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6186 INNOVATION WAY; BLDG P; AS070157; Permit
9114/22, 11:12 AM AS070157 Permit Data City of Carlsbad Sprinkler Permit 6186 INNOVATION Job Address: WY Permit Type: SPRINK Parcel No: 2132621000 Lot #: 0 Reference No.: Permit No: AS070157 Status: ISSUED Applied 6/7/2007 Approved: 6/7/2007 Issued: 6/7/2007 PC #: Inspector: Project Title: TOWERS @ BRESSI, BLDG. P 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'l Fees ($) Total ($) Balance ($) 186 0 , 186 0 about:blank 1/1 05-10-07 10:00am From-Industrial Fire Sprinkler 619 266 6035 T-026 P001/001 F-514 r -.----------- fr5o7/57 CARLSBAD FM PREVENTION DIVISION Permit Application Form A Check or fill-in pertinent information for type of permit you are submitting. AS —Automatic SprüMlers (Check offe ofpläns being subni&t4 X New System - How manyevels? (evn) - Tenant Improvement Residential - How many systems and/or buildings?_____ Underground for approval - Underground included for reference oniy Total Fees______ FA - Fire Alarm 25 Devices or less______ Over 26 devices # of devices____ Monitoring System Total Fees_____ FS - Fired Systems (Circle One) Hood & Dnct Special Chemical Agent Suppression System Standpipe, Spryooth -. Total Pee Repeated Inspection Inspection fee Is $73.00. B Nam ofPr ieTowe cth j3a~§i Y)6) Ctc) -A*C,Y) C. Address ofjob site: )2 (bJ) (o 'I 1'44 L%' 4'I q~ Suite 11 cw WAY • P Building PeTmit # GB 4'tXa, 32c6 1) Con f b7S Contractor .. ormatiort Name Mduria/ p: prirCo-/i _- Address • ;f34E; /iprkJ Ave, cny, state, zip. 9a1 Diy CA 92/f Phone b/g74fple2939.••. FAX W r-&03S • Kind of License and uinber Pp. iQ Do you cuncntly have a business license on file with the City of Carlsbad? or 4 A. & S*nu ture istc J7 Please esiimnte at least 141 busIns days For plan review comnients and/or approvaL We will contact you by telephone when the plans are approvedfdisapproved. Thank you! 1 PIaY elfVyd Par6/ey CD17,su - From: Ken Wagoner To: James Weigand Date: 6/1/2007 Time: 3:00:32 PM Page 2 of 2 C Towers at Bressi Ranch Review Comments. Page 2 Review Comments Towers at Bressi Ranch, 6186 Innovation Way, Carlsbad, CA Sheet 2 comments No core required note at columns D & E for 6" main. End branch line segments in extra hazard areas are not sized. Calculation suggests 2" Verify slope of roof in all areas is not greater than 2:12, or systems must be modified. i. Note that storage protection methods in NFPA- 13 are all based on roof slopes which do not exceed 2:12. 2. Sheet 3 comments Per NFPA- 13, branch lines larger than 21/2" are required to be provided with lateral sway bracing, see section 6-4.5.3 (1999 edition). Note ic above applies 3. Sheet 4 comments a. Note ic above applies 4. Sheet 5 comments a. Note I above applies Sheet 6, 7 & 8 comments End branch line segments in extra hazard areas are not sized. Calculation suggests 2" Verify slope of roof in all areas is not greater than 2:12, or systems must be modified. i. Note that storage protection methods in NFPA- 13 are all based on roof slopes which do not exceed 2:12. Per NFPA-13, branch lines larger than 2'/2" are required to be provided with lateral sway bracing, see section 6-4.5.3 (1999 edition). 