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HomeMy WebLinkAbout6144 INNOVATION WAY; BLDG M; AS070154; Permit9/14/22,11:07 AM AS070154 Permit Data City of Carlsbad Sprinkler Permit 6144 INNOVATION Job Address: WY Permit Type: SPRINK Parcel No: 2132621000 Lot #: 0 Reference No.: PC #: Project Title Permit No: AS070154 Status: ISSUED Applied 6/7/2007 Approved: 6/7/2007 Issued: 6/7/2007 Inspector: TOWERS @ BRESSI, BLDG. M THREE FIRE SPRINKLER INSPECTIONS @ $62/EA Applicant: INDUSTRIAL FIRE SPRINKLER CO., 3845 IMPERIAL AV SAN DIEGO CA 619-266-6030 Owner: PALOMAR AIRPORT ROAD LLC 9171 TOWNE CENTRE DR #460 SAN DIEGO CA Fees ($) Add'I Fees ($) Total ($) Balance ($) 186 0 186 0 about:blarik 1/1 ASoots 4 APPROVE SU BITTED - - Fire Protection by Computer Design INDUSTRIAL FIRE SPRINKLER Co. 3845 IMPERIAL AVE. SAN DIEGO, CA 92113 619-266-6030 Job Name TOWERS AT BRESSI Building : BUILDING M Location : 6144 INNOVATION WAY System : REMOTE AREAI Contract Data File : Towers-M1.wxl Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 INDUSTRIAL FIRE SPRINKLER CO. Page 1 TOWERS AT BRESSI Date 5/2/07 Hydraulic Desian Information Sheet Name - TOWERS AT BRESSI Date - 5/2/07 Location - 6144 INNOVATION WAY Building - BUILDING M System No. - REMOTE AREA1 Contractor - INDUSTRIAL FIRE SPRINKELR CO. Contract No. - Calculated By - M.G. Drawing No. - FP-4 Construction: (X) Combustible ( ) Non-Combustible Ceiling Height - VARIES Occupancy - EXTRA (X) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 (X) Ex.Haz. NFPA 231 ( ) NFPA 231C Figure Curve Other Specific Ruling Made By Date Area of Sprinkler Operation - 3000 System Type Sprinkler/Nozzle Density - .45 (X) Wet Make RELIABLE Area Per Sprinkler - 93 MAX. ( ) Dry Model G VELO Elevation at Highest Outlet - 281 6" ( ) Deluge Size 3/4" Hose Allowance - Inside - ( ) Preaction K-Factor 14.0 Rack Sprinkler Allowance - ( ) Other Temp.Rat.286 Hose Allowance - Outside - 500 Note Calculation Flow Required - Press Required - Summary C-Factor Used: 120 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - 1/31/07 Cap. - T Time of Test - Rated Cap.- Elev.- E Static Press - 75 @ Press - R Residual Press - 74 Elev. - Well Flow - 1780 Proof Flow S Elevation - 385.0 U P Location - GATEWAY RD & INNOVATION WAY P L Source of Information - PERFORMED BY I.F.S., WITNESSED BY CARLSBAD WATER DIST Y C Commodity Class Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled % Palletized % Rack M Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Encap. SR Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non TA Mult. Row ( ) Open Shelf O C R K Flue Spacing Clearance:Storage to Ceiling A Longitudinal Transverse G B Horizontal Barriers Provided: Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 S Y S T E M D E S I G N Water Supply Curve (C) INDUSTRIAL FIRE SPRINKLER CO. Page 2 TOWERS AT BRESSI Date 5/2/07 City Water Supply: Demand: Cl - Static Pressure : 75 Dl - Elevation : 13.210 C2 - Residual Pressure: 74 D2 - System Flow : 1664.41 stem Pressure : 60.700 C2 - Residual Flow : 1780 D2 - SrDemand Hose Adj City) Hose ) D3 - System Demand : 2164.41 Safety Margin : 12.864 150 140 130 P 120 - R° - E 100 S90 s 80 U 70 D2° R6° E5° D3 40 30 20 2' 10 • --Dl- A. 300 600 900 1200 1500 1800 2100 2400 2700 FLOW ( N "1 .85) Computer Programs by Hydratec inc. Route 111 Windham N.H. USA 03087 Fittings Used Summary INDUSTRIAL FIRE SPRINKLER CO. Page 3 TOWERS AT BRESSI Date 5/2/07 Fitting Legend Abbrev. Name 1,4 % 1 11/4 11/2 2 21/2 3 31,4 4 5 6 8 10 12 14 16 18 20 24 E 90 Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 F 45 Elbow 1 1 1 1 2 2 3 3 3 4 5 7 9 11 13 17 19 21 24 28 G Generic Gate Valve 1 1 1 1 1 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 L Long Turn Elbow 1 1 2 2 2 3 4 5 5 6 8 9 13 16 18 24 27 30 34 40 T 90' Flow Th ru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Z