - 119.0 - - - 7 425.0 - - - - 119.0 - - - BOR1 423.0 - - - - 119.9 - - - 8 422.0 - - - - 120.1 9 422.0 - - - - 120.0 - - - 10 421.0 - - - - 119.6 - - - BOR2 421.0 HOSE STREAM 118.9 600.0 bA 420.0 - - - - 120.9 - - - 11 419.0 - - - - 121.3 - - - 12 419.0 - - - - 121.3 - - - 13 418.0 - - - - 121.8 - - - 14 420.0 - - - - 120.9 - - - SOURCE 410.0 SOURCE 125.9 600.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/11/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGA) .SDF JOB TITLE: SheaProperties Building A Carlsbad CA - Attachment #3A NFPA PIPE DATA Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 1 Source 0.0 1.00 150 0.0 SOURCE 410.0 125.9 600.0 2 D12.00 ---- 0.00 0.0 1 410.0 125.9 600.0 12.460 1.00 0.000 0.0 Pipe: 2 0.0 0.0 125.00 150 6.6 1 410.0 125.9 600.0 3 D12.00 T:111.3 111.34 6.5 2 425.0 119.3 600.0 12.460 236.34 0.000 0.1 Pipe: 3 0.0 0.0 95.00 150 0.5 2 425.0 119.3 600.0 4 D12.00 E:50.0 161.33 0.4 3 426.0 118.8 600.0 12.460 T:111.3 256.33 0.000 0.1 Pipe: 4 0.0 0.0 250.00 150 0.1 3 426.0 118.8 600.0 5 D12.00 T:111.3 111.34 0.0 4 426.0 118.7 600.0 12.460 361.34 0.000 0.1 Pipe: 5 0.0 0.0 95.00 150 0.0 4 426.0 118.7 600.0 6 012.00 E:50.0 84.07 0.0 5 426.0 118.6 600.0 12.460 L:34.1 179.07 0.000 0.0 Pipe: 6 0.0 0.0 195.00 150 -0.4 5 426.0 118.6 600.0 8 D12.00 T:111.3 111.34 -0.4 6 425.0 119.0 600.0 12.460 306.34 0.000 0.1 Pipe: 7 0.0 0.0 75.00 140 0.0 7 425.0 119.0 0.0 D6.000 T:47.0 52.00 0.0 6 425.0 119.0 0.0 6.280 G: 5.0 127.00 0.000 0.0 Pipe: 8 0.0 0.0 75.00 140 0.9 BOR1 423.0 119.9 0.0 06.000 T:47.0 47.00 0.9 7 425.0 119.0 0.0 6.280 122.00 0.000 00 Pipe: 9 0.0 0.0 600.00 150 -1.1 6 425.0 119.0 600.0 9 D12.00 T:111.3 111.34 -1.3 8 422.0 120.1 600.0 12.460 711.34 0.000 0.2 Pipe: 10 0.0 0.0 115.00 150 0.1 8 422.0 120.1 600.0 10 D12.00 E:50.0 84.07 0.0 9 422.0 120.0 600.0 12.460 L:34.1 199.07 0.000 0.1 Pipe: 11 0.0 0.0 55.00 140 0.5 9 422.0 120.0 600.0 BOR2 D6.000 T:47.0 52.00 -0.4 10 421.0 119.6 600.0 6.280 G: 5.0 107.00 0.009 0.9 Pipe: 12 H.S. 600.0 Disch 25.00 140 0.6 10 421.0 119.6 0.0 D6.000 T:47.0 47.00 0.0 BOR2 421.0 118.9 600.0 6.280 72.00 0.009 0.6 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/11/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGA) .SDF JOB TITLE: SheaProperties Building A Carlsbad CA - Attachment #3A Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 13 0.0 0.0 225.00 150 0.9 10A 420.0 120.9 0.0 D12.00 T:111.3 111.34 0.9 9 422.0 120.0 0.0 12.460 336.34 0.000 0.0 Pipe: 14 0.0 0.0 725.00 150 0.4 11 419.0 121.3 0.0 D12.00 T:111.3 111.34 0.4 bA 420.0 120.9 0.0 12.460 836.34 0.000 0.0 Pipe: 15 0.0 0.0 115.00 150 0.0 12 419.0 121.3 0.0 D12.00 T:111.3 111.34 0.0 11 419.0 121.3 0.0 12.460 226.34 0.000 0.0 Pipe: 16 0.0 0.0 95.00 150 0.4 13 418.0 121.8 0.0 D12.00 T:111.3 111.34 0.4 12 419.0 121.3 0.0 12.460 206.34 0.000 0.0 Pipe: 17 0.0 0.0 125.00 150 0.9 13 418.0 121.8 0.0 D12.00 T:111.3 111.34 0.9 14 420.0 120.9 0.0 12.460 236.34 0.000 0.0 NOTES (HASS) Calculations were performed by the HASS 8.7 computer program in accordance with NFPA13 (2017) under license no. 2704110710 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.018 gpm and a maximum imbalance at any node of 0.154 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.2 ft/sec at pipe 12. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SOURCE under full flow conditions is 125.86 psi with a flow of 600.04 gpm. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/11/2017 C:\FIASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGA).SDF JOB TITLE: SheaProperties Building A_Carlsbad_CA - Attachment #3A PAGE: D MATERIAL: DIRON HNC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 12.460 44.00 98.00 30.00 107.00 34.00 10.00 98.00 AUACI-IMENT# 3C PAGE 1 OF t!I1 WATER SUPPLY SITE SURVEY PROJECT: Shea Properties FIRE SPRINKLER DEMAND LOCATION: Building C CITY/STATE: Carlsbad, CA Static (psi) Residual (psi) Flow (gpm) 126 109 8000 Gauge Hydrant Building FFE Elevation (ft) (ft) 410 425 Outlet Diameter #1 (in) Hydrant Coefficient #1 Pitot #1 (psi) Outlet Diameter #2 (in) Hydrant Coefficient #2 . . Pitot #2 (psi) Outlet Diameter #3 (in) Hydrant Coefficient . #3 . Pitot #3 . (psi) Outlet Diameter #4 (in) Hydrant Coefficient : Pitot #4 (psi) Gauge Hydrant Location: Flow test results provided by computer modeling Flow Hydrant Location: See Report for Results Test By: Carlsbad Fire Prevention Division IDate: 2/24/2017 [Time: N/A Backflow Prevention: Size: 6-inch Type: Double Check Detector Mfg: AMES Model: 300OSS Mfg: Model: 1111 I'JJ_IjjJ hull uulhuuhlh[llul III ii lluuhluuhhuI[jjhhiIjluluuhljjjjjuuhhuu I) 11 1 11 1 . 11 f1 1 111 . 11 till l R111 , IL11111 1,11111 11 fii 111 11,1 111111111 FIN IL111911 11111 1 fll U1lJ)jjt.l.l.l)jjjlJ fill llIllIfl 1111111 "111 11 111 iii.iiJI)illunlui IIII I 11 UTTIII il HL PII 11 JJJJjU1TIIJ1IIFIIIJ..JJJJJII1Tljilhjjj.kijjj 'ilJlt I I III 111111 I I I I liii JJffl11 II II 111111LlJ.lwilJ.'l...1'.JJ'JJ1!JJJ.JJJJ. Illllhlillfl 11 I III 111111111 JIIJJJJftI.ojlllllUilliiuirttrtrr'J1.IiJ1lJJJ.lJ.rWi ftllu11IiJJJIi.J liii 111111 III is l Ii I Ii. III 1111 (III I IJlill (ii llii11IiIi1IIl1iii11lI jjlliilll I 11111 III Ii ill IltIl Il 11111 III 'Ill! tiilliiii II 'II Ii I u. ill lilt I il1111111111111111111111111 1_Ij_tlIiiilIlIlIi I lIi11iiIi1i1iilE1u1iilli1 I lltllllllli_ IrlillilTEfIl II 1 III! 1111 11111 II 1111111 lIllillII1TiiIiT1hiti lI1iijjlilIlIjI II ill II IlillillI lIllillIlIl II I Ill I 1111111] lililill ii.iH.i: -ff1-}ll f 1fl-llifIf 1IR f*ftffiH{ f*-{f1-}1ll U3iLW "F1 I I lilt I I I li,'llll lilI1rt1I.'1IuI1l I I II lllj_IlJlILtJJlIlitjlli IlIlllllII1TITii1IIIIi1iIIrlIIlllllilIIt lii Ill! I II Ii huh lllIilflI Ill ii I 11111111 lliltlhhiiiillll III II Tu1 ft11 ff i'__ I I LIiIIJJ.11hlill illIlliThU I I lljjIIjjjjJjJJl II llhhlllhllhill I II III I fill I jJ1Jjjjj!jlliJlIi I 9llillhhllTiihhi I I liii ItI 1111111 HiT (Ii (IflUllIt IHIlIlill III III III III 111111 1111111111111 tIll_il II I 111111111 i i_il hUt!] 11111111 11 1,116 III III is (11111 III 11111 lilt I ii HIS hIll I I I I I II II Ill I II I I 111111 I II lIlIuu Iii II 1111111 Il 111111111111110111 111111 i l 'lIllJ 1111 jJ ñIHllIIliiIIlIII I I IlIJIlilIlihl IflTfllHl iii I H III IU hiljjl IllhiIilIhiIjjJlhi IltiThIlhlIlihlill Ill till H1iiiUIIhlhIluhhfIuiU 111111111111 lUIHilI hillEl 1111111 huh lhhilhlhihllhllhillhl llllhllllhhlhhlhlllllll I_Ii 111111 I 1111111 III liii 1111111 Ii lii I lUiI Ill llhuriifHIM1HbI 11111 i Ill III' II 4000 5000 L Flow (gpm) Flow Rate (gpm) 0 600 I Static (psi) Residual (psi) Pressure available at test 126 126.0 Elevation Adjustment -6.5 -6.5 3 Pressure loss due to friction 0 -4.5 Pressure at base of riser upstream of BFP & meter 119.5 115.0 BFP loss/preload -4 -3 Water meter loss 0 0 Pressure at base of riser downstream of BFP & meter 115.5 112 Safety factor -13 -13 Total base of riser pressure 102.5 99 — — — - Raw Water Flow Test — #4 Below — —#7 Below #9 Below Target Demand Calculated Demands 600 35 1. Additional Demands I Pump Test I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGC) .SDF JOB TITLE: SheaProperties Building C_Carlsbad_CA - Attachment #3 NFPA WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 126.0 109.0 8000.0 125.9 600.