6. Sheet 9 comments Side beam bracket hanger detail is in error, maximum pipe size for hangers using 2/a" rod is 4", per NFPA-13. Inspector's test outlet size is to match smallest orifice used in building. Smallest outlet used in each building in this submittal is 1/2" APPROVED #1VU BIIHTTED /.4 xa&&' AjIUIIIIIItIlL CARLSBAD TMENT - - - 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 P Location : 6186 INNOVATION WAY System : REMOTE AREA1 Contract Data File Towers-P1.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 - 6186 INNOVATION WAY Building - BUILDING P System No. - REMOTE AREA1 Contractor - INDUSTRIAL FIRE SPRINKELR CO. Contract No. - Calculated By - M.G. Drawing No. - FP-7 Construction: (X) Combustible ( ) Non-Combustible Ceiling Height - VARIES Occupancy - EXTRA S (X) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 (X) Ex.Haz. Y ( ) NFPA 231 ( ) NFPA 231C ( ) Figure Curve S Other T Specific Ruling Made By Date E M Area of Sprinkler Operation - 3000 System Type Sprinkler/Nozzle Density - .45 (X) Wet Make RELIABLE D Area Per Sprinkler - 94.2 ( ) Dry Model G VELO E Elevation at Highest Outlet - 28'-9" ( ) Deluge Size 3/4" S Hose Allowance - Inside - ( ) Preaction K-Factor 14.0 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.286 G Hose Allowance - Outside - 500 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. N Storage Method: Solid Piled % Palletized % Rack N SR TA O C R K A G E Single Row Double Row Mult. Row Flue Spacing Longitudinal Conven. Pallet ( ) Auto. Storage Encap. Slave Pallet ( ) Solid Shelf Non Open Shelf Clearance:Storage to Ceiling Transverse 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: CI - Static Pressure : 75 Dl - Elevation : 15.808 C2 - Residual Pressure: 74 D2 - System Flow : 1744.98 stem Pressure : 61.894 02- Residual Flow : 1780 D2 - SrDemand) Hose Adj City ________Hose : 500 D3 - System Demand : 2244.98 Safety Margin : 11.570 150 140 130 P 120 R110 E 100 S90 80 U7° D2 R6° - D3 E 50 40 30 20 : 10 • a.I I I I 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 ½ % 1 1% 11/2 2 21/2 3 31/2 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 ThruTee 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 / 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. 