Generic Flow Switch 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Pressure I Flow Summary - STANDARD INDUSTRIAL FIRE SPRINKLER CO. Page 4 TOWERS AT BRESSI Date 5/2/07 Node No. Elevation KFact Pt Actual Pn Flow Actual Density Area Press Req. 56 27.875 14 9.14 na 42.32 0.45 90.2 7.0 57 27.875 14 9.19 na 42.45 0.45 90.2 7.0 58 27.875 14 9.38 na 42.89 0.45 93 7.0 53 28.08 14 9.11 na 42.25 0.45 90.2 7.0 54 28.08 14 9.16 na 42.38 0.45 90.2 7.0 55 28.08 14 9.35 na 42.82 0.45 93 7.0 51 28.5 14 9.04 na 42.1 0.45 90 7.0 52 28.5 11.88 - na 48 27.67 14 9.19 na 42.45 0.45 90.2 7.0 49 27.67 14 9.25 na 42.58 0.45 90.2 7.0 50 27.67 14 9.44 na 43.02 0.45 93 7.0 44 27.875 14 8.85 na 41.64 0.45 90 7.0 45 27.875 14 8.9 na 41.76 0.45 90 7.0 46 27.875 14 9.08 na 42.19 0.45 92 7.0 47 27.875 10.19 na 40 28.08 14 8.82 na 41.57 0.45 90 7.0 41 28.08 14 8.87 na 41.69 0.45 90 7.0 42 28.08 14 9.05 na 42.12 0.45 92 7.0 43 28.08 10.15 na 38 28.33 14 15.19 na 54.56 0.45 90 7.0 39 28.33 14 15.28 na 54.72 0.45 90 7.0 36 27.875 14 16.93 na 57.61 0.45 90 7.0 37 27.875 14 17.03 na 57.77 0.45 90 7.0 34 28.08 14 16.86 na 57.49 0.45 90 7.0 35 28.08 14 16.96 na 57.65 0.45 90 7.0 31 28.33 14 9.37 na 42.84 0.45 90.2 7.0 32 28.33 14 9.42 na 42.97 0.45 90.2 7.0 33 28.33 14 9.62 na 43.41 0.45 93 7.0 26 28.5 14 8.37 na 40.5 0.45 90 7.0 27 28.5 11.01 na 28 28.5 12.86 na 29 24.0 15.71 na 30 24.0 15.73 na 19 27.67 14 9.05 na 42.12 0.45 90 7.0 20 27.67 14 9.09 na 42.21 0.45 90 7.0 21 27.67 14 9.23 na 42.52 0.45 90 7.0 22 27.67 10.25 na 23 24.0 15.11 na 24 24.0 15.13 na 25 24.0 15.21 na 15 28.5 14 15.11 na 54.43 0.45 90 7.0 16 28.5 14 15.2 na 54.58 0.45 90 7.0 17 24.0 19.02 na 18 24.0 19.02 na 10 27.67 14 17.01 na 57.75 0.45 90 7.0 11 27.67 14 17.11 na 57.91 0.45 90 7.0 12 24.0 20.75 na 13 24.0 20.75 na 14 24.0 20.77 na 1 28.33 14 9.07 na 42.16 0.45 90 7.0 2 28.33 14 9.12 na 42.28 0.45 90 7.0 3 28.33 14 9.31 na 42.71 0.45 92 7.0 4 28.33 10.44 na 5 24.0 15.73 na 6 24.0 15.9 na 7 24.0 19.03 na 8 24.0 20.93 na Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Flow Summary - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 5 TOWERS AT BRESSI Date 5/2/07 Node No. Elevation K-Fact Pt Actual Pn Flow Density Area Press Actual Req. TRM 24.0 31.68 na BRM 1.0 43.38 na Ml -4.0 46.06 na M2 -4.0 48.37 na M3 -4.0 . 54.79 na A -4.0 60.54 na B -4.0 60.52 na C -4.0 60.5 na D -4.0 61.17 na E -4.0 61.44 na TEST -2.0 60.7 na M -4.0 59.43 na N -4.0 59.79 na Q -4.0 60.97 na R -4.0 61.24 na F -4.0 59.41 na G -4.0 58.16 na H -4.0 58.12 na J -4.0 57.82 na K -4.0 57.18 na 500.0 L -4.0 57.57 na P -4.0 59.74 na The maximum velocity is 16.82 and it occurs in the pipe between nodes 8 and TRM Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams INDUSTRIAL FIRE SPRINKLER CO. Page 6 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. 'IC" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 56 42.32 2.635 0.0 9.250 9.139 K Factor = 14.00 to 120 0.0 0.0 0.0 57 42.32 0.0058 0.0 9.250 0.054 Vel = 2.49 57 42.45 2.635 0.0 9.000 9.193 K Factor = 14.00 to 120 0.0 0.0 0.0 58 84.77 0.0212 0.0 9.000 0.191 Vel = 4.99 58 42.89 2.635 IT 16.474 1.250 9.384 KFactor= 14.00 to 120 0.0 16.474 0.0 47 127.66 0.0452 0.0 17.724 0.802 Vel = 7.51 0.0 127.66 10.186 KFactor= 40.00 53 42.25 2.635 0.0 9.250 9.108 K Factor = 14.00 to 120 0.0 0.0 0.0 54 42.25 0.0058 0.0 9.250 0.054 Vel = 2.49 54 42.38 2.635 0.0 9.000 9.162 K Factor = 14.00 to 120 0.0 0.0 0.0 55 84.63 0.0212 0.0 9.000 0.191 Vel = 4.98 55 42.81 2.635 1 16.474 1.250 9.353 K Factor = 14.00 to 120 0.0 16.474 0.0 43 127.44 0.0451 0.0 17.724 0.799 Vel = 7.50 0.0 127.44 10.152 KFactor= 40.00 51 42.10 1.049 IT 5.0 0.500 9.044 K Factor = 14.00 to 120 0.0 5.000 0.0 52 42.1 0.5158 0.0 5.500 2.837 Vel = 15.63 52 0.0 1.38 IT 6.0 1.250 11.881 to 120 0.0 6.000 0.0 28 42.1 0.1357 0.0 7.250 0.984 Vel = 9.03 0.0 42.10 12.865 