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 600.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 600.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 0.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE NOTES (FT) (PSI) (GPM) 1 410.0 - - - - 125.9 - - - 2 425.0 - - - - 119.3 - - - 3 426.0 - - - - 118.8 - - - 4A 426.0 - - - - 118.7 - - - SA 426.0 - - - - 116.6 - - - 6A 425.0 - - - - 115.7 - - - BOR3 425.0 HOSE STREAM 115.0 600.0 7A 423.0 - - - - 117.9 - - - 8A 422.0 - - - - 118.3 - - - BOR4 422.0 - - - - 118.3 - - - 9A 421.0 - - - - 118.8 - - - 9B 421.0 - - - - 118.8 - - - BOR5 420.0 - - - - 119.2 - - - lOB 419.0 - - - - 119.6 - - - hA 419.0 - - - - 119.6 - - - 12A 418.0 - - - - 120.1 - - - BOR6 420.0 - - - - 119.2 - - - 12B 419.0 - - - - 119.6 - - - 13A 418.0 - - - - 120.1 - - - 14A 416.0 - - - - 120.9 - - - 15 412.0 - - - - 122.7 - - - 16 410.0 - - - - 123.5 - - - SOURCE 410.0 SOURCE 125.9 600.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGC) .SDF JOB TITLE: SheaProperties Building C Carlsbad CA - Attachment #3 NFPA PIPE DATA Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf/ft. (Pf) Pipe: 1 Source 0.0 1.00 150 0.0 SOURCE 410.0 125.9 600.0 2 D12.00 ---- 0.00 0.0 1 410.0 125.9 600.0 12.460 1.00 0.000 0.0 Pipe: 2 0.0 0.0 125.00 150 6.6 1 410.0 125.9 600.0 3 D12.00 T:111.3 111.34 6.5 2 425.0 119.3 600.0 12.460 236.34 0.000 0.1 Pipe: 3 0.0 0.0 95.00 150 0.5 2 425.0 119.3 600.0 4A D12.00 E:50.0 161.33 0.4 3 426.0 118.8 600.0 12.460 T:111.3 256.33 0.000 0.1 Pipe: 4 0.0 0.0 110.00 150 0.1 3 426.0 118.8 600.0 5A D12.00 T:111.3 111.34 0.0 4A 426.0 118.7 600.0 12.460 221.34 0.000 0.1 Pipe: 5 0.0 0.0 200.00 140 2.1 4A 426.0 118.7 600.0 6A D6.000 T:47.0 47.00 0.0 5A 426.0 116.6 600.0 6.280 247.00 0.009 2.1 Pipe: 6 0.0 0.0 110.00 140 0.9 5A 426.0 116.6 600.0 BOR3 D6.000 T:47.0 47.00 -0.4 6A 425.0 115.7 600.0 6.280 157.00 0.009 1.4 Pipe: 7 H.S. 600.0 Disch 25.00 140 0.7 6A 425.0 115.7 0.0 D6.000 T:47.0 52.00 0.0 BOR3 425.0 115.0 600.0 6.280 G: 5.0 77.00 0.009 0.7 Pipe: 8 0.0 0.0 100.00 140 1.3 7A 423.0 117.9 0.0 D6.000 E:22.0 36.00 1.3 5A 426.0 116.6 0.0 6.280 L:14.0 136.00 0.000 0.0 Pipe: 9 0.0 0.0 75.00 140 0.4 8A 422.0 118.3 0.0 D8.000 E:31.0 53.00 0.4 7A 423.0 117.9 0.0 8.390 L:22.0 128.00 0.000 0.0 Pipe: 10 0.0 0.0 75.00 140 0.0 BOR4 422.0 118.3 0.0 D6.000 T:47.0 47.00 0.0 8A 422.0 118.3 0.0 6.280 122.00 0.000 0.0 Pipe: 11 0.0 0.0 125.00 150 0.4 9A 421.0 118.8 0.0 D8.000 T:67.0 67.03 0.4 8A 422.0 118.3 0.0 8.390 192.03 0.000 0.0 Pipe: 12 0.0 0.0 50.00 150 0.0 9B 421.0 118.8 0.0 D8.000 E:35.2 60.22 0.0 9A 421.0 118.8 0.0 8.390 L:25.0 110.22 0.000 0.0 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGC).SDF JOB TITLE: SheaProperties Building C_Carlsbad_CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 13 0.0 0.0 E:22.0 75.00 140 0.4 BOR5 420.0 119.2 0.0 D6.000 L:14.0 41.00 0.4 9B 421.0 118.8 0.0 6.280 G: 5.0 116.00 0.000 0.0 Pipe: 14 0.0 0.0 75.00 150 0.9 lOB 419.0 119.6 0.0 D8.000 T:67.0 67.03 0.9 9B 421.0 118.8 0.0 8.390 142.03 0.000 0.0 Pipe: 15 0.0 0.0 90.00 150 0.0 ilA 419.0 119.6 0.0 D8.000 E:35.2 35.22 0.0 lOB 419.0 119.6 0.0 8.390 125.22 0.000 0.0 Pipe: 16 0.0 0.0 50.00 140 0.4 12A 418.0 120.1 0.0 D6.000 E:22.0 69.00 0.4 hA 419.0 119.6 0.0 6.280 T:47.0 119.00 0.000 0.0 Pipe: 17 0.0 0.0 65.00 140 0.9 12A 418.0 120.1 0.0 D6.000 E:22.0 69.00 0.9 BOR6 420.0 119.2 0.0 6.280 T:47.0 134.00 0.000 0.0 Pipe: 18 0.0 0.0 95.00 150 0.0 12B 419.0 119.6 0.0 D8.000 E:35.2 102.25 0.0 hA 419.0 119.6 0.0 8.390 T:67.0 197.25 0.000 0.0 Pipe: 19 0.0 0.0 195.00 150 0.4 13A 418.0 120.1 0.0 D8.000 E:35.2 102.25 0.4 123 419.0 119.6 0.0 8.390 T:67.0 297.25 0.000 0.0 Pipe: 20 0.0 0.0 535.00 150 -0.9 13A 418.0 120.1 0.0 D12.00 E:50.0 161.33 -0.9 14A 416.0 120.9 0.0 12.460 T:111.3 696.33 0.000 0.0 Pipe: 21 0.0 0.0 90.00 150 1.7 15 412.0 122.7 0.0 D12.00 T:111.3 111.34 1.7 14A 416.0 120.9 0.0 12.460 201.34 0.000 0.0 Pipe: 22 0.0 0.0 50.00 150 0.9 16 410.0 123.5 0.0 D12.00 T:111.3 111.34 0.9 15 412.0 122.7 0.0 12.460 161.34 0.000 0.0 NOTES (FIASS) (1) Calculations were performed by the HASS 8.7 computer program in accordance with NFPA13 (2017) under license no. 2704110710 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGC).SDF JOB TITLE: SheaProperties Building C_Carlsbad_CA - Attachment #3 The system has been calculated to provide an average imbalance at each node of 0.014 gpm and a maximum imbalance at any node of 0.154 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.2 ft/sec at pipe 7. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SOURCE under full flow conditions is 125.86 psi with a flow of 600.04 gpm. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 12.460 44.00 98.00 30.00 107.00 34.00 10.00 98.00 I If I'll 10111 1 11 1 1 I 111 11 11 $11 1 1 111, "111 ~l E, 1 1 I IN 11 11, 1 11111] 1 L111 1 1 11 I Y11011111 11 11 `111 111 "111 1[ If R1111 11 fill I 11111111111 fill fill 11111 11111111f] 111111fill 11 II[Ill 111 11111 HIS 911111( 11111111 filli HIR1111 1 11 1111111 11HII[lill 11 11 11111 'tI1H1llI'L Il 111111111 if 11111 jJffljftl ll1llftffMii1ii 111111111111 llllllijjjJjllllllI1Il 1 'Ill ii i•iiIii• IIJJJJJjIJJIJ.IJIIJJ I II i. 'ilJfl I (jIJ Ii (III II II (11(1 Jill lljJjJjJjljjjJjj(jj IIIIIIIIIIIIIiIIII IjjJ(jjIIJJIIiI lIllIII(llIlIII III III Ilifiiililllllt1iilIt III (1111 II IlijillIl 111111111 I Ii 1111111 (Ill ItiTilliTti I 11111 illI Ilii. I' ' lilIlIIII illll__Ill! I I I I III II I lii*1 11 II III liii 1111111111111 11111111 Il II 111111 III I till II 111111111111111 (tilt I I fF111] lull Ill II fFl .k[ll II JilDiiii 'iI:I}H -iliiI} IIJIf ¶dfiJEIIlli.ii JfiII LI IFiItEi IIIIIJjIHH1.Lliili1.11hI ..H1fti Nu k. IFI i. 