51 28.5 14 10.76 na 45.92 0.45 94.2 7.0 50 28.5 14 10.02 na 44.32 0.45 94.2 7.0 47 28.5 14 9.85 na 43.93 0.45 94.2 7.0 48 28.5 12.92 na 49 28.5 14.09 na 44 28.75 14 13.56 na 51.56 0.45 94.2 7.0 45 28.75 14 13.66 na 51.75 0.45 94.2 7.0 46 28.75 14 14.0 na 52.38 0.45 94.2 7.0 41 28.5 14 13.81 na 52.02 0.45 94.2 7.0 42 28.5 14 13.91 na 52.21 0.45 94.2 7.0 43 28.5 14 14.25 na 52.85 0.45 94.2 7.0 38 28.33 14 14.08 na 52.54 0.45 94.2 7.0 39 28.33 14 14.18 na 52.73 0.45 94.2 7.0 40 28.33 14 14.54 na 53.38 0.45 94.2 7.0 35 28.08 14 14.52 na 53.34 0.45 94.2 7.0 36 28.08 14 14.62 na 53.53 0.45 94.2 7.0 37 28.08 14 14.98 na 54.19 0.45 94.2 7.0 32 28.75 14 13.54 na 51.52 0.45 94.2 7.0 33 28.75 14 13.64 na 51.7 0.45 94.2 7.0 34 28.75 14 13.98 na 52.34 0.45 94.2 7.0 27 28.5 14 9.17 na 42.39 0.45 94.2 7.0 28 28.5 12.04 na 29 28.5 13.14 na 30 28.5 16.37 na 31 24.0 22.22 na 5A 24.0 22.28 na 23 28.75 14 13.3 na 51.06 0.45 94.2 7.0 24 28.75 14 13.4 na 51.24 0.45 94.2 7.0 25 28.75 14 13.73 na 51.87 0.45 94.2 7.0 26 28.75 15.3 na 19 28.5 14 13.54 na 51.51 0.45 94.2 7.0 20 28.5 14 13.64 na 51.7 0.45 94.2 7.0 21 28.5 14 13.97 na 52.33 0.45 94.2 7.0 22 28.5 15.57 na 15 28.33 14 13.81 na 52.03 0.45 94.2 7.0 16 28.33 14 13.91 na 52.21 0.45 94.2 7.0 17 28.33 14 14.25 na 52.86 0.45 94.2 7.0 18 28.33 15.88 na 11 28.08 14 14.24 na 52.83 0.45 94.2 7.0 12 28.08 14 14.34 na 53.01 0.45 94.2 7.0 13 28.08 14 14.69 na 53.66 0.45 94.2 7.0 14 28.08 16.37 na 1 28.75 14 13.28 na 51.02 0.45 94.2 7.0 2 28.75 14 13.37 na 51.2 0.45 94.2 7.0 3 28.75 14 13.71 na 51.83 0.45 94.2 7.0 4 28.75 15.28 na 5 24.0 22.28 na 6 24.0 22.34 na 7 24.0 22.5 na 8 24.0 22.79 na 9 24.0 23.24 na 10 24.0 26.0 na 228 24.0 27.68 na TRP 24.0 29.15 na BRP 0.5 41.21 na P1 -4.0 43.72 na P2 -4.0 46.47 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. P3 -4.0 53.07 na A -4.0 59.26 na B -4.0 59.24 na C -4.0 59.21 na D -4.0 59.8 na E -4.0 60.05 na TEST -8.0 61.89 na M -4.0 58.22 na N -4.0 57.46 na Q -4.0 59.25 na R -4.0 59.67 na F -4.0 58.29 na G -4.0 58.27 na H -4.0 58.27 na J -4.0 58.26 na K -4.0 58.25 na L -4.0 58.25 na P -4.0 55.53 na 500.0 The maximum velocity is 18.86 and it occurs in the pipe between nodes 14 and 9 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 Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 51 45.92 1.049 IT 5.0 0.500 10.760 K Factor = 14.00 to 120 0.0 5.000 0.0 49 45.92 0.6056 0.0 5.500 3.331 Vel = 17.05 0.0 45.92 14.091 KFactor= 12.23 50 44.32 1.049 IT 5.0 0.500 10.021 K Factor = 14.00 to 120 0.0 5.000 0.0 29 44.32 0.5671 0.0 5.500 3.119 Vel = 16.45 0.0 44.32 13.140 KFactor= 12.23 47 43.93 1.049 IT 5.0 0.500 9.847 KFactor= 14.00 to 120 0.0 5.000 0.0 48 43.93 0.5580 0.0 5.500 3.069 Vel = 16.31 48 0.0 1.38 0.0 8.000 12.916 to 120 0.0 0.0 0.0 49 43.93 0.1469 0.0 8.000 1.175 Vel= 9.42 49 45.93 1.61 1 8.0 0.750 14.091 to 120 0.0 8.000 0.0 30 89.86 0.2602 0.0 8.750 2.277 Vel = 14.16 0.0 89.86 16.368 KFactor= 22.21 44 51.56 2.635 0.0 11.410 13.565 K Factor = 14.00 to 120 0.0 0.0 0.0 45 51.56 0.0085 0.0 11.410 0.097 Vel = 3.03 45 51.75 2.635 0.0 11.080 13.662 K Factor = 14.00 to 120 0.0 0.0 0.0 46 103.31 0.0305 0.0 11.080 0.338 VeI= 6.08 46 52.38 2.635 IT 16.474 3.450 14.000 KFactor= 14.00 to 120 0.0 16.474 0.0 26 155.69 0.0653 0.0 19.924 1.302 VeI= 9.16 0.0 155.69 15.302 KFactor= 39.80 41 52.02 2.635 0.0 11.410 13.807 KFactor= 14.00 to 120 0.0 0.0 0.0 42 52.02 