KFactor= 11.74 48 42.45 2.635 0.0 9.250 9.194 K Factor = 14.00 to 120 0.0 0.0 0.0 49 42.45 0.0059 0.0 9.250 0.055 Vel = 2.50 49 42.58 2.635 0.0 9.000 9.249 KFactor= 14.00 to 120 0.0 0.0 0.0 50 85.03 0.0213 0.0 9.000 0.192 Vel = 5.00 50 43.01 2.635 iT 16.474 1.250 9.441 K Factor = 14.00 to 120 0.0 16.474 0.0 22 128.04 0.0455 0.0 17.724 0.806 Vel= 7.53 0.0 128.04 10.247 K Factor = 40.00 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 7 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 44 41.64 2.635 0.0 9.080 8.847 KFactor= 14.00 to 120 0.0 0.0 0.0 45 41.64 0.0057 0.0 9.080 0.052 Vel = 2.45 45 41.77 2.635 0.0 8.830 8.899 KFactor= 14.00 to 120 0.0 0.0 0.0 46 83.41 0.0206 0.0 8.830 0.182 Vel = 4.91 46 42.18 . 2.635 IT 16.474 8.700 9.081 KFactor= 14.00 to 120 0.0 16.474 0.0 47 125.59 0.0439 0.0 25.174 1.105 Vel= 7.39 47 127.66 2.635 IT 16.474 3.875 10.186 to 120 0.0 16.474 1.678 24 253.25 0.1607 0.0 20.349 3.270 Vel = 14.90 0.0 253.25 15.134 KFactor= 65.10 40 41.57 2.635 0.0 9.080 8.818 K Factor = 14.00 to 120 0.0 0.0 0.0 41 41.57 0.0056 0.0 9.080 0.051 Vel = 2.45 41 41.70 2.635 0.0 8.830 8.869 K Factor = 14.00 to 120 0.0 0.0 0.0 42 83.27 0.0205 0.0 8.830 0.181 Vel = 4.90 42 42.11 2.635 iT 16.474 8.700 9.050 KFactor= 14.00 to 120 0.0 16.474 0.0 43 125.38 0.0438 0.0 25.174 1.102 VeI= 7.38 43 127.45 2.635 1 16.474 4.080 10.152 to 120 0.0 16.474 1.767 25 252.83 0.1602 0.0 20.554 3.293 VeI= 14.87 0.0 252.83 15.212 KFactor= 64.82 38 54.56 2.635 0.0 9.250 15.190 KFactor= 14.00 to 120 0.0 0.0 0.0 39 54.56 0.0093 0.0 9.250 0.086 Vel = 3.21 39 54.72 2.635 2T 32.948 22.080 15.276 KFactor= 14.00 to 120 0.0 32.948 1.875 18 109.28 0.0340 0.0 55.028 1.869 Vel = 6.43 0.0 109.28 19.020 K Factor= 25.06 36 57.61 2.635 0.0 9.250 16.931 KFactor= 14.00 to 120 0.0 0.0 0.0 37 57.61 0.0104 0.0 9.250 0.096 Vel = 3.39 37 57.76 2.635 2T 32.948 21.670 17.027 KFactor= 14.00 to 120 0.0 32.948 1.678 13 115.37 0.0375 0.0 54.618 2.050 Vel = 6.79 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 8 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Filling Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 0.0 115.37 20.755 KFactor= 25.32 34 57.49 2.635 0.0 9.250 16.861 KFactor= 14.00 to 120 0.0 0.0 0.0 35 57.49 0.0103 0.0 9.250 0.095 Vel = 3.38 35 57.65 2.635 2T 32.948 21.830 16.956 K Factor = 14.00 to 120 0.0 32.948 1.767 14 115.14 0.0374 0.0 54.778 2.048 VeI= 6.77 0.0 115.14 20.771 KFactor= 25.26 31 42.84 2.635 0.0 9.250 9.365 K Factor = 14.00 to 120 0.0 0.0 0.0 32 42.84 0.0061 0.0 9.250 0.056 Vel = 2.52 32 42.97 2.635 0.0 9.000 9.421 K Factor = 14.00 to 120 0.0 0.0 0.0 33 85.81 0.0217 0.0 9.000 0.195 Vel = 5.05 33 43.42 2.635 IT 16.474 1.250 9.616 K Factor = 14.00 to 120 0.0 16.474 0.0 4 129.23 0.0463 0.0 17.724 0.820 Vel = 7.60 0.0 129.23 10.436 K Factor= 40.00 26 40.50 1.049 IT 5.0 0.500 8.369 K Factor = 14.00 to 120 0.0 5.000 0.0 27 40.5 0.4800 0.0 5.500 2.640 Vel = 15.03 27 0.0 1.38 IT 6.0 8.700 11.009 to 120 0.0 6.000 0.0 28 40.5 0.1263 0.0 14.700 1.856 Vel = 8.69 28 42.10 2.157 iT 12.307 4.500 12.865 to 120 0.0 12.307 1.949 29 82.6 0.0536 0.0 16.807 0.901 Vel = 7.25 29 0.0 4.26 0.0 8.500 15.715 to 120 0.0 0.0 0.0 30 82.6 0.0019 0.0 8.500 0.016 Vel = 1.86 30 0.0 6.357 0.0 1.000 15.731 to 120 0.0 0.0 0.0 5 82.6 0.0010 0.0 1.000 0.001 Vel = 0.83 0.0 82.60 15.732 KFactor= 20.83 19 42.12 2.635 0.0 6.500 9.051 K Factor = 14.00 to 120 0.0 0.0 0.0 20 42.12 0.0058 0.0 6.500 0.038 Vel = 2.48 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 9 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 20 42.21 2.635 0.0 6.500 9.089 K Factor = 14.00 to 120 0.0 0.0 0.0 21 84.33 0.0209 0.0 6.500 0.136 Vel = 4.96 21 42.52 2.635 IT 16.474 6.370 9.225 K Factor = 14.00 to 120 0.0 16.474 0.0 22 126.85 0.0447 0.0 22.844 1.022 Vel= 7.46 22 128.04 2.635 IT 16.474 3.670 10.247 to 120 0.0 16.474 1.589 23 254.89 0.1627 0.0 