'iELi t tii1ItllJJ. JIIiiiI IMlihi' IIIIIIIIIIIIIIIIIi 1TIIIfI11TII1III III, k T1IF1$I!l Tfllh1 F11fI1TiIIf1 ill 1 1llTrH 111111111 1iihiHf}llI fri*FFiIffFllf if Ill 1111 I 1 1111111 1 MIMIC 1111 Ill 11,1 111 P111111 *111,1111cli 111111111 1111 111111 F1111111 11 LINI.. 11111( ill 1 111111 +111 ril 111% if IIl..I I 111111911 Ill ll II! III (I III lilllllj2 1111111 111111 I Ill Ill I I II11t1. li,lllI 11111 Ii, II II III lilil IilIllJjlIIll_lllII IIlllllItIitIlt tillillil 11111111 II II jjj III 11111111 I 1111111111 lllllttj lll1 ill r60oP' c) ltIIIJJ_ilt 111111111 I I 111t111 rillll I 1111 illillilitl tIjjjj.II_1ttIII II 11111111! IIIlttlIIllIllllIilIilI 111(11111 II 111111 lilt IIHIIHI 11111_i] 1111111 1I'IffIIi-IIi-FiIi1.'FiIIti .Ill i1iiffifN 1--FftfFI1 II{Ifi iFfllf ill lillff thlif4hiiih1lli HI1 HTIi1iilIIhIl iiiTiiIIt1ITIffli '*II1IfFIII{ft d'tIHI 150 140 130 120 110 100 90 80 70 o 60 50 40 30 20 10 A Observed Flow Test Point - - -. Raw Water Flow Test - #4 Below - _#7 Below #9 Below Target Demand ATTACHMENT# 3H PAGE 1OF WATER SUPPLY SITE SURVEY FIRE SPRINKLER DEMAND Static (psi) Residual (psi) Flow (gpm) 126 109 8000 PROJECT: Shea Properties LOCATION: Building H CITY/STATE: Carlsbad, CA Gauge Hydrant Building FFE Elevation (ft) (ft) 410 422 Outlet Diameter #1 (in) Hydrant Coefficient #1 Pitot #1 (psi) Outlet Diameter #2 (in) Hydrant Coefficient #2 Pitot #2 (psi) Outlet Diameter #3 (in) Hydrant - Coefficient #3 Pitot #3 Outlet Diameter #4 (in) Hydrant Coefficient #4 Pitot #4 (psi) Gauge Hydrant Location: Flow test results provided by computer modeling Flow Hydrant Location: See Report for Results Test By: Carlsbad Fire Prevention Division IDate: 2/24/2017 ITime: N/A Backflow Prevention: Size: 6-inch Type: Double Check Detector Mfg: AMES Model: 300OSS Mfg: Model: 0 1000 2000 3000 4000 5000 6000 7000 8000 Flow (gpm) Flow Rate (gpm) 0 600 I Static (psi) Residual (psi) Pressure available at test 126 126.0 Elevation Adjustment -5 -5 Pressure loss due to friction 0 -3 Pressure at base of riser upstream of BFP & meter 121 118.0 S. BFP loss/preload -4 -3 Water meter loss 0 0 Pressure at base of riser downstream of BFP & meter 117 115 S. Safety factor -13 -13 9. Total base of riser pressure 104 102 Calculated Demands 600 I 35 Additional Demands I Pump Test I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/11/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGH).SDF JOB TITLE: SheaProperties Building H Carlsbad CA - Attachment #3 NFPA WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 126.0 109.0 8000.0 125.9 600.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 600.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 600.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 0.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE NOTES (FT) (PSI) (GPM) 1 410.0 - - - - 125.9 - - - 2 425.0 - - - - 119.3 - - - 3 426.0 - - - - 118.8 - - - 4A 426.0 - - - - 118.7 - - - 5A 426.0 - - - - 118.2 - - - 6A 425.0 - - - - 118.7 - - - BOR3 425.0 - - - - 118.7 - - - 7A 423.0 - - - - 119.2 - - - 8A 422.0 - - - - 119.4 - - - BOR4 422.0 HOSE STREAM 118.4 600.0 9A 421.0 - - - - 119.9 - - - 9B 421.0 - - - - 119.9 - - - BOR5 420.0 - - - - 120.3 - - - lOB 419.0 - - - - 120.7 - - - hA 419.0 - - - - 120.7 - - - 12A 418.0 - - - - 121.2 - - - BOR6 420.0 - - - - 120.3 - - - 12B 419.0 - - - - 120.7 - - - 13A 418.0 - - - - 121.2 - - - 14A 416.0 - - - - 122.0 - - - 15 412.0 - - - - 123.8 - - - 16 410.0 - - - - 124.6 - - - SOURCE 410.0 SOURCE 125.9 600.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/11/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGH) .SDF JOB TITLE: SheaProperties Building H_Carlsbad_CA - Attachment #3 NFPA PIPE DATA Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf/ft. (Pf) Pipe: 1 Source 0.0 1.00 150 0.0 SOURCE 410.0 125.9 600.0 2 D12.00 ---- 0.00 0.0 1 410.0 125.9 600.0 12.460 1.00 0.000 0.0 Pipe: 2 0.0 0.0 125.00 150 6.6 1 410.0 125.9 600.0 3 D12.00 T:111.3 111.34 6.5 2 425.0 119.3 600.0 12.460 236.34 0.000 0.1 Pipe: 3 0.0 0.0 95.00 150 0.5 2 425.0 119.3 600.0 4A D12.00 E:50.0 161.33 0.4 3 426.0 118.8 600.0 12.460 T:111.3 256.33 0.000 0.1 Pipe: 4 0.0 0.0 110.00 150 0.1 3 426.0 118.8 600.0 5A D12.00 T:111.3 111.34 0.0 4A 426.0 118.7 600.0 12.460 221.34 0.000 0.1 Pipe: 5 0.0 0.0 200.00 150 0.5 4A 426.0 118.7 600.0 7A D8.000 T:67.0 67.03 0.0 5A 426.0 118.2 600.0 8.390 267.03 0.002 0.5 Pipe: 6 0.0 0.0 110.00 140 0.4 6A 425.0 118.7 0.0 D6.000 T:47.0 47.00 0.4 5A 426.0 118.2 0.0 6.280 157.00 0.000 0.0 Pipe: 7 0.0 0.0 25.00 140 0.0 BOR3 425.0 118.7 0.0 D6.000 T:47.0 52.00 0.0 6A 425.0 118.7 0.0 6.280 G: 5.0 77.00 0.000 0.0 Pipe: 8 0.0 0.0 100.00 150 -1.0 5A 426.0 118.2 600.0 8A D8.000 E:35.2 60.22 -1.3 7A 423.0 119.2 600.0 8.390 L:25.0 160.22 0.002 0.3 Pipe: 9 0.0 0.0 75.00 150 -0.2 7A 423.0 119.2 600.0 BOR4 D8.000 E:35.2 60.22 -0.4 8A 422.0 119.4 600.0 8.390 L:25.0 135.22 0.002 0.3 Pipe: 10 H.S. 600.0 Disch 75.00 140 1.1 8A 422.0 119.4 0.0 D6.000 T:47.0 47.00 0.0 BOR4 422.0 118.4 600.0 6.280 122.00 0.009 1.1 Pipe: 11 0.0 0.0 125.00 150 0.4 9A 421.0 119.9 0.0 D8.000 T:67.0 67.03 0.4 8A 422.0 119.4 0.0 8.390 192.03 0.000 0.0 Pipe: 12 0.0 0.0 50.00 150 0.0 9B 421.0 119.9 0.0 D8.000 E:35.2 60.22 0.0 9A 421.0 119.9 0.0 8.390 L:25.0 110.22 0.000 0.0 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page EEI DATE: 10/11/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGR).SDF JOB TITLE: SheaProperties Building H_Carlsbad_CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot.(Q) Disch Act ID (ft.) T Pf/ft. (Pf) Pipe: 13 0.0 0.0 E:22.0 75.00 140 0.4 BOR5 420.0 120.3 0.0 D6.000 L:14.0 41.00 0.4 9B 421.0 119.9 0.0 6.280 G: 5.0 116.00 0.000 0.0 Pipe: 14 0.0 0.0 75.00 150 0.9 lOB 419.0 120.7 0.0 D8.000 T:67.0 67.03 0.9 9B 421.0 119.9 0.0 8.390 142.03 0.000 0.0 Pipe: 15 0.0 0.0 90.00 150 0.0 11A 419.0 120.7 0.0 D8.000 E:35.2 35.22 0.0 lOB 419.0 120.7 0.0 8.390 125.22 0.000 0.0 Pipe: 16 0.0 0.0 50.00 140 0.4 12A 418.0 121.2 0.0 D6.000 E:22.0 69.00 0.4 hA 419.0 120.7 0.0 6.280 T:47.0 119.00 0.000 0.0 Pipe: 17 0.0 0.0 65.00 140 0.9 12A 418.0 121.2 0.0 D6.000 E:22.0 69.00 0.9 BOR6 420.0 120.3 0.0 6.280 T:47.0 134.00 0.000 0.0 Pipe: 18 0.0 0.0 95.00 150 0.0 12B 419.0 120.7 0.0 D8.000 E:35.2 102.25 0.0 hA 419.0 120.7 0.0 8.390 T:67.0 197.25 0.000 0.0 Pipe: 19 0.0 0.0 195.00 150 0.4 13A 418.0 121.2 0.0 D8.000 E:35.2 102.25 0.4 12B 419.0 120.7 0.0 8.390 T:67.0 297.25 0.000 0.0 Pipe: 20 0.0 0.0 235.00 150 -0.9 13A 418.0 121.2 0.0 D12.00 E:50.0 161.33 -0.9 14A 416.0 122.0 0.0 12.460 T:111.3 396.33 0.000 0.0 Pipe: 21 0.0 0.0 90.00 150 1.7 15 412.0 123.8 0.0 D12.00 T:111.3 111.34 1.7 14A 416.0 122.0 0.0 12.460 201.34 0.000 0.0 Pipe: 22 0.0 0.0 50.00 150 0.9 16 410.0 124.6 0.0 D12.00 T:111.3 111.34 0.9 15 412.0 123.8 0.0 12.460 161.34 0.000 0.0 NOTES (BASS) (1) Calculations were performed by the HASS 8.7 computer program in accordance with NFPA13 (2017) under license no. 2704110710 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/11/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGH).SDF JOB TITLE: SheaProperties Building H_Carlsbad_CA - Attachment #3 The system has been calculated to provide an average imbalance at each node of 0.014 gpm and a maximum imbalance at any node of 0.154 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.2 ft/sec at pipe 10. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SOURCE under full flow conditions is 125.86 psi with a flow of 600.04 gpm. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 12.460 44.00 98.00 30.00 107.00 34.00 10.00 98.00 181 11' -41M I 1111IN11111 - 1 1411 11 "M 11111 jjllllllllliiillli illflllllllilllllll [11l1UJJJJlI1tUiIIjiJtUj.UjjJjUThljlVJ1liLllTIIiThlWJUl(flWJJLfltii' Illlllllllllllllili illilI)Ill1iIllt[lilllilllii(1111 IflhiTi1flT Illll[IlLiijj II II ii iI.iIiiiiIIlIIIIlll i HIIII'll ff1111 lllIllL!JJjjllJjll I ilillllli I 11111)111 I II IllllllllTTTiI fill I Ill I! I 11i.iJlitlliiiliilililllllll.i'ill'Il lIJUjJllllll1iIliiilllIi(lll! IJ]iIlJll1lIllJUIliIIuu !Tflh11Tl11iIffftlllll ii *ifHrItri I IIIjllllJjllll I li''il1l(lil 11111111 111111 iill I II I1IlliI ljlllulllllllllllilllllliullliiFlill krIihiiiiFdii111Iiiiii1rm1ii JJJJ!IJILUJII Il(llllllllll Iljjjj. ilU1J 11 "'s IljtjjjjIjJ lIll1fl1T ii lllllll $1110111 Ii UJJltiIIJlJjllj.IlLJ Ill IlllTI1J1Illlli11III iffj,.11I II i II IllillIllIlIllIli, lllIllIl lllllj(IJIIUIL:'l ljJJ1jJjJj.fljjJJjLJJ.fi I tIlllilllilIIlIIIjlIlliIllliII Hill 1111H1]'ffiIj h II1h i 11 *fllMrIftf l[IlIllllllIlJli illliIilTflTlffI 50 11 ffflThTflTlli ill Ill ilTiii, 'lf Th' llllllltlllllllljlillllIIIll'illIli iiTfflil)luliiIlllilflhllfllflThTil I IlllIl1il111 I II Ii I II I II 1111 1111 'I IIl IVJjlJ1lllIIIlij1IlltJllL)jjjjjII I 111Ill1il11IlJ111iIFt1iT111I1iI! rIll11-llf 600gpm @ 35psi llliiiffflUhiWi! II 1IIIII11I1TIITIII[ll[!I1illl IiJJJ.11J11tlIIIi11IJ1Ffl1lJllil II lIlT III 11111 11111 111111 111111111 IL. ill I ._ 'WJ.lI.p.tilljillluj]IIJIIIJIIIJ lilll111iiFiTIllIIlTIII Iii II I1111r, Ill I Ill I it III III, fill R" "Ill I UI T ii 11 11 :11 i!Jlii[iUiiI,Illh1llhJ hIll11 III II Ill ''\ II UIHI 11 ill1111 1111thj II 0 1000 2000 3000 4000 Flow (gpm) 150 140 130 120 110 100 90 80 70 60 40 30 20 10 3G PAGE 1OF10 1 WATER SUPPLY SITE SURVEY PROJECT: Shea Properties FIRE SPRINKLER DEMAND LOCATION: Building G CITY/STATE: Carlsbad, CA Static (psi) Residual (psi) Flow (gpm) 126 109 8000 Gauge Hydrant Building FFE Elevation (ft) (ft) 410 420 Outlet Diameter #1 (in) Coefficient #1 Hydran it Pitot #1 (psi) Outlet Diameter #2 (in) Hydrant Coefficient #2 Pitot #2 (psi) Outlet Diameter #3 (in) Hydrant Coefficient #3 Pitot•#3 (psi) Outlet Diameter #4 (in) Hydrant Coefficient #4 Pitot#4 (psi) Gauge Hydrant Location: Flow test results provided by computer modeling Flow Hydrant Location: See Report for Results Test By: Carlsbad Fire Prevention Division [Date: 2/24/2017 ITime: N/A Backflow Prevention: Size: 6-inch Type: Double Check Detector Mfg: AMES Model: 30005S Mfg: Model: Flow Rate (gpm) 0 600 I Static (psi) Residual (psi) Pressure available at test 126 126.0 Elevation Adjustment -4.5 -45 Pressure loss due to friction 0 -4.5 Pressure at base of riser upstream of BFP & meter 121.5 117.0 BFP loss/preload -4 -3 Water meter loss 0 0 Pressure at base of riser downstream of BFP & meter 117.5 114 Safety factor -13 -13 Total base of riser pressure 104.5 101 i.:... eiidii LUi jUi dLIUII Calculated Demands 600 I 35 Additional Demands Pump Test SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGG) .SDF JOB TITLE: SheaProperties Building G Carlsbad CA - Attachment #3 NFPA WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. B PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 126.0 109.0 8000.0 125.9 600.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 600.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 600.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 0.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE NOTES (FT) (PSI) (GPM) 1 410.0 - - - - 125.9 - - - 2 425.0 - - - - 119.3 - - - 3 426.0 - - - - 118.8 - - - 4A 426.0 - - - - 118.7 - - - 5A 426.0 - - - - 116.6 - - - 6A 425.0 - - - - 117.0 - - - BOR3 425.0 - - - - 117.0 - - - 7A 423.0 - - - - 117.6 - - - BA 422.0 - - - - 117.8 - - - BOR4 422.0 - - - - 117.8 - - - 9A 421.0 - - - - 117.8 - - - 9B 421.0 - - - - 117.6 - - - BORS 420.0 HOSE STREAM 117.1 600.0 lOB 419.0 - - - - 118.5 - - - hA 419.0 - - - - 118.5 - - - 12A 418.0 - - - - 118.9 - - - BOR6 420.0 - - - - 118.1 - - - 12B 419.0 - - - - 118.5 - - - 13A 418.0 - - - - 118.9 - - - 14A 416.0 - - - - 119.8 - - - 15 412.0 - - - - 121.5 - - - 16 410.0 - - - - 122.4 - - - SOURCE 410.0 SOURCE 125.9 600.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGG) .SDF JOB TITLE: SheaProperties Building G Carlsbad CA - Attachment #3 NFPA PIPE DATA Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 1 Source 0.0 1.00 150 0.0 SOURCE 410.0 125.9 600.0 2 D12.00 ---- 0.00 0.0 1 410.0 125.9 600.0 12.460 1.00 0.000 0.0 Pipe: 2 0.0 0.0 125.00 150 6.6 1 410.0 125.9 600.0 3 D12.00 T:111.3 111.34 6.5 2 425.0 119.3 600.0 12.460 236.34 0.000 0.1 Pipe: 3 0.0 0.0 95.00 150 0.5 2 425.0 119.3 600.0 4A D12.00 E:50.0 161.33 0.4 3 426.0 118.8 600.0 12.460 T:111.3 256.33 0.000 0.1 Pipe: 4 0.0 0.0 110.00 150 0.1 3 426.0 118.8 600.0 5A D12.00 T:111.3 111.34 0.0 4A 426.0 118.7 600.0 12.460 221.34 0.000 0.1 Pipe: 5 0.0 0.0 200.00 140 2.1 4A 426.0 118.7 600.0 7A D6.000 T:47.0 47.00 0.0 5A 426.0 116.6 600.0 6.280 247.00 0.009 2.1 Pipe: 6 0.0 0.0 110.00 140 0.4 6A 425.0 117.0 0.0 D6.000 T:47.0 47.00 0.4 5A 426.0 116.6 0.0 6.280 157.00 0.000 0.0 Pipe: 7 0.0 0.0 25.00 140 0.0 BOR3 425.0 117.0 0.0 D6.000 T:47.0 52.00 0.0 6A 425.0 117.0 0.0 6.280 G: 5.0 77.00 0.000 0.0 Pipe: 8 0.0 0.0 100.00 150 -1.0 5A 426.0 116.6 600.0 8A D8.000 E:35.2 60.22 -1.3 7A 423.0 117.6 600.0 8.390 L:25.0 160.22 0.002 0.3 Pipe: 9 0.0 0.0 75.00 150 -0.2 7A 423.0 117.6 600.0 9A D8.000 E:35.2 60.22 -0.4 8A 422.0 117.8 600.0 8.390 L:25.0 135.22 0.002 0.3 Pipe: 10 0.0 0.0 75.00 140 0.0 BOR4 422.0 117.8 0.0 D6.000 T:47.0 47.00 0.0 8A 422.0 117.8 0.0 6.280 122.00 0.000 0.0 Pipe: 11 0.0 0.0 125.00 150 -0.1 8A 422.0 117.8 600.0 9B D8.000 T:67.0 67.03 -0.4 9A 421.0 117.8 600.0 8.390 192.03 0.002 0.4 Pipe: 12 0.0 0.0 50.00 140 0.2 9A 421.0 117.8 600.0 BOR5 D8.000 E:31.0 53.00 0.0 9B 421.0 117.6 600.0 8.390 L:22.0 103.00 0.002 0.2 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGG).SDF JOB TITLE: SheaProperties Building G Carlsbad CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 13 H.S. 600.0 Disch E:22.0 75.00 140 0.6 9B 421.0 117.6 0.0 D6.000 L:14.0 41.00 -0.4 BOR5 420.0 117.1 600.0 6.280 G: 5.0 116.00 0.009 1.0 Pipe: 14 0.0 0.0 75.00 150 0.9 lOB 419.0 118.5 0.0 D8.000 T:67.0 67.03 0.9 9B 421.0 117.6 0.0 8.390 142.03 0.000 0.0 Pipe: 15 0.0 0.0 90.00 150 0.0 hA 419.0 118.5 0.0 D8.000 E:35.2 35.22 0.0 lOB 419.0 118.5 0.0 8.390 125.22 0.000 0.0 Pipe: 16 0.0 0.0 50.00 150 0.4 12A 418.0 118.9 0.0 D8.000 E:35.2 102.25 0.4 llA 419.0 118.5 0.0 8.390 T:67.0 152.25 0.000 0.0 Pipe: 17 0.0 0.0 65.00 140 0.9 12A 418.0 118.9 0.0 D6.000 E:22.0 69.00 0.9 BOR6 420.0 118.1 0.0 6.280 T:47.0 134.00 0.000 0.0 Pipe: 18 0.0 0.0 95.00 150 0.0 123 419.0 118.5 0.0 D8.000 E:35.2 102.25 0.0 llA 419.0 118.5 0.0 8.390 T:67.0 197.25 0.000 0.0 Pipe: 19 0.0 0.0 195.00 150 0.4 13A 418.0 118.9 0.0 D8.000 E:35.2 102.25 0.4 12B 419.0 118.5 0.0 8.390 T:67.0 297.25 0.000 0.0 Pipe: 20 0.0 0.0 535.00 150 -0.9 13A 418.0 118.9 0.0 D12.00 E:50.0 161.33 -0.9 14A 416.0 119.8 0.0 12.460 T:111.3. 