0.0086 0.0 11.410 0.098 Vel = 3.06 42 52.21 2.635 0.0 11.080 13.905 KFactor= 14.00 to 120 0.0 0.0 0.0 43 104.23 0.0311 0.0 11.080 0.345 Vel = 6.13 43 52.85 2.635 iT 16.474 3.450 14.250 KFactor= 14.00 to 120 0.0 16.474 0.0 22 157.08 0.0664 0.0 19.924 1.323 Vel= 9.24 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 0.0 157.08 15.573 KFactor= 39.80 38 52.54 2.635 0.0 11.410 14.085 K Factor = 14.00 to 120 0.0 0.0 0.0 39 52.54 0.0087 0.0 11.410 0.099 VeI= 3.09 39 52.73 2.635 0.0 11.080 14.184 KFactor= 14.00 to 120 0.0 0.0 0.0 40 105.27 0.0318 0.0 11.080 0.352 Vel = 6.19 40 53.37 2.635 iT 16.474 3.450 14.536 KFactor= 14.00 to 120 0.0 16.474 0.0 18 158.64 0.0676 0.0 19.924 1.347 VeI= 9.33 0.0 158.64 15.883 K Factor= 39.81 35 53.34 2.635 0.0 11.410 14.518 K Factor = 14.00 to 120 0.0 0.0 0.0 36 53.34 0.0090 0.0 11.410 0.103 Vel = 3.14 36 53.54 2.635 0.0 11.080 14.621 KFactor= 14.00 to 120 0.0 0.0 0.0 37 106.88 0.0326 0.0 11.080 0.361 Vel = 6.29 37 54.19 2.635 IT 16.474 3.450 14.982 KFactor= 14.00 to 120 0.0 16.474 0.0 14 161.07 0.0696 0.0 19.924 1.386 Vel = 9.48 0.0 161.07 16.368 KFactor= 39.81 32 51.52 2.635 0.0 11.410 13.542 KFactor= 14.00 to 120 0.0 0.0 0.0 33 51.52 0.0084 0.0 11.410 0.096 VeI= 3.03 33 51.70 2.635 0.0 11.080 13.638 KFactor= 14.00 to 120 0.0 0.0 0.0 34 103.22 0.0306 0.0 11.080 0.339 Vel = 6.07 34 52.34 2.635 IT 16.474 3.450 13.977 KFactor= 14.00 to 120 0.0 16.474 0.0 4 155.56 0.0652 0.0 19.924 1.299 VeI= 9.15 0.0 155.56 15.276 KFactor= 39.80 27 42.39 1.049 1 5.0 0.500 9.168 K Factor = 14.00 to 120 0.0 5.000 0.0 28 42.39 0.5222 0.0 5.500 2.872 Vel = 15.74 28 0.0 1.38 0.0 8.000 12.040 to 120 0.0 0.0 0.0 29 42.39 0.1375 0.0 8.000 1.100 Vel = 9.09 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard JNDUSTRIAL 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 29 44.32 1.61 iT 8.0 5.250 13.140 to 120 0.0 8.000 0.0 30 86.71 0.2436 0.0 13.250 3.228 Vet = 13.66 30 89.85 2.067 iT 10.0 4.500 16.368 to 120 0.0 10.000 1.949 31 176.56 0.2690 0.0 14.500 3.900 Vel = 16.88 31 0.0 4.26 0.0 7.750 22.217 to 120 0.0 0.0 0.0 5A 176.56 0.0080 0.0 7.750 0.062 Vet = 3.97 5A 0.0 6.357 0.0 1.000 22.279 to 120 0.0 0.0 0.0 5 176.56 0.0010 0.0 1.000 0.001 Vet = 1.78 0.0 176.56 22.280 KFactor= 37.41 23 51.06 2.635 0.0 11.410 13.302 KFactor= 14.00 to 120 0.0 0.0 0.0 24 51.06 0.0082 0.0 11.410 0.094 VeI= 3.00 24 51.24 2.635 0.0 11.080 13.396 KFactor= 14.00 to 120 0.0 0.0 0.0 25 102.3 0.0301 0.0 11.080 0.333 Vel = 6.02 25 51.88 2.635 1 16.474 8.040 13.729 KFactor= 14.00 to 120 0.0 16.474 0.0 26 154.18 0.0642 0.0 24.514 1.573 VeI= 9.07 26 155.69 2.635 IT 16.474 4.875 15.302 to 120 0.0 16.474 2.057 6 309.87 0.2335 0.0 21.349 4.984 Vet = 18.23 0.0 309.87 22.343 K Factor= 65.56 19 51.51 2.635 0.0 11.410 13.540 KFactor= 14.00 to 120 0.0 0.0 0.0 20 51.51 0.0084 0.0 11.410 0.096 Vel = 3.03 20 51.70 2.635 0.0 11.080 13.636 KFactor= 14.00 to 120 0.0 0.0 0.0 21 103.21 0.0305 0.0 11.080 0.338 Vet = 6.07 21 52.34 2.635 1 16.474 