20.144 3.277 Vet = 15.00 23 0.0 6.357 0.0 9.750 15.113 to 120 0.0 0.0 0.0 24 254.89 0.0022 0.0 9.750 0.021 Vet = 2.58 24 253.25 6.357 0.0 9.750 15.134 to 120 0.0 0.0 0.0 25 508.14 0.0080 0.0 9.750 0.078 Vet = 5.14 25 252.83 6.357 IT 37.72 3.000 15.212 to 120 0.0 37.720 0.0 6 760.97 0.0169 0.0 40.720 0.688 Vet = 7.69 0.0 760.97 15.900 K Factor = 190.84 15 54.43 2.635 0.0 9.250 15.115 KFactor= 14.00 to 120 0.0 0.0 0.0 16 54.43 0.0093 0.0 9.250 0.086 Vet = 3.20 16 54.58 2.635 2T 32.948 22.250 15.201 K Factor = 14.00 to 120 0.0 32.948 1.949 17 109.01 0.0338 0.0 55.198 1.866 Vel = 6.41 17 0.0 6.357 0.0 9.080 19.016 to 120 0.0 0.0 0.0 18 109.01 0.0004 0.0 9.080 0.004 Vet = 1.10 18 109.29 6.357 0.0 4.370 19.020 to 120 0.0 0.0 0.0 7 218.3 0.0016 0.0 4.370 0.007 Vet = 2.21 0.0 218.30 19.027 KFactor= 50.05 10 57.75 2.635 0.0 9.250 17.014 KFactor= 14.00 to 120 0.0 0.0 0.0 11 57.75 0.0105 0.0 9.250 0.097 Vet = 3.40 11 57.91 2.635 2T 32.948 21.420 17.111 K Factor = 14.00 to 120 0.0 32.948 1.589 12 115.66 0.0377 0.0 54.368 2.050 Vet = 6.80 12 0.0 6.357 0.0 9.080 20.750 to 120 0.0 0.0 0.0 13 115.66 0.0006 0.0 9.080 0.005 Vet= 1.17 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 10 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 13 115.37 6.357 0.0 9.080 20.755 to 120 0.0 0.0 0.0 14 231.03 0.0018 0.0 9.080 0.016 Vel = 2.34 14 115.14 6.357 1 37.72 1.700 20.771 to 120 0.0 37.720 0.0 8 346.17 0.0039 0.0 39.420 0.155 Vel = 3.50 0.0 346.17 20.926 K Factor= 75.67 1 42.16 2.635 0.0 9.080 9.067 K Factor = 14.00 to 120 0.0 0.0 0.0 2 42.16 0.0058 0.0 9.080 0.053 Vel = 2.48 2 42.27 2.635 0.0 8.830 9.120 K Factor = 14.00 to 120 0.0 0.0 0.0 3 84.43 0.0211 0.0 8.830 0.186 Vel= 4.97 3 42.71 2.635 1 16.474 8.700 9.306 K Factor = 14.00 to 120 0.0 16.474 0.0 4 127.14 0.0449 0.0 25.174 1.130 VeI= 7.48 4 129.23 2.635 IT 16.474 4.330 10.436 to 120 0.0 16.474 1.875 5 256.37 0.1644 0.0 20.804 3.421 Vel= 15.08 5 82.60 6.357 1 37.72 6.750 15.732 to 120 0.0 37.720 0.0 6 338.97 0.0038 0.0 44.470 0.168 Vel = 3.43 6 760.97 6.357 1 37.72 56.000 15.900 to 120 0.0 37.720 0.0 7 1099.94 0.0334 0.0 93.720 3.127 Vel= 11.12 7 218.30 6.357 1 37.72 3.000 19.027 to 120 0.0 37.720 0.0 8 1318.24 0.0466 0.0 40.720 1.899 Vel = 13.33 8 346.17 6.357 1 17.603 56.700 20.926 to 120 2T 75.44 93.043 0.0 TRM 1664.41 0.0718 0.0 149.743 10.752 Vel = 16.82 TRM 0.0 8.249 1 21.141 23.000 31.678 to 120 2E 42.282 63.423 9.961 BRM 1664.41 0.0202 0.0 86.423 1.745 Vel = 9.99 BRM 0.0 8.249 IL 15.269 10.000 43.384 to 120 0.0 15.269 2.166 MI 1664.41 0.0202 0.0 25.269 0.510 Vel = 9.99 Mi 0.0 7.98 2E 54.365 79.000 46.060 to 150 1 13.591 67.957 0.0 M2 1664.41 0.0157 0.0 146.957 2.308 Vel = 10.68 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page II TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. Cu or Ftng's Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn M2 0.0 8.27 2E 56.936 16.000 48.368 to 140 1 55.354 112.290 4.500 *Fixed loss ...45 M3 1664.41 0.0150 0.0 128.290 1.923 Vel = 9.94 M3 0.0 7.98 1G 6.041 93.000 54.791 to 150 IT 52.855 58.895 0.0 K 1664.41 0.0157 0.0 151.895 2.385 Vel = 10.68 0.0 1664.41 57.176 K Factor = 220.12 A -74.80 7.98 2F 27.183 352.000 60.543 to 150 1 6.041 33.222 0.0 B -74.8 0.0 0.0 385.222 -0.019 Vel = 0.48 B 0.0 7.98 1E 27.183 405.000 60.524 to 150 1G 6.041 86.077 0.0 C -74.8 -0.0001 IT 52.855 491.077 -0.025 Vel = 0.48 C 618.28 7.98 2F 27.183 180.000 60.499 to 150 2T 105.71 157.054 0.0 D 543.48 0.0020 4G 24.162 337.054 0.667 Vel = 3.49 D 0.0 11.65 8G 64.398 719.000 61.166 to 150 iT 80.498 144.896 0.0 E 543.48 0.0003 0.0 863.896 0.271 VeI= 1.64 E 0.0 11.65 4G 32.199 379.000 61.437 to 150 0.0 32.200 -0.866 TEST 543.48 0.0003 0.0 411.200 0.129 Vel = 1.64 0.0 543.48 60.700 K Factor= 69.76 C -618.28 7.98 4G 24.162 387.000 60.499 to 150 IF 13.591 37.754 0.0 M -618.28 -0.0025 0.0 424.754 -1.068 Vel = 3.97 M 1092.64 