696.33 0.000 0.0 Pipe: 21 0.0 0.0 90.00 150 1.7 15 412.0 121.5 0.0 D12.00 T:111.3 111.34 1.7 14A 416.0 119.8 0.0 12.460 201.34 0.000 0.0 Pipe: 22 0.0 0.0 50.00 150 0.9 16 410.0 122.4 0.0 D12.00 T:111.3 111.34 0.9 15 412.0 121.5 0.0 12.460 161.34 0.000 0.0 NOTES (HASS) (1) Calculations were performed by the HASS 8.7 computer program in accordance with NFPA13 (2017) under license no. 2704110710 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGG).SDF JOB TITLE: SheaProperties Building G Carlsbad CA - Attachment #3 The system has been calculated to provide an average imbalance at each node of 0.014 gpm and a maximum imbalance at any node of 0.154 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.2 ft/sec at pipe 13. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SOURCE under full -flow conditions is 125.86 psi with a flow of 600.04 gpm. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HHC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 12.460 44.00 98.00 30.00 107.00 34.00 10.00 98.00 150 140 A Observed Flow Test Point 130 110 — — — - Raw Water Flow Test 100 — • #4 Below H 70 cL 60 —#7 Below 50 #9 Below 30 20 10 Target Demand 0 0 1000 2000 3000 4000 5000 6000 7000 8000 Flow (gpm) Iii iii II iii !_l ii mm liii mm imm_imi r iii I Ii iii II i Tii liii iii ii Ii! 11 1 111 Jj ij_ 1 1 mm ii 11 11 Hill Jifil ii liii 111 Iii iii i_jim I 11 ii ii IlIllfflll1II}1l 120 11 lllIllllliiiTil1 [i.iW.!W.lW!U!.ffIHhllIllfflhlI!lIlJllllIIlJJJijllIllllTlllIllllllIlIlIl uiTlilW — II lllullllllllilllllT)i1lllllllllllllil QIiTI1flhIJJ1I(1T1l1T111Tfffl llllllllllllllllllljlllllllliJilllll llllTiflhlliiliiuljjlliflhfllTlllTh I I II '117 DII I I II I 1IIJ II I I II 11111111 II I III I lii I 111111111 111111111 ill ill I 111111 II ' .iIltI I I I II II I I II 11111111 I IjI ll(llIflIlHllmiTh IlIIllllJjjjjjJlI1IlIlllIIlIl II I 1111111 J1TEflh11iT7pm. II I 1111 I II 11111111 liii. Ill) Ill,lu1 I I Ill (Ill II 11111111111111 II III 11111 1111 1111111 11111 90 11 iI.IIIIIuIuIl II-I-iiiII1fiIIfh iIIF11 I1iFi11lli-I-fl Il1 -Iffii1 I III 1 IN I H1.111 4111 1 41111 fill 111, Iffill Will IIIIII P11111111 HIMS 11111111 1 TI" Ill f}IH1'Iillfl Ii I lJJJi]4JiI f IfI*I F1*If1{ llu1ftf II I Iftffl 1*II I*Ur IH I *I* *tf}1* -ft" Ill Mfl{Hfl I{IHM1FI IIIIIIIIIIIIIII — 111 111 I IIIIIIII III III 1 1 I I ll' f1H-ll1' fH-Iftf' * I1fI fl* FFFJ*Ff' IIIIJJJ.fI fff 40 4—f '' . 111111. IJ.'I Ill I II I 11111 II I 11111 III Il 11111 600gprn 35psi III II I 1111 III II II 1111 III 11111 11111 11111111111111111 1 I Ii Ill IlIllIllIlillI 1111111 111111 III I I'_J I' "111 II' 11 11 111 111111 iI11llIl''JlI'lIIIllIlliIill .JIiI1TtII41T'IIf.... I.jjhiij.lJJjj. iJJ]J1XIEH))11)II Hilit.' ii.I1.ii IliEL 11J ItI I Ill I I I III Ill Ijj ll.ulj IJ\I II 11111 I II III hIll II II IlI_ I_Ill Ill' IIIIjJ I I 11111 I 1_ii I I ATFACHMENT# 3D PAGE 10F WATER SUPPLY SITE SURVEY PROJECT: Shea Properties FIRE SPRINKLER DEMAND LOCATION: Building D CITY/STATE: Carlsbad, CA Static (psi) Residual (psi) Flow (gpm) 126 109 8000 Gauge Hydrant Building FFE Elevation (ft) (ft) 410 420 Outlet Diameter #1 (in) Hydrant Coefficient #1 Pitot #1 (psi) Outlet Diameter #2(m) Hydrant Coefficient #2 . Pitot #2 (psi) - Outlet . Diameter #3 (in) Hydrant Coefficient #3 Pitot #3 (psi) Outlet Diameter #4(m) Hydrant Coefficient #4 Pitot #4 - (psi) Gauge Hydrant Location: Flow test results provided by computer modeling Flow Hydrant Location: See Report for Results Test By: Carlsbad Fire Prevention Division IDate: 2/24/2017 ITime: N/A Backflow Prevention: Size: 6-inch Type: Double Check Detector Mfg: AMES Model: QQQS Mfg: Model: Flow Rate (gpm) 0 600 I Static (psi) Residual (psi) Pressure available at test 126 126.0 Elevation Adjustment -4.5 -4.5 Pressure loss due to friction- 0 -4.5 Pressure at base of riser S upstream of BFP & meter 121.5 117.0 BFP loss/preload -4 -3 Water meter loss - 0 0 Pressure at base of riser -. downstream of BFP & meter 117.5 114 Safety factor -13 -13 9. Total base of riser pressure 104.5 101 Calculated Demands 600 I 35 Additional Demands I PumpTest - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGD).SDF JOB TITLE: SheaProperties Building D Carlsbad CA - Attachment #3 NFPA WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 126.0 109.0 8000.0 125.9 600.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 600.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 600.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 0.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE NOTES (FT) (PSI) (GPM) 1 410.0 - - - - 125.9 - - - 2 425.0 - - - - 119.3 - - - 3 426.0 - - - - 118.8 - - - 4A 426.0 - - - - 118.7 - - - 5A 426.0 - - - - 118.2 - - - 6A 425.0 - - - - 118.7 - - - BOR3 425.0 - - - - 118.7 - - - 7A 423.0 - - - - 119.2 - - - 8A 422.0 - - - - 119.4 - - - BOR4 422.0 - - - - 119.4 - - - 9A 421.0 - - - - 119.5 - - - 9B 421.0 - - - - 119.3 - - - BOR5 420.0 - - - - 119.7 - - - lOB 419.0 - - - - 119.9 - - - hA 419.0 - - - - 119.7 - - - 12A 418.0 - - - - 119.1 - - - BOR6 420.0 HOSE STREAM 117.0 600.0 12B 419.0 - - - - 119.7 - - - 13A 418.0 - - - - 120.1 - - - 14A 416.0 - - - - 121.0 - - - 15 412.0 - - - - 122.7 - - - 16 410.0 - - - - 123.6 - - - SOURCE 410.0 SOURCE 125.9 600.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGD).SDF JOB TITLE: SheaProperties Building DCarlsbadCA - Attachment #3 NFPA PIPE DATA Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 1 Source 0.0 1.00 150 0.0 SOURCE 410.0 125.9 600.0 2 D12.00 ---- 0.00 0.0 1 410.0 125.9 600.0 12.460 1.00 0.000 0.0 Pipe: 2 0.0 0.0 125.00 150 6.6 1 410.0 125.9 600.0 3 D12.00 T:111.3 111.34 6.5 2 425.0 119.3 600.0 12.460 236.34 0.000 0.1 Pipe: 3 0.0 0.0 95.00 150 0.5 2 425.0 119.3 600.0 4A D12.00 E:50.0 161.33 0.4 3 426.0 118.8 600.0 12.460 T:111.3 256.33 0.000 0.1 Pipe: 4 0.0 0.0 110.00 150 0.1 3 426.0 118.8 600.0 5A D12.00 T:111.3 111.34 0.0 4A 426.0 118.7 600.0 12.460 221.34 0.000 0.1 Pipe: 5 0.0 0.0 200.00 150 0.5 4A 426.0 118.7 600.0 7A 08.000 T:67.0 67.03 0.0 5A 426.0 118.2 600.0 8.390 267.03 0.002 0.5 Pipe: 6 0.0 0.0 110.00 140 0.4 6A 425.0 118.7 0.0 D6.000 T:47.0 47.00 0.4 5A 426.0 118.2 0.0 6.280 157.00 0.000 0.0 Pipe: 7 0.0 0.0 25.00 140 0.0 BOR3 425.0 118.7 0.0 D6.000 T:47.0 52.00 0.0 6A 425.0 118.7 0.0 6.280 G: 5.0 77.00 0.000 0.0 Pipe: 8 0.0 0.0 100.00 150 -1.0 5A 426.0 118.2 600.0 8A 08.000 E:35.2 60.22 -1.3 7A 423.0 119.2 600.0 8.390 L:25.0 160.22 0.002 0.3 Pipe: 9 0.0 0.0 75.00 150 -0.2 7A 423.0 119.2 600.0 9A D8.000 E:35.2 60.22 -0.4 8A 422.0 119.4 600.0 8.390 L:25.0 135.22 0.002 0.3 Pipe: 10 0.0 0.0 75.00 140 0.0 BOR4 422.0 119.4 0.0 D6.000 T:47.0 47.00 0.0 8A 422.0 119.4 0.0 