8.040 13.974 KFactor= 14.00 to 120 0.0 16.474 0.0 22 155.55 0.0652 0.0 24.514 1.599 Vet = 9.15 22 157.07 2.635 1 16.474 4.500 15.573 to 120 0.0 16.474 1.949 7 312.62 0.2372 0.0 20.974 4.976 Vet = 18.39 0.0 312.62 22.498 KFactor= 65.91 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard JNDUSTRIAL 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 15 52.03 2.635 0.0 11.410 13.812 K Factor = 14.00 to 120 0.0 0.0 0.0 16 52.03 0.0086 0.0 11.410 0.098 VeI= 3.06 16 52.21 2.635 0.0 11.080 13.910 K Factor = 14.00 to 120 0.0 0.0 0.0 17 104.24 0.0311 0.0 11.080 0.345 Vel= 6.13 17 52.86 2.635 1 16.474 8.040 14.255 KFactor= 14.00 to 120 0.0 16.474 0.0 18 157.1 0.0664 0.0 24.514 1.628 Vet = 9.24 18 158.65 2.635 1 16.474 4.330 15.883 to 120 0.0 16.474 1.875 8 315.75 0.2417 0.0 20.804 5.028 Vet = 18.58 0.0 315.75 22.786 KFactor= 66.15 11 52.83 2.635 0.0 11.410 14.238 K Factor = 14.00 to 120 0.0 0.0 0.0 12 52.83 0.0089 0.0 11.410 0.101 VeI= 3.11 12 53.01 2.635 0.0 11.080 14.339 K Factor = 14.00 to 120 0.0 0.0 0.0 13 105.84 0.0319 0.0 11.080 0.354 Vet = 6.23 13 53.66 2.635 IT 16.474 8.040 14.693 KFactor= 14.00 to 120 0.0 16.474 0.0 14 159.5 0.0683 0.0 24.514 1.675 VeI= 9.38 14 161.07 2.635 iT 16.474 4.080 16.368 to 120 0.0 16.474 1.767 9 320.57 0.2486 0.0 20.554 5.109 Vet = 18.86 0.0 320.57 23.244 K Factor= 66.49 1 51.02 2.635 0.0 11.410 13.279 KFactor= 14.00 to 120 0.0 0.0 0.0 2 51.02 0.0083 0.0 11.410 0.095 Vet = 3.00 2 51.20 2.635 0.0 11.080 13.374 K Factor = 14.00 to 120 0.0 0.0 0.0 3 102.22 0.0300 0.0 11.080 0.332 Vet= 6.01 3 51.82 2.635 IT 16.474 8.040 13.706 KFactor= 14.00 to 120 0.0 16.474 0.0 4 154.04 0.0640 0.0 24.514 1.570 VeI= 9.06 4 155.57 2.635 1 16.474 4.750 15.276 to 120 0.0 16.474 2.057 5 309.61 0.2331 0.0 21.224 4.947 Vel = 18.22 5 176.56 6.357 0.0 8.500 22.280 to 120 0.0 0.0 0.0 6 486.17 0.0074 0.0 8.500 0.063 Vel = 4.91 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'1 or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 6 309.87 6.357 0.0 8.500 22.343 to 120 0.0 0.0 0.0 7 796.04 0.0182 0.0 8.500 0.155 Vel = 8.05 7 312.62 6.357 0.0 8.500 22.498 to 120 0.0 0.0 0.0 8 1108.66 0.0339 0.0 8.500 0.288 Vel = 11.21 8 315.75 6.357 0.0 8.500 22.786 to 120 0.0 0.0 0.0 9 1424.41 0.0539 0.0 8.500 0.458 Vel = 14.40 9 320.57 6.357 1E 17.603 17.580 23.244 to 120 0.0 17.603 0.0 10 1744.98 0.0784 0.0 35.183 2.757 Vel = 17.64 10 0.0 8.249 0.0 76.000 26.001 to 120 0.0 0.0 0.0 228 1744.98 0.0220 0.0 76.000 1.675 Vel = 10.48 228 0.0 8.249 IT 41.108 26.000 27.676 to 120 0.0 41.108 0.0 TRIP 1744.98 0.0220 0.0 67.108 1.478 Vel = 10.48 TRP 0.0 8.249 1Z 21.141 22.000 29.154 to 120 2E 42.282 63.423 10.178 BRP 1744.98 0.0220 0.0 85.423 1.882 Vel = 10.48 BRP 0.0 8.249 1L 15.269 10.000 41.214 to 120 0.0 15.269 1.949 P1 1744.98 0.0220 0.0 25.269 0.557 Vel = 10.48 P1 0.0 7.98 2E 54.365 106.000 43.720 to 150 0.0 54.365 0.0 P2 1744.98 0.0171 0.0 160.365 2.748 Vel= 11.19 P2 0.0 8.27 2E 56.936 16.000 46.468 to 140 1 