7.98 2G 12.081 220.000 59.431 to 150 0.0 12.082 0.0 N 474.36 0.0015 0.0 232.082 0.358 Vel = 3.04 N 213.08 7.98 2F 27.183 281.000 59.789 to 150 4G 24.162 104.199 0.0 Q 687.44 0.0031 iT 52.855 385.199 1.178 VeI= 4.41 Q 0.0 11.65 4G 32.199 438.000 60.967 to 150 iT 80.498 130.139 0.0 R 687.44 0.0005 iF 17.441 568.139 0.275 Vel = 2.07 R 0.0 11.65 4G 32.199 620.000 61.242 to 150 1F 17.441 49.641 -0.866 TEST 687.44 0.0005 0.0 669.641 0.324 Vel = 2.07 0.0 687.44 60.700 K Factor= 88.23 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 12 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Filling Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn F -1071.76 7.98 IG 6.041 107.000 59.412 to 150 1 52.855 72.487 0.0 G -1071.76 -0.0070 1 13.591 179.487 -1.248 Vel = 6.88 G 0.0 7.98 0.0 7.000 58.164 to 150 0.0 0.0 0.0 H -1071.76 -0.0070 0.0 7.000 -0.049 Vel = 6.88 H 0.0 7.98 0.0 42.000 58.115 to 150 0.0 0.0 0.0 J -1071.76 -0.0070 0.0 42.000 -0.292 Vel = 6.88 J 0.0 7.98 0.0 93.000 57.823 to 150 0.0 0.0 0.0 K -1071.76 -0.0070 0.0 93.000 -0.647 Vel = 6.88 K 2164.41 7.98 0.0 54.000 57.176 Qa= 500 to 150 0.0 0.0 0.0 L 1092.65 0.0072 0.0 54.000 0.389 Vel = 7.01 L 0.0 7.98 IG 6.041 200.000 57.565 to 150 iT 52.855 58.895 0.0 M 1092.65 0.0072 0.0 258.895 1.866 VeI= 7.01 0.0 1092.65 59.431 K Factor = 141.73 N -213.08 7.98 IF 13.591 64.000 59.789 to 150 1G 6.041 72.487 0.0 P -213.08 -0.0004 1 52.855 136.487 -0.048 Vel= 1.37 P 0.0 7.98 5F 67.957 812.000 59.741 to 150 1 6.041 126.852 0.0 F -213.08 -0.0004 IT 52.855 938.852 -0.329 Vel = 1.37 F 1071.76 7.98 2F 27.183 153.000 59.412 to 150 2G 12.081 92.119 0.0 A 858.68 0.0046 IT 52.855 245.119 1.131 VeI= 5.51 A 74.80 7.98 2G 12.081 125.000 60.543 to 150 IT 52.855 64.937 -0.866 TEST 933.48 0.0054 0.0 189.937 1.023 Vel = 5.99 0.0 933.48 60.700 K Factor = 119.81 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 F.W.Le..9 APPROVED #SflU BITTED CARLSBAb RTMENT A Sôci- - - Fire Protection by Computer Design INDUSTRIAL FIRE SPRINKLER CO. 3845 IMPERIAL AVE. SAN DIEGO, CA 92113 619-266-6030 Job Name : TOWERS AT BRESSI Building : BUILDING M Location : 6144 INNOVATION WAY System : REMOTE AREA2 Contract Data File Towers-M2.wxl Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 INDUSTRIAL FIRE SPRINKLER Co. Page 1 TOWERS AT BRESSI Date 5/2/07 Hydraulic Design Information Sheet Name - TOWERS AT BRESSI Date - 5/2/07 Location - 6144 INNOVATION WAY Building - BUILDING M System No. - REMOTE AREA2 Contractor - INDUSTRIAL FIRE SPRINKELR CO. Contract No. - Calculated By - M.G. Drawing No. - FP-4 Construction: (X) Combustible ( ) Non-Combustible Ceiling Height - 9-2" Occupancy - LIGHT S (X) NFPA 13 (X) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz. Y NFPA 231 ( ) NFPA 231C Figure Curve S Other T Specific Ruling Made By Date E M Area of Sprinkler Operation - 900 System Type Sprinkler/Nozzle Density - .10 (X) Wet Make GLOBE D Area Per Sprinkler - 195 MAX Dry Model GL E Elevation at Highest Outlet - 91 -2" Deluge Size 1/2" S Hose Allowance - Inside - Preaction K-Factor 5.6 I Rack Sprinkler Allowance - Other Temp . Rat . 155 G Hose Allowance - Outside - 100 N Note Calculation Flow Required - Press Required - Summary C-Factor Used: 120 Overhead 150 Underground W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - 1/31/07 Cap. - T Time of Test - Rated Cap.- Elev.