6.280 122.00 0.000 0.0 Pipe: 11 0.0 0.0 125.00 150 -0.1 8A 422.0 119.4 600.0 9B D8.000 T:67.0 67.03 -0.4 9A 421.0 119.5 600.0 8.390 192.03 0.002 0.4 Pipe: 12 0.0 0.0 50.00 150 0.2 9A 421.0 119.5 600.0 lOB D8.000 E:35.2 60.22 0.0 9B 421.0 119.3 600.0 8.390 L:25.0 110.22 0.002 0.2 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGD).SDF JOB TITLE: SheaProperties Building D Carlsbad CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf/ft. (Pf) Pipe: 13 0.0 0.0 E:22.0 75.00 140 0.4 BOR5 420.0 119.7 0.0 D6.000 L:14.0 41.00 0.4 9B 421.0 119.3 0.0 6.280 G: 5.0 116.00 0.000 0.0 Pipe: 14 0.0 0.0 75.00 150 -0.6 9B 421.0 119.3 600.0 hA D8.000 T:67.0 67.03 -0.9 lOB 419.0 119.9 600.0 8.390 142.03 0.002 0.3 Pipe: 15 0.0 0.0 90.00 150 0.2 lOB 419.0 119.9 600.0 12A D8.000 E:35.2 35.22 0.0 hA 419.0 119.7 600.0 8.390 125.22 0.002 0.2 Pipe: 16 0.0 0.0 50.00 140 0.6 hA 419.0 119.7 600.0 BOR6 D6.000 E:22.0 69.00 -0.4 12A 418.0 119.1 600.0 6.280 T:47.0 119.00 0.009 1.0 Pipe: 17 H.S. 600.0 Disch 65.00 140 2.0 12A 418.0 119.1 0.0 D6.000 E:22.0 69.00 0.9 BOR6 420.0 117.0 600.0 6.280 T:47.0 134.00 0.009 1.2 Pipe: 18 0.0 0.0 95.00 150 0.0 12B 419.0 119.7 0.0 D8.000 E:35.2 102.25 0.0 hA 419.0 119.7 0.0 8.390 T:67.0 197.25 0.000 0.0 Pipe: 19 0.0 0.0 195.00 150 0.4 13A 418.0 120.1 0.0 D8.000 E:35.2 102.25 0.4 12B 419.0 119.7 0.0 8.390 T:67.0 297.25 0.000 0.0 Pipe: 20 0.0 0.0 535.00 150 -0.9 13A 418.0 120.1 0.0 D12.00 E:50.0 161.33 -0.9 14A 416.0 121.0 0.0 12.460 T:111.3 696.33 0.000 0.0 Pipe: 21 0.0 0.0 90.00 150 1.7 15 412.0 122.7 0.0 D12.00 T:111.3 111.34 1.7 14A 416.0 121.0 0.0 12.460 201.34 0.000 0.0 Pipe: 22 0.0 0.0 50.00 150 0.9 16 410.0 123.6 0.0 D12.00 T:111.3 111.34 0.9 15 412.0 122.7 0.0 12.460 161.34 0.000 0.0 NOTES (HASS) (1) Calculations were performed by the HASS 8.7 computer program in accordance with NFPA13 (2017) under license no. 2704110710 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGD).SDF JOB TITLE: SheaProperties Building D Carlsbad CA - Attachment #3 The system has been calculated to provide an average imbalance at each node of 0.014 gpm and a maximum imbalance at any node of 0.154 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.2 ft/sec at pipe 16. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SOURCE under full flow conditions is 125.86 psi with a flow of 600.04 gpm. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 12.460 44.00 98.00 30.00 107.00 34.00 10.00 98.00 AUACHMENT# 3E PAGE 1 O WATER SUPPLY SITE SURVEY PROJECT: Shea Properties FIRE SPRINKLER DEMAND LOCATION: Building E CITY/STATE: Carlsbad, CA Static (psi) Residual (psi) Flow (gpm) 126 109 8000 Gauge Hydrant Building FFE Elevation (ft) (ft) 410 420 Outlet • Diameter #1 • (in) Hydrant Coefficient #1 • Pitot #1 (psi) Outlet • Diameter #2 (in) Hydrant Coefficient #2 . . . Pitot #2 (psi) Outlet Diameter #3 (in) Hydrant • Coefficient #3 Pitot #3 (psi) Outlet Diameter #4 (in) Hydrant • Coefficient #4 Pitot #4 (psi) Gauge Hydrant Location: Flow test results provided by computer modeling Flow Hydrant Location: See Report for Results Test By: Carlsbad Fire Prevention Division IDate: 2/24/2017 ITime: N/A Backflow Prevention: Size: 6-inch Type: Double Check Detector Mfg: AMES Model: 3PS Mfg: Model: 150 140 1111111 11 Hit MI IN fl 11 1011111 1 lit hillftil !fill A Observed Flow Test Point 130 IIIII 120 110 - - - - Raw Water Flow Test 100 90 11 WE I fill - • #4 Below 11.11 111I.I.Mil !11111 11 1.1114 11 111 1111 11 W ILI till I I j80 III i1i U Hit 70 f 117 Ill 11 Ill Iffirl 111 11 . .1 pitl - _#7 Below o- 60 It Ll 11 50 lit 40 1.1 "HIIIIII 111 1 1 ______ #9 Below 30 1 11 111111 Ill 11 Ill 20 10 Ill I Hill 111 Ill 11 • Target Demand 0 0 1000 2000 3000 4000 5000 6000 7000 8000 Flow (gpm) * llI III1{11f *II1ftfFfl lii II ihJlitlfil{ ii FiIJIIIJIIBJILiJ1 iU1uuiI.lRl 1.J.LIjj.'.wj33J IllilIliji IJJJJJ I !jJJ,J.j4jJJJIllJi r:j iJl11I 11 Ii 1ijJllllijjllil II l.1JJMIjLL.l II it H IJ1.UIWJIL.ILI.IUJJIJ IJjJ1jJHl 1 1 I HIlL Hi I IIIJJII I tJ.IJJJiJiJ....IJJJJJJJJJJI(11'JJ jjJjJjIJJjJJJjfl Ii.LlJi.i•lJJJ.IJJIIJJ.l.ILIJJJ.JJJJJ.I I tIJJJII IIIi IJJJJJi1IJJJ.IJJiJJJ 7111-111111 UJiJJ!Lui HliiJiJjjlfl :JLjLl I .I'JIJ.J IIIljjjJj 1111 I II I lflii II I 111111 II IIIIlIIiifI1III lI1jJjlIl IlJjJllI 1111(111 II 1111111 I1il11iIiI il 1111 IIII 11111111111 11111 111111 II IIlIIlIIliillIJl 'I iIIIl1flllIlllll I IllIllIlli 1II1T1IIIII ITi11l I1MftIfi à'M I Ihi1HIf1 i ìii1i1iFi fiWh1ftffliT1 In{ Ht ii fliHmliToTffl 1f1IMf H IIiii pi i1I:i I II FIIFIIMH 11111 II It, 1111 hmfrh1111 IIH1V IfI HTHiIIL lMT11TfllCi1i I IIiflhiII I H II I 1111 II I Ill Ill It III IJIIJI IlIllIllIll,TtH1lIillI I I1IiII11jJ III I II IliliTtI IIIiltI 1111 II IIIiiIJII IlITilIlIlIlIl IlIlIlilIll Ii 11111 iIIIIIIIJiI 111111 111111111111 11111 IIIIIilIII III 111111 Ill 600gpm @ 35 psi IillIftiiH'i 1IMJflft lliFIfflftifIth TIiiTfflifrllIlIIft iiiihmiiifii1i 1b1111 lJJlIiMiIIiIIiIiII}llJiifi{JJ.ti{1J 1I*if1-ilifih fffIIllI} II flhTffhT{biffll{i i III 1.1_U .11! I I .11 lIft 111111 111111 IL lilt IftI_iUlJjjjlub'II\IlI 11111111 Lilhiflulk I11I iI 'IIIIIIIII!IIII IJI1J 111111 IIJJIIIiIlI1114 1 9 TiHfnifr lI_It 111111 1111! 1Wl1lIIlilIIlJi•i!JIJJJJIIILIILLIJ IlIllIliRl. 1H4{!dHIi fill C, IF11 Flow Rate (gpm) 0 600 I Static (psi) Residual (psi) Pressure available at test 126 126.0 Elevation Adjustment -4.5 -4.5 Pressure loss due to friction 0 -4.5 Pressure at base of riser upstream of BFP & meter 121.5 117.0 S. BFP loss/preload -4 -3 Water meter loss 0 0 Pressure at base of riser downstream of BFP & meter 117.5 114 Safety factor -13 -13 Total base of riser pressure 104.5 101 r..l.. , Calculated Demands 600 I 35 Additional Demands Pump Test SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGE).SDF JOB TITLE: SheaProperties Building E Carlsbad CA - Attachment #3 NFPA WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 126.0 109.0 8000.0 125.9 600.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 600.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 600.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 0.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE NOTES (FT) (PSI) (GPM) 1 410.0 - - - - 125.9 - - - 2 425.0 - - - - 119.3 - - - 3 426.0 - - - - 118.8 - - - 4A 426.0 - - - - 118.7 - - - 5A 426.0 - - - - 118.2 - - - 7A 423.0 - - - - 119.3 - - - 8A 422.0 - - - - 119.4 - - - 9A 422.0 - - - - 119.1 - - - 9B 421.0 - - - - 119.3 - - - lOB 419.0 - - - - 119.9 - - - hA 419.0 - - - - 119.6 - - - 12B 418.0 - - - - 119.8 - - - 13A 418.0 - - - - 119.4 - - - 13B 416.0 - - - - 120.1 - - - BOR7 420.0 HOSE STREAM 117.3 600.0 14B 416.0 - - - - 120.1 - - - 16A 416.0 - - - - 120.1 - - - 15 418.0 - - - - 119.3 - - - 10A 420.0 - - - - 118.4 - - - 11 419.0 - - - - 118.8 - - - 12 419.0 - - - - 118.8 - - - 13 418.0 - - - - 119.3 - - - 14 410.0 - - - - 122.7 - - - 15A 418.0 - - - - 119.3 - - - 16B 417.0 - - - - 119.7 - - - BOR8 415.0 - - - - 120.6 - - - SOURCE 410.0 SOURCE 125.9 600.