55.354 112.290 4.500 *Fixed loss ....45 P3 1744.98 0.0164 0.0 128.290 2.099 Vel= 10.42 P3 0.0 7.98 1G 6.041 85.000 53.067 to 150 iT 52.855 58.895 0.0 P 1744.98 0.0171 0.0 143.895 2.466 VeI= 11.19 0.0 1744.98 55.533 K Factor = 234.16 A -82.06 7.98 2F 27.183 352.000 59.260 to 150 1G 6.041 33.222 0.0 B -82.06 -0.0001 0.0 385.222 -0.023 Vel = 0.53 B 0.0 7.98 IE 27.183 405.000 59.237 to 150 IG 6.041 86.077 0.0 C -82.06 -0.0001 iT 52.855 491.077 -0.029 Vel = 0.53 Computer Programs by Hydratec Inc. 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. "C" or Ftng's Fe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn C 593.60 7.98 2F 27.183 180.000 59.208 to 150 2T 105.71 157.054 0.0 D 511.54 0.0018 4G 24.162 337.054 0.596 Vel= 3.28 D 0.0 11.65 8G 64.398 719.000 59.804 to 150 iT 80.498 144.896 0.0 E 511.54 0.0003 0.0 863.896 0.242 VeI= 1.54 E 0.0 11.65 4G 32.199 379.000 60.046 to 150 0.0 32.200 1.732 TEST 511.54 0.0003 0.0 411.200 0.116 VeI= 1.54 0.0 511.54 61.894 KFactor= 65.02 C -593.60 7.98 4G 24.162 387.000 59.208 to 150 1 13.591 37.754 0.0 M -593.6 -0.0023 0.0 424.754 -0.991 Vel = 3.81 M -117.21 7.98 2G 12.081 220.000 58.217 to 150 0.0 12.082 0.0 N -710.81 -0.0033 0.0 232.082 -0.755 Vel = 4.56 N 1572.39 7.98 2F 27.183 281.000 57.462 to 150 4G 24.162 104.199 0.0 Q 861.58 0.0046 1 52.855 385.199 1.789 Vel= 5.53 Q 0.0 11.65 4G 32.199 438.000 59.251 to 150 1 80.498 130.139 0.0 R 861.58 0.0007 1 17.441 568.139 0.418 VeI= 2.59 R 0.0 11.65 4G 32.199 620.000 59.669 to 150 IF 17.441 49.641 1.732 TEST 861.58 0.0007 0.0 669.641 0.493 Vel = 2.59 0.0 861.58 61.894 KFactor= 109.51 F -117.21 7.98 1 6.041 107.000 58.291 to 150 IT 52.855 72.487 0.0 G -117.21 -0.0001 1 13.591 179.487 -0.021 Vel = 0.75 G 0.0 7.98 0.0 7.000 58.270 to 150 0.0 0.0 0.0 H -117.21 -0.0001 0.0 7.000 -0.001 Vel = 0.75 H 0.0 7.98 0.0 42.000 58.269 to 150 0.0 0.0 0.0 J -117.21 -0.0001 0.0 42.000 -0.005 Vel = 0.75 J 0.0 7.98 0.0 93.000 58.264 to 150 0.0 0.0 0.0 K -117.21 -0.0001 0.0 93.000 -0.010 Vel = 0.75 K 0.0 7.98 0.0 54.000 58.254 to 150 0.0 0.0 0.0 L -117.21 -0.0001 0.0 54.000 -0.007 Vel = 0.75 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. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn L 0.0 7.98 1G 6.041 200.000 58.247 to 150 IT 52.855 58.895 0.0 M -117.21 -0.0001 0.0 258.895 -0.030 Vel = 0.75 0.0 -117.21 58.217 K Factor =-I5.36 N -1572.39 7.98 IF 13.591 64.000 57.462 to 150 1 6.041 72.487 0.0 P -1572.39 -0.0141 IT 52.855 136.487 -1.929 Vel = 10.09 P 2244.98 7.98 5F 67.957 812.000 55.533 Qa = 500 to 150 1 6.041 126.852 0.0 F 672.59 0.0029 1 52.855 938.852 2.758 Vel = 4.31 F 117.21 7.98 2F 27.183 153.000 58.291 to 150 2G 12.081 92.119 0.0 A 789.8 0.0040 IT 52.855 245.119 0.969 Vel = 5.07 A 82.06 7.98 2G 12.081 125.000 59.260 to 150 iT 52.855 64.937 1.732 TEST 871.86 0.0047 0.0 189.937 0.902 Vel = 5.59 0.0 871.86 61.894 K Factor = 110.82 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 APPROVED S UITTED CARLSBAD IRE EPARTMENT - - - 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 P Location : 6186 INNOVATION WAY System REMOTE AREA2 Contract Data File : Towers-P2.