- E Static Press - 75 8 Press - R Residual Press - 74 Elev. - Well Flow - 1780 Proof Flow S Elevation - 385.0 U P Location - GATEWAY RD & INNOVATION WAY P L Source of Information - PERFORMED BY I.F.S., WITNESSED BY CARLSBAD WATER DIST Y C Commodity Class Location 0 Storage Ht. Area Aisle W. M Storage Method: Solid Piled % Palletized % Rack M Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Encap. SR Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non TA Mult. Row ( ) Open Shelf O C R K Flue Spacing Clearance:Storage to Ceiling A Longitudinal Transverse G E Horizontal Barriers Provided: Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Water Supply Curve (C) INDUSTRIAL FIRE SPRINKLER CO. Page 2 TOWERS AT BRESSI Date 5/2/07 City Water Supply: Demand: Cl - Static Pressure : 75 Dl - Elevation : 4.838 C2 - Residual Pressure: 74 D2 - System Flow : 182.361 stem Pressure : 39.279 C2 - Residual Flow : 1780 D2 - SrDemand Hose Adj City) Hose ) D3 - System Demand : 282.361 Safety Margin : 35.688 150 140 130 p120 R° E10° S90 80 U70 R60 E5° D - ei- 40 30 20 . .1 I I 10 I I I I 200 400 600 800 1000 1200 1400 1600 1800 FLOW ( N ' 1.85) Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Fittings Used Summary INDUSTRIAL FIRE SPRINKLER CO. Page 3 TOWERS AT BRESSI Date 5/2/07 Fitting Legend Abbrev. Name E 90 Standard Elbow F 45' Elbow G Generic Gate Valve L Long Turn Elbow T 90' Flow Thru Tee Z Generic Flow Switch 1/2 % 1 1% 11/2 -------------------------------- 2 2½ 3 31/2 4 5 6 8 10 12 14 16 18 20 24 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 1 1 1 1 2 2 3 3 3 4 5 7 9 11 13 17 19 21 24 28 1 1 1 1 1 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 1 1 2 2 2 3 4 5 5 6 8 9 13 16 18 24 27 30 34 40 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Pressure / Flow Summary - STANDARD INDUSTRIAL FIRE SPRINKLER CO. Page 4 -TOWERS AT BRESSI Date 5/2/07 Node No. Elevation K-Fact Pt Actual Pn Flow Actual Density Area Press Req. D001 9.17 5.6 14.0 na 20.95 0.1 180 7.0 D002 9.17 5.6 10.33 na 18.0 0.1 180 7.0 D003 9.17 5.6 10.54 na 18.18 0.1 96 7.0 D004 9.17 5.6 10.26 na 17.94 0.1 80 7.0 D005 9.17 5.6 14.4 na 21.25 0.1 153 7.0 D006 9.17 5.6 11.65 na 19.11 0.1 145 7.0 D007 9.17 5.6 15.83 na 22.28 0.1 148 7.0 D008 9.17 5.6 16.17 na 22.52 0.1 195 7.0 D009 9.17 5.6 15.61 na 22.12 0.1 120 7.0 121 9.67 10.59 na 120 9.67 16.02 na 117 9.67 10.38 na 118 10.0 11.08 na 119 10.0 11.3 na 116 9.67 11.73 na 115 9.67 14.55 na 113 9.67 16.36 na 114 10.0 17.49 na 110 9.67 15.78 na 111 10.0 16.87 na 112 10.0 17.12 na 106 9.67 10.31 na 107 10.0 11.02 na 108 10.0 11.37 na 109 10.0 12.52 na 101 9.67 14.13 na 102 10.0 15.1 na 103 10.0 15.55 na 104 10.0 17.92 na 105 10.0 18.33 na 125 10.0 21.24 na 126 24.0 21.28 na 29 24.0 21.3 na 30 24.0 21.37 na 5 24.0 21.37 na 6 24.0 21.43 na 7 24.0 21.54 na 8 24.0 21.59 na TRM 24.0 21.77 na BRM 1.0 31.76 na Ml -4.0 33.93 na M2 -4.0 33.97 na M3 -4.0 40.0 na A -4.0 40.12 na B -4.0 40.12 na C -4.0 40.12 na D -4.0 40.14 na E -4.0 40.14 na TEST -2.0 39.28 na M -4.0 40.1 na N -4.0 40.1 na Q -4.0 40.13 na R -4.0 40.14 na F -4.0 40.1 na G -4.0 40.07 na H -4.0 40.07 na J -4.0 40.06 na Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Flow Summary - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 5 TOWERS AT BRESSI Date 5/2/07 Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Req. K -4.0 40.04 na 100.0 L -4.0 40.05 na P -4.0 40.1 na The maximum velocity is 16.01 and it occurs in the pipe between nodes 105 and 125 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams INDUSTRIAL FIRE SPRINKLER CO. Page 6 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Fe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 0001 20.95 1.049 IE 2.0 0.500 13.997 K Factor= 5.60 to 120 0.0 2.000 -0.217 101 20.95 0.1420 0.0 2.500 0.355 Vel = 7.78 0.0 20.95 14.135 K Factor = 5.57 0002 18.00 1.049 1E 2.0 0.500 10.332 K Factor = 5.60 to 120 0.0 2.000 -0.217 117 18.0 0.1072 0.0 2.500 0.268 Vel= 6.68 0.0 18.00 10.383 KFactor= 5.59 D003 18.18 1.049 1 2.0 0.500 10.537 K Factor = 5.60 to 120 0.0 2.000 -0.217 121 18.18 0.1092 0.0 2.500 0.273 Vel = 6.75 0.0 18.18 10.593 K Factor = 5.59 D004 17.94 1.049 1E 2.0 0.500 10.263 K Factor = 5.60 to 120 0.0 2.000 -0.217 106 17.94 0.1068 0.0 2.500 0.267 Vel= 6.66 0.0 17.94 10.313 KFactor= 5.59 0005 21.25 1.049 1E 2.0 0.500 14.405 K Factor= 5.60 to 120 0.0 2.000 -0.217 115 