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGE).SDF JOB TITLE: SheaProperties Building E_Carlsbad_CA - Attachment #3 NFPA PIPE DATA Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 1 Source 0.0 1.00 150 0.0 SOURCE 410.0 125.9 600.0 2 D12.00 ---- 0.00 0.0 1 410.0 125.9 600.0 12.460 1.00 0.000 0.0 Pipe: 2 0.0 0.0 125.00 150 6.6 1 410.0 125.9 600.0 3 D12.00 T:111.3 111.34 6.5 2 425.0 119.3 600.0 12.460 236.34 0.000 0.1 Pipe: 3 0.0 0.0 95.00 150 0.5 2 425.0 119.3 600.0 4A D12.00 T:111.3 111.34 0.4 3 426.0 118.8 600.0 12.460 206.34 0.000 0.1 Pipe: 4 0.0 0.0 110.00 150 0.1 3 426.0 118.8 600.0 5A D12.00 T:111.3 111.34 0.0 4A 426.0 118.7 600.0 12.460 221.34 0.000 0.1 Pipe: 5 0.0 0.0 200.00 150 0.5 4A 426.0 118.7 600.0 7A D8.000 T:67.0 67.03 0.0 5A 426.0 118.2 600.0 8.390 267.03 0.002 0.5 Pipe: 6 0.0 0.0 100.00 150 -1.0 5A 426.0 118.2 600.0 8A D8.000 E:35.2 60.22 -1.3 7A 423.0 119.3 600.0 8.390 L:25.0 160.22 0.002 0.3 Pipe: 7 0.0 0.0 75.00 150 -0.2 7A 423.0 119.3 600.0 9A D8.000 E:35.2 60.22 -0.4 8A 422.0 119.4 600.0 8.390 L:25.0 135.22 0.002 0.3 Pipe: 8 0.0 0.0 125.00 150 0.4 8A 422.0 119.4 600.0 9B D8.000 T:67.0 67.03 0.0 9A 422.0 119.1 600.0 8.390 192.03 0.002 0.4 Pipe: 9 0.0 0.0 50.00 150 -0.2 9A 422.0 119.1 600.0 103 D8.000 E:35.2 60.22 -0.4 9B 421.0 119.3 600.0 8.390 L:25.0 110.22 0.002 0.2 Pipe: 10 0.0 0.0 75.00 150 -0.6 9B 421.0 119.3 600.0 hA D8.000 E:35.2 60.22 -0.9 lOB 419.0 119.9 600.0 8.390 L:25.0 135.22 0.002 0.3 Pipe: 11 0.0 0.0 90.00 150 0.3 lOB 419.0 119.9 600.0 12B D8.000 E:35.2 60.22 0.0 hA 419.0 119.6 600.0 8.390 L:25.0 150.22 0.002 0.3 Pipe: 12 0.0 0.0 90.00 150 -0.2 hA 419.0 119.6 600.0 13A D8.000 E:35.2 35.22 -0.4 12B 418.0 119.8 600.0 8.390 125.22 0.002 0.2 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGE).SDF JOB TITLE: SheaProperties Building E Carlsbad CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node/ Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf/ft. (Pf) Pipe: 13 0.0 0.0 200.00 150 0.5 12B 418.0 119.8 600.0 13B D8.000 E:35.2 60.22 0.0 13A 418.0 119.4 600.0 8.390 L:25.0 260.22 0.002 0.5 Pipe: 14 0.0 0.0 125.00 150 -0.8 13A 418.0 119.4 600.0 BOR7 D12.00 E:50.0 161.33 -0.9 13B 416.0 120.1 600.0 12.460 T:111.3 286.33 0.000 0.1 Pipe: 15 H.S. 600.0 Disch 75.00 140 2.8 13B 416.0 120.1 0.0 D6.000 T:47.0 52.00 1.7 BOR7 420.0 117.3 600.0 6.280 G: 5.0 127.00 0.009 1.1 Pipe: 16 0.0 0.0 25.00 150 0.0 14B 416.0 120.1 0.0 D12.00 T:111.3 111.34 0.0 13B 416.0 120.1 0.0 12.460 136.34 0.000 0.0 Pipe: 17 0.0 0.0 25.00 150 0.0 16A 416.0 120.1 0.0 D12.00 T:111.3 111.34 0.0 14B 416.0 120.1 0.0 12.460 136.34 0.000 0.0 Pipe: 18 0.0 0.0 225.00 150 -0.9 15 418.0 119.3 0.0 D12.00 E:50.0 49.99 -0.9 16A 416.0 120.1 0.0 12.460 274.99 0.000 0.0 Pipe: 19 0.0 0.0 50.00 150 0.9 15 418.0 119.3 0.0 D12.00 E:50.0 49.99 0.9 10A 420.0 118.4 0.0 12.460 99.99 0.000 0.0 Pipe: 20 0.0 0.0 725.00 150 0.4 11 419.0 118.8 0.0 D12.00 T:111.3 111.34 0.4 bA 420.0 118.4 0.0 12.460 836.34 0.000 0.0 Pipe: 21 0.0 0.0 115.00 150 0.0 12 419.0 118.8 0.0 D12.00 T:111.3 111.34 0.0 11 419.0 118.8 0.0 12.460 226.34 0.000 0.0 Pipe: 22 0.0 0.0 95.00 150 0.4 13 418.0 119.3 0.0 D12.00 T:111.3 111.34 0.4 12 419.0 118.8 0.0 12.460 206.34 0.000 0.0 Pipe: 23 0.0 0.0 125.00 150 -3.5 13 418.0 119.3 0.0 D12.00 T:111.3 111.34 -3.5 14 410.0 122.7 0.0 12.460 236.34 0.000 0.0 Pipe: 24 0.0 0.0 115.00 140 -0.9 15A 418.0 119.3 0.0 D8.000 T:59.0 59.00 -0.9 14B 416.0 120.1 0.0 8.390 174.00 0.000 0.0 Pipe: 25 0.0 0.0 85.00 140 0.4 16B 417.0 119.7 0.0 D6.000 T:47.0 52.00 0.4 15A 418.0 119.3 0.0 6.280 G: 5.0 137.00 0.000 0.0 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page Iq DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGE).SDF JOB TITLE: SheaPropertiesBuildirig E Carlsbad CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 26 0.0 0.0 25.00 140 -0.9 16B 417.0 119.7 0.0 D6.000 E:22.0 22.00 -0.9 BOR8 415.0 120.6 0.0 6.280 47.00 0.000 0.0 NOTES (HASS) Calculations were performed by the HASS 8.7 computer program in accordance with NFPA13 (2017) under license no. 2704110710 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.012 gpm and a maximum imbalance at any node of 0.154 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.2 ft/sec at pipe 15. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SOURCE under full flow conditions is 125.86 psi with a flow of 600.04 gpm. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 12.460 44.00 98.00 30.00 107.00 34.00 10.00 98.00 Notes H1II.11.11.1 1 H{If4DI iffllfIi *f jj]jJJjjjl.l I IiIlIIIIIIll Ijj.lj.ljj.l.l.lJJ.(i lllll)IjJJ LIIi iiI1T7 II I g11411111111ill, 1111 111111.....IJ...iJ. III! II II 11 if H11,11 11)11 II.U!.II.l 111111 I+11!JII III liii II111iiIIItI ''lilllJjjlj_ljjJ IllIi uh1iFl 1 '_1llLliljl[i1l 1li 9i1111ThTl Ii ffi11T1)li Ill! I II III liii I II Fir lil lilllltlltflill_tli fill llliiiliilll El lllllll I (ill 11111111 III lllil If (Ill fill 11111(11111111111111111 1111111 lii 1111 1t!tjj{IIi IJlliIItIJII I11T1ITi1llI 1111111111 I 11111 111111) tIllJl liii. Ii. I I IlIJlilI II II Ii I Ill ii I ill I 11111)1111 lill Illil ftIt IfIfIf} III II I 111111111 IillIlIlIiIll1IIII 11111111 III III 1111111 1111111 liii II H IIII 11111 llhi1ftFIIfllh1 i 1frllHi II fFFIII11*1 1 FfIfllfF Ill1 Fi1H- 11111 1111111111 liifiL 4i111iIJii i111110111iJ Jfff J1Jft1 II11JfiJii 'Jftfiii 1111111 1111111 Il Ill I I Iii Ill II fiji I l3II TEIII Rh. iii) lIll! III III ; WhIil! 11111 ii I III II 11111111111 III ii Ii 111111 II II IllIllIllIllIl II llllhilijhilll II III I 1111111 1111 11111111 II 11111 III liii I I lIi' 6Ol:gprri i 35psi I I Iil t1i I 11111 1!II I. i illlllflljjil Ii III II 1111 lljhllhllhl Ill Illil II III III I If 111111111 Ill II I III! Ill 1)111111 I I 11111 lj._Jj.J. 1 I 111111 I.......I.l.JJ.I.J. II lJ!IJ.I.! 