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 - 6186 INNOVATION WAY Building - BUILDING P System No. - REMOTE AREA2 Contractor - INDUSTRIAL FIRE SPRINKELR CO. Contract No. - Calculated By - M.G. Drawing No. - FP-7 Construction: (X) Combustible ( ) Non-Combustible Ceiling Height - VARIES Occupancy - O.H. 2 S (X) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 (X) 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 - 1942 System Type Sprinkler/Nozzle Density - .17 (X) Wet Make GLOBE D Area Per Sprinkler - 120 MAX. ( ) Dry Model GL E Elevation at Highest Outlet - 16'-10" ( ) Deluge Size 1/2" S Hose Allowance - Inside - ( ) Preaction K-Factor 5.6 I Rack Sprinkler Allowance - ( ) Other Temp.Rat.200 G Hose Allowance - Outside - 250 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 @ 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 O Storage Ht. Area Aisle W. M Storage Method: Solid Piled % Palletized % Rack M Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Encap. S R ( ) Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non T A ( ) 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 : 10.503 C2 - Residual Pressure: 74 D2 - System Flow : 396.299 stem Pressure : 52.518 02 - Residual Flow : 1780 D2 - SrDemand Hose Adj City Hose ) D3 - System Demand : 646.299 Safety Margin : 22.329 150 140 130 p120 R110 100 S90 S80 lEt Cz u 7° R60 -- D2 E5° 51 40 30 20 10 "T I I I I I I I U 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 1/2 % 1 11/4 11/2 2 21/2 3 31/2 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 ThruTee 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 K-Fact Pt Actual Pn Flow Actual Density Area Press Req. 145 15.67 - 5.6 16.38 na 22.66 0.17 120 7.0 144 15.08 5.6 16.4 na 22.68 0.17 120 7.0 143 15.67 5.6 16.22 na 22.55 0.17 120 7.0 140 15.67 5.6 16.35 na 22.64 0.17 120 7.0 141 15.67 16.76 na 142 15.67 17.28 na 139 16.83 5.6 13.51 na 20.58 0.17 120 7.0 138 16.83 5.6 14.99 na 21.68 0.17 120 7.0 137 16.25 5.6 15.98 na 22.38 0.17 120 7.0 136 15.08 5.6 16.55 na 22.78 0.17 120 7.0 133 15.08 5.6 16.37 na 22.66 0.17 120 7.0 134 15.08 16.78 na 135 15.08 17.3 na 129 15.67 5.6 16.19 na 22.54 0.17 120 7.0 130 15.67 16.6 na 131 15.67 17.11 na 132 15.67 19.05 na 128 16.83 5.6 16.24 na 22.56 0.17 120 7.0 124 16.83 5.6 13.49 na 20.57 0.17 120 7.0 125 16.83 13.83 na 126 16.83 14.26 na 127 16.83 15.82 na 123 16.25 5.6 13.29 na 20.42 0.17 120 7.0 122 16.25 5.6 14.75 na 21.51 0.17 120 7.0 119 16.25 5.6 15.95 na 22.37 0.17 120 7.0 120 16.25 16.35 na 121 16.25 16.86 na 113 15.08 5.6 16.53 na 22.77 0.17 120 7.0 114 15.08 16.94 na 115 15.08 17.47 na 116 15.08 19.26 na 117 13.0 21.11 na 118 13.0 21.19 na 109 16.83 5.6 16.21 na 22.55 0.17 120 7.0 110 16.83 16.62 na 111 16.83 17.13 na 112 16.83 19.07 na 101 16.25 5.6 13.27 na 20.4 0.17 120 7.0 