21.25 0.1456 0.0 2.500 0.364 Vel= 7.89 0.0 21.25 14.552 K Factor = 5.57 D006 19.11 1.049 1E 2.0 0.500 11.646 K Factor = 5.60 to 120 0.0 2.000 -0.217 116 19.11 0.1196 0.0 2.500 0.299 VeI= 7.09 0.0 19.11 11.728 K Factor = 5.58 D007 22.28 1.049 1 E 2.0 0.500 15.834 K Factor = 5.60 to 120 0.0 2.000 -0.217 120 22.28 0.1592 0.0 2.500 0.398 Vel = 8.27 0.0 22.28 16.015 K Factor = 5.57 D008 22.52 1.049 1 2.0 0.500 16.172 K Factor = 5.60 to 120 0.0 2.000 -0.217 113 22.52 0.1624 0.0 2.500 0.406 Vel= 8.36 0.0 22.52 16.361 KFactor= 5.57 0009 22.12 1.049 1E 2.0 0.500 15.608 K Factor = 5.60 to 120 0.0 2.000 -0.217 110 22.12 0.1572 0.0 2.500 0.393 Vel= 8.21 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 7 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Filling Pipe Pt Pt Ref. 1Cu or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 0.0 22.12 15.784 K Factor = 5.57 121 18.18 1.049 1E 2.0 0.830 10.593 to 120 1 5.0 7.000 -0.143 119 18.18 0.1091 0.0 7.830 0.854 Vel = 6.75 0.0 - 18.18 11.304 KFactor= 5.41 120 22.28 1.049 1E 2.0 0.830 16.015 to 120 IT 5.0 7.000 -0.143 112 22.28 0.1590 0.0 7.830 1.245 Vel = 8.27 0.0 22.28 17.117 K Factor = 5.39 117 18.00 1.049 1E 2.0 0.830 10.383 to 120 1 5.0 7.000 -0.143 118 18.0 0.1070 0.0 7.830 0.838 Vel = 6.68 118 0.0 1.38 0.0 8.000 11.078 to 120 0.0 0.0 0.0 119 18.0 0.0282 0.0 8.000 0.226 Vel = 3.86 119 18.18 1.38 0.0 0.660 11.304 to 120 0.0 0.0 0.0 108 36.18 0.1015 0.0 0.660 0.067 Vel = 7.76 0.0 36.18 11.371 KFactor= 10.73 116 19.11 1.049 1 2.0 0.830 11.728 to 120 1 5.0 7.000 -0.143 109 19.11 0.1197 0.0 7.830 0.937 Vel = 7.09 0.0 19.11 12.522 KFactor= 5.40 115 21.25 1.049 1 2.0 0.830 14.552 to 120 IT 5.0 7.000 -0.143 103 21.25 0.1457 0.0 7.830 1.141 Vel= 7.89 0.0 21.25 15.550 K Factor = 5.39 113 22.52 1.049 1E 2.0 0.830 16.361 to 120 1 5.0 7.000 -0.143 114 22.52 0.1621 0.0 7.830 1.269 VeI= 8.36 114 0.0 1.38 IT 6.0 4.080 17.487 to 120 0.0 6.000 0.0 104 22.52 0.0427 0.0 10.080 0.430 VeI= 4.83 0.0 22.52 17.917 K Factor = 5.32 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 8 TOWERS AT BRESSI Date, 5/2/07 Hyd. Qa Dia. Filling Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 110 22.12 1.049 IE 2.0 0.830 15.784 to 120 iT 5.0 7.000 -0.143 111 22.12 0.1568 0.0 7.830 1.228 Vel= 8.21 111 0.0 1.38 0.0 6.000 16.869 to 120 0.0 0.0 0.0 112 22.12 0.0413 0.0 6.000 0.248 Vet = 4.74 112 22.29 1.38 iT 6.0 2.080 17.117 to 120 0.0 6.000 0.0 105 44.41 0.1496 0.0 8.080 1.209 Vet = 9.53 0.0 44.41 18.326 KFactor= 10.37 106 17.94 1.049 1E 2.0 1.000 10.313 to 120 iT 5.0 7.000 -0.143 107 17.94 0.1064 0.0 8.000 0.851 Vet = 6.66 107 0.0 1.38 iT 6.0 6.500 11.021 to 120 0.0 6.000 0.0 108 17.94 0.0280 0.0 12.500 0.350 Vet = 3.85 108 36.18 1.38 0.0 5.330 11.371 to 120 0.0 0.0 0.0 109 54.12 0.2159 0.0 5.330 1.151 Vel= 11.61 109 19.11 1.38 IT 6.0 9.370 12.522 to 120 0.0 6.000 0.0 105 73.23 0.3776 0.0 15.370 5.804 Vet = 15.71 0.0 73.23 18.326 KFactor= 17.11 101 20.95 1.049 1E 2.0 0.830 14.135 to 120 iT 5.0 7.000 -0.143 102 20.95 0.1418 0.0 7.830 1.110 Vet = 7.78 102 0.0 1.38 0.0 12.000 15.102 to 120 0.0 0.0 0.0 103 20.95 0.0373 0.0 12.000 0.448 Vet= 4.49 103 21.25 1.38 iT 6.0 11.370 15.550 to 120 0.0 6.000 0.0 104 42.2 0.1363 0.0 17.370 2.367 Vet = 9.05 104 22.53 2.157 0.0 12.000 17.917 to 120 0.0 0.0 0.0 105 64.73 0.0341 0.0 12.000 0.409 Vet = 5.68 105 117.63 2.157 1E 6.153 6.410 18.326 to 120 0.0 6.153 0.0 125 182.36 0.2320 0.0 12.563 2.915 Vet = 16.01 125 0.0 2.157 iT 12.307 14.000 21.241 to 120 0.0 12.307 -6.063 126 182.36 0.2320 0.0 26.307 6.104 Vel= 16.01 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 9 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Filling Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 126 0.0 4.26 0.0 2.330 21.282 to 120 0.0 0.0 0.0 29 182.36 0.0082 0.0 2.330 0.019 Vel= 4.10 29 0.0 4.26 0.0 8.500 21.301 to 120 0.0 0.0 0.0 30 182.36 0.0085 