'II I J...I..J.L. Ill (III Ii -Afflfill 111111 U..J.U.1II...I...IJ II 11 111 1111111111 JJ1WJJJ.J.'L.II II 111111111 IjJJJJJ.1111111 1111111(1111111111 L11 1 I 11 fill I 1.JlillIiJ.i U{iill ii\41I Ill nI 11 . .11hiJi- 1'L fIIffllft111 ft! ti I f1iiftllftii1L IIftHtiflilftll.lu Ill if 11 11 150 140 130 120 110 100 90 80 70 ci) 60 so 40 30 20 10 (.I A Observed Flow Test Point - - - - Raw Water Flow Test - • #4 Below - -#7 Below #9 Below Target Demand AITACHMENT#3F PAGE 1OF WATER SUPPLY SITE SURVEY PROJECT: Shea Properties FIRE SPRINKLER DEMAND LOCATION: Building F CITY/STATE: Carlsbad, CA Static (psi) Residual (psi) Flow (gpm) 126 109 8000 Gauge Hydrant Building FFE. Elevation (ft) (ft) 410 415 Outlet Diameter #1 Hydrant Coefficient #1 . . Pitot #1 (psi) Outlet . Diameter #2 (in) Hydrant Coefficient #2 (in) Pitot #2 (psi) Outlet Diameter #3 . (in) Hydrant Coefficient- #3 - . Pitot#3 . (psi) Outlet Diameter #4 (in) Hydrant . Coefficient #4 Pitot#4 (psi) Gauge Hydrant Location: Flow test results provided by computer modeling Flow Hydrant Location: See Report for Results Test By: Carlsbad Fire Prevention Division IDate: 2/24/2017 ITime: N/A Backflow Prevention: Size: 6-inch Type: Double Check Detector Mfg: AMES Model: 300OSS Mfg: Model: 0 1000 2000 3000 4000 5000 6000 7000 8000 Flow (gpm) Flow Rate (gpm) 0 600 I Static (psi) Residual (psi) - - - 1. Pressure available at test 126 126.0 2. Elevation Adjustment -2 -2 3. Pressure loss due to friction 0 -5 4. Pressure at base of riser upstream of BFP & meter 124 119.0 5 BFP loss/preload -4 -3 Water meter loss 0 0 Pressure at base of riser downstream of BFP & meter 120 116 Safety factor -13 -13 9 Total base of riser pressure 107 103 r...l:..... r.i.:..... Calculated Demands 600 I 35 Additional Demands - PumpTest - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGF) .SDF JOB TITLE: SheaProperties Building F_Carlsbad_CA - Attachment #3 NFPA WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 126.0 109.0 8000.0 125.9 600.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 600.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 600.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 0.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE NOTES (FT) (PSI) (GPM) 1 410.0 - - - - 125.9 - - - 2 425.0 - - - - 119.3 - - - 3 426.0 - - - - 118.8 - - - 4A 426.0 - - - - 118.7 - - - 5A 426.0 - - - - 118.2 - - - 7A 423.0 - - - - 119.3 - - - 8A 422.0 - - - - 119.4 - - - 9A 422.0 - - - - 119.1 - - - 9B 421.0 - - - - 119.3 - - - lOB 419.0 - - - - 119.9 - - - hA 419.0 - - - - 119.6 - - - 12B 418.0 - - - - 119.8 - - - 13A 418.0 - - - - 119.4 - - - 13B 416.0 - - - - 120.1 - - - BOR7 420.0 - - - - 118.4 - - - 14B 416.0 - - - - 120.1 - - - 16A 416.0 - - - - 120.1 - - - 15 418.0 - - - - 119.2 - - - bA 420.0 - - - - 118.4 - - - 11 419.0 - - - - 118.8 - - - 12 419.0 - - - - 118.8 - - - 13 418.0 - - - - 119.2 - - - 14 410.0 - - - - 122.7 - - - 15A 418.0 - - - - 118.9 - - - 16B 417.0 - - - - 118.1 - - - BOR8 415.0 HOSE STREAM 118.6 600.0 SOURCE 410.0 SOURCE 125.9 600.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGF) .SDF JOB TITLE: SheaProperties Building F_Carlsbad_CA - Attachment #3 NFPA PIPE DATA Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot.(Q) Disch Act ID (ft.) T Pf/ft. (Pf) Pipe: 1 Source 0.0 1.00 150 0.0 SOURCE 410.0 125.9 600.0 2 D12.00 ---- 0.00 0.0 1 410.0 125.9 600.0 12.460 1.00 0.000 0.0 Pipe: 2 0.0 0.0 125.00 150 6.6 1 410.0 125.9 600.0 3 D12.00 T:111.3 111.34 6.5 2 425.0 119.3 600.0 12.460 236.34 0.000 0.1 Pipe: 3 0.0 0.0 95.00 150 0.5 2 425.0 119.3 600.0 4A D12.00 T:111.3 111.34 0.4 3 426.0 118.8 600.0 12.460 206.34 0.000 0.1 Pipe: 4 0.0 0.0 110.00 150 0.1 3 426.0 118.8 600.0 5A D12.00 T:111.3 111.34 0.0 4A 426.0 118.7 600.0 12.460 221.34 0.000 0.1 Pipe: 5 0.0 0.0 200.00 150 0.5 4A 426.0 118.7 600.0 7A D8.000 T:67.0 67.03 0.0 5A 426.0 118.2 600.0 8.390 267.03 0.002 0.5 Pipe: 6 0.0 0.0 100.00 150 -1.0 5A 426.0 118.2 600.0 8A D8.000 E:35.2 60.22 -1.3 7A 423.0 119.3 600.0 8.390 L:25.0 160.22 0.002 0.3 Pipe: 7 0.0 0.0 75.00 150 -0.2 7A 423.0 119.3 600.0 9A D8.000 E:35.2 60.22 -0.4 8A 422.0 119.4 600.0 8.390 L:25.0 135.22 0.002 0.3 Pipe: 8 0.0 0.0 125.00 150 0.4 8A 422.0 119.4 600.0 9B D8.000 T:67.0 67.03 0.0 9A 422.0 119.1 600.0 8.390 192.03 0.002 0.4 Pipe: 9 0.0 0.0 50.00 150 -0.2 9A 422.0 119.1 600.0 lOB D8.000 E:35.2 60.22 -0.4 9B 421.0 119.3 600.0 8.390 L:25.0 110.22 0.002 0.2 Pipe: 10 0.0 0.0 75.00 150 -0.6 9B 421.0 119.3 600.0 hA D8.000 E:35.2 60.22 -0.9 lOB 419.0 119.9 600.0 8.390 L:25.0 135.22 0.002 0.3 Pipe: 11 0.0 0.0 90.00 150 0.3 lOB 419.0 119.9 600.0 12B D8.000 E:35.2 60.22 0.0 llA 419.0 119.6 600.0 8.390 L:25.0 150.22 0.002 0.3 Pipe: 12 0.0 0.0 90.00 150 -0.2 ilA 419.0 119.6 600.0 13A D8.000 E:35.2 35.22 -0.4 12B 418.0 119.8 600.0 8.390 125.22 0.002 0.2 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGF).SDF JOB TITLE: SheaProperties Building F_Carlsbad_CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) To Node El (ft) PT Tot.(Q) Disch Act ID (ft.) T Pf/ft. (Pf) Pipe: 13 0.0 0.0 200.00 150 0.5 12B 418.0 119.8 600.0 13B D8.000 E:35.2 60.22 0.0 13A 418.0 119.4 600.0 8.390 L:25.0 260.22 0.002 0.5 Pipe: 14 0.0 0.0 125.00 150 -0.8 13A 418.0 119.4 600.0 14B D12.00 E:50.0 161.33 -0.9 13B 416.0 120.1 600.0 12.460 T:111.3 286.33 0.000 0.1 Pipe: 15 0.0 0.0 75.00 140 -1.7 BOR7 420.0 118.4 0.0 D6.000 T:47.0 52.00 -1.7 13B 416.0 120.1 0.0 6.280 G: 5.0 127.00 0.000 0.0 Pipe: 16 0.0 0.0 25.00 150 0.0 13B 416.0 120.1 600.0 15A D12.00 T:111.3 111.34 0.0 14B 416.0 120.1 600.0 12.460 136.34 0.000 0.0 Pipe: 17 0.0 0.0 25.00 150 0.0 16A 416.0 120.1 0.0 D12.00 T:111.3 111.34 0.0 14B 416.0 120.1 0.0 12.460 136.34 0.000 0.0 Pipe: 18 0.0 0.0 225.00 150 -0.9 15 418.0 119.2 0.0 D12.00 E:50.0 49.99 -0.9 16A 416.0 120.1 0.0 12.460 274.99 0.000 0.0 Pipe: 19 0.0 0.0 50.00 150 0.9 15 418.0 119.2 0.0 D12.00 E:50.0 49.99 0.9 10A 420.0 118.4 0.0 12.460 99.99 0.000 0.0 Pipe: 20 0.0 0.0 725.00 150 0.4 11 419.0 118.8 0.0 D12.00 T:111.3 111.34 0.4 10A 420.0 118.4 0.0 12.460 836.34 0.000 0.0 Pipe: 21 0.0 0.0 115.00 150 0.0 12 419.0 118.8 0.0 D12.00 T:111.3 111.34 0.0 11 419.0 118.8 0.0 12.460 226.34 0.000 0.0 Pipe: 22 0.0 0.0 95.00 150 0.4 13 418.0 119.2 0.0 D12.00 T:111.3 111.34 0.4 12 419.0 118.8 0.0 12.460 206.34 0.000 0.0 Pipe: 23 0.0 0.0 125.00 150 -3.5 13 418.0 119.2 0.0 D12.00 T:111.3 111.34 -3.5 14 410.0 122.7 0.0 12.460 236.34 0.000 0.0 Pipe: 24 0.0 0.0 115.00 140 1.2 14B 416.0 120.1 600.0 163 D8.000 T:59.0 59.00 0.9 15A 418.0 118.9 600.0 8.390 174.00 0.002 0.4 Pipe: 25 0.0 0.0 85.00 140 0.8 15A 418.0 118.9 600.0 BOR8 D6.000 T:47.0 52.00 -0.4 16B 417.0 118.1 600.0 6.280 G: 5.0 137.00 0.009 1.2 Notes SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/10/2017 C:\HASS\SHEAPROPERTIES CARLSBAD CA 10 6 17(BLDGF).SDF JOB TITLE: SheaProperties Building F_Carlsbad_CA - Attachment #3 Pipe Tag K-fac Add Fl Add Fl To Fit: L C (Pt) Frm Node El (ft) PT (q) Node! Nom ID Eq.Ln. F (Pe) Notes To Node El (ft) PT Tot. (Q) Disch Act ID (ft.) T Pf!ft. (Pf) Pipe: 26 H.S. 600.0 Disch 25.00 140 -0.5 16B 417.0 118.1 0.0 D6.000 E:22.0 22.00 -0.9 BOR8 415.0 118.6 600.0 6.280 47.00 0.009 0.4 NOTES (HASS) Calculations were performed by the HASS 8.7 computer program in accordance with NFPA13 (2017) under license no. 2704110710 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.012 gpm and a maximum imbalance at any node of 0.154 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 6.2 ft/sec at pipe 26. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SOURCE under full flow conditions is 125.86 psi with a flow of 600.04 gpm. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 12.460 44.00 98.00 30.00 107.00 34.00 10.00 98.00