0.0 8.500 0.072 Vel = 4.10 30 0.0 6.357 0.0 1.000 21.373 to 120 0.0 0.0 0.0 5 182.36 0.0010 0.0 1.000 0.001 Vel = 1.84 5 0.0 6.357 IT 37.72 6.750 21.374 to 120 0.0 37.720 0.0 6 182.36 0.0012 0.0 44.470 0.054 Vel= 1.84 6 0.0 6.357 1 37.72 56.000 21.428 to 120 0.0 37.720 0.0 7 182.36 0.0012 0.0 93.720 0.112 Vel= 1.84 7 0.0 6.357 IT 37.72 3.000 21.540 to 120 0.0 37.720 0.0 8 182.36 0.0012 0.0 40.720 0.049 Vel= 1.84 8 0.0 6.357 1 17.603 56.700 21.589 to 120 2T 75.44 93.043 0.0 TRM 182.36 0.0012 0.0 149.743 0.180 Vel = 1.84 TRM 0.0 8.249 1Z 21.141 23.000 21.769 to 120 2E 42.282 63.423 9.961 BRM 182.36 0.0003 0.0 86.423 0.029 Vel = 1.09 BRM 0.0 8.249 1L 15.269 10.000 31.759 to 120 0.0 15.269 2.166 MI 182.36 0.0003 0.0 25.269 0.008 Vel = 1.09 Ml 0.0 7.98 2E 54.365 79.000 33.933 to 150 1 13.591 67.957 0.0 M2 182.36 0.0003 0.0 146.957 0.039 Vel = 1.17 M2 0.0 8.27 2E 56.936 16.000 33.972 to 140 1T 55.354 112.290 6.000 *Fixed loss _.6 M3 182.36 0.0002 0.0 128.290 0.032 VeI= 1.09 M3 0.0 7.98 1G 6.041 93.000 40.004 to 150 iT 52.855 58.895 0.0 K 182.36 0.0003 0.0 151.895 0.040 Vel= 1.17 0.0 182.36 40.044 KFactor= 28.82 A -9.76 7.98 2F 27.183 352.000 40.122 to 150 1G 6.041 33.222 0.0 B -9.76 0.0 0.0 385.222 -0.001 Vel = 0.06 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 10 -TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn B 0.0 7.98 1E 27.183 405.000 40.121 to 150 1G 6.041 86.077 0.0 C -9.76 0.0 IT. 52.855 491.077 0.0 Vel = 0.06 C 80.66 7.98 2F 27.183 180.000 40.121 to 150 2T 105.71 157.054 0.0 D 70.9 0.0 4G 24.162 337.054 0.015 Vel = 0.45 D 0.0 11.65 8G 64.398 719.000 40.136 to 150 IT 80.498 144.896 0.0 E 70.9 0.0 0.0 863.896 0.006 Vel = 0.21 E 0.0 11.65 4G 32.199 379.000 40.142 to 150 0.0 32.200 -0.866 TEST 70.9 0.0 0.0 411.200 0.003 Vel = 0.21 0.0 70.90 39.279 K Factor= 11.31 C -80.66 7.98 4G 24.162 387.000 40.121 to 150 1 13.591 37.754 0.0 M -80.66 -0.0001 0.0 424.754 -0.025 Vel = 0.52 M 142.54 7.98 2G 12.081 220.000 40.096 to 150 0.0 12.082 0.0 N 61.88 0.0 0.0 232.082 0.008 Vel = 0.40 N 27.80 7.98 2F 27.183 281.000 40.104 to 150 4G 24.162 104.199 0.0 Q 89.68 0.0001 1 52.855 385.199 0.028 Vel = 0.58 Q 0.0 11.65 4G 32.199 438.000 40.132 to 150 iT 80.498 130.139 0.0 R 89.68 0.0 1 17.441 568.139 0.006 Vel = 0.27 R 0.0 11.65 4G 32.199 620.000 40.138 to 150 1 17.441 49.641 -0.866 TEST 89.68 0.0 0.0 669.641 0.007 Vel = 0.27 0.0 89.68 39.279 K Factor= 14.31 F -139.82 7.98 iG 6.041 107.000 40.096 to 150 iT 52.855 72.487 0.0 G -139.82 -0.0002 1 13.591 179.487 -0.029 Vel = 0.90 G 0.0 7.98 0.0 7.000 40.067 to 150 0.0 0.0 0.0 H -139.82 -0.0001 0.0 7.000 -0.001 Vel = 0.90 H 0.0 7.98 0.0 42.000 40.066 to 150 0.0 0.0 0.0 J -139.82 -0.0002 0.0 42.000 -0.007 Vel = 0.90 J 0.0 7.98 0.0 93.000 40.059 to 150 0.0 0.0 0.0 K -139.82 -0.0002 0.0 93.000 -0.015 Vel = 0.90 Computer Programs by Hydratecinc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard INDUSTRIAL FIRE SPRINKLER CO. Page 11 TOWERS AT BRESSI Date 5/2/07 Hyd. Qa Dia. Filling Pipe Pt Pt Ref. "CI' or Ftng's Fe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn K 282.36 7.98 0.0 54.000 40.044 Qa= 100 to 150 0.0 0.0 0.0 L 142.54 0.0002 0.0 54.000 0.009 Vel = 0.91 L 0.0 7.98 IG 6.041 200.000 40.053 to 150 IT 52.855 58.895 0.0 M 142.54 0.0002 0.0 258.895 0.043 Vel = 0.91 0.0 142.54 40.096 KFactor= 22.51 N -27.80 7.98 IF 13.591 64.000 40.104 to 150 IG 6.041 72.487 0.0 P -27.8 0.0 IT 52.855 136.487 -0.001 Vel = 0.18 P 0.0 7:98 SF 67.957 812.000 40.103 to 150 IG 6.041 126.852 0.0 F -27.8 0.0 IT 52.855 938.852 -0.007 Vel = 0.18 F 139.82 7.98 2F 27.183 153.000 40.096 to 150 2G 12.081 92.119 0.0 A 112.02 0.0001 IT 52.855 245.119 0.026 Vel= 0.72 A 9.76 7.98 2G 12.081 125.000 40.122 to 150 IT 52.855 64.937 -0.866 TEST 121.78 0.0001 0.0 189.937 0.023 Vel = 0.78 0.0 121.78 39.279 KFactor= 19.43 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087