102 16.25 13.61 na 103 16.25 14.03 na 104 16.25 15.57 na 105 16.25 18.77 na 106 13.0 21.5 na 107 13.0 22.23 na 108 24.0 32.57 na TRP 24.0 33.07 na BRP 0.5 43.37 na P1 -4.0 45.35 na P2 -4.0 45.53 na P3 -4.0 50.16 na A -4.0 50.7 na B -4.0 50.69 na C -4.0 50.69 na D -4.0 50.75 na E -4.0 50.77 na TEST -8.0 52.52 na M -4.0 50.59 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. N -4.0 50.52 na Q -4.0 50.69 na R -4.0 50.74 na F -4.0 50.6 na G -4.0 50.6 na H -4.0 50.6 na J -4.0 50.6 na K -4.0 50.59 na L -4.0 50.59 na P -4.0 50.32 na 250.0 The maximum velocity is 15.23 and it occurs in the pipe between nodes 107 and 108 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. ICU or Ftngs Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 145 22.66 1.049 IT 5.0 0.500 16.375 K Factor = 5.60 to 120 0.0 5.000 0.0 142 22.66 0.1640 0.0 5.500 0.902 VeI= 8.41 0.0 22.66 17.277 K Factor = 5.45 144 22.68 1.049 IT 5.0 0.500 16.396 K Factor = 5.60 to 120 0.0 5.000 0.0 135 22.68 0.1642 0.0 5.500 0.903 Vel = 8.42 0.0 22.68 17.299 KFactor= 5.45 143 22.55 1.049 1T 5.0 0.500 16.218 K Factor = 5.60 to 120 0.0 5.000 0.0 131 22.55 0.1625 0.0 5.500 0.894 Vel = 8.37 0.0 22.55 17.112 KFactor= 5.45 140 22.64 1.049 1E 2.0 0.500 16.351 K Factor= 5.60 to 120 0.0 2.000 0.0 141 22.64 0.1636 0.0 2.500 0.409 Vel = 8.40 141 0.0 1.38 0.0 12.000 16.760 to 120 0.0 0.0 0.0 142 22.64 0.0431 0.0 12.000 0.517 Vel = 4.86 142 22.67 1.38 IT 6.0 5.410 17.277 to 120 0.0 6.000 0.0 132 45.31 0.1553 0.0 11.410 1.772 Vel = 9.72 0.0 45.31 19.049 KFactor= 10.38 139 20.58 1.049 iT 5.0 0.500 13.508 K Factor = 5.60 to 120 0.0 5.000 0.0 126 20.58 0.1373 0.0 5.500 0.755 Vel = 7.64 0.0 20.58 14.263 K Factor = 5.45 138 21.68 1.049 1 5.0 0.500 14.992 K Factor = 5.60 to 120 0.0 5.000 0.0 127 21.68 0.1511 0.0 5.500 0.831 Vel = 8.05 0.0 21.68 15.823 K Factor = 5.45 137 22.38 1.049 IT 5.0 0.500 15.977 K Factor = 5.60 to 120 0.0 5.000 0.0 121 22.38 0.1602 0.0 5.500 0.881 Vel = 8.31 0.0 22.38 16.858 KFactor= 5.45 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. "C" or Ftng's Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 136 22.78 1.049 iT 5.0 0.500 16.554 K Factor = 5.60 to 120 0.0 5.000 0.0 115 22.78 0.1656 0.0 5.500 0.911 Vel = 8.46 0.0 22.78 17.465 K Factor= 5.45 133 22.66 1.049 1 2.0 0.500 16.372 K Factor = 5.60 to 120 0.0 2.000 0.0 134 22.66 0.1640 0.0 2.500 0.410 Vel = 8.41 134 0.0 1.38 0.0 12.000 16.782 to 120 0.0 0.0 0.0 135 22.66 0.0431 0.0 12.000 0.517 Vel = 4.86 135 22.67 1.38 IT 6.0 6.580 17.299 to 120 0.0 6.000 0.0 116 45.33 0.1556 0.0 12.580 1.957 Vel= 9.72 0.0 45.33 19.256 KFactor= 10.33 129 22.54 1.049 1E 2.0 0.500 16.194 K Factor = 5.60 to 120 0.0 2.000 0.0 130 22.54 0.1624 0.0 2.500 0.406 Vel= 8.37 130 0.0 1.38 0.0 12.000 16.600 to 120 0.0 0.0 0.0 131 22.54 0.0427 0.0 12.000 0.512 Vel = 4.83 131 22.55 1.38 IT 6.0 6.580 17.112 to 120 0.0 6.000 0.0 132 45.09 0.1540 0.0 12.580 1.937 VeI= 9.67 132 45.30 2.067 1 10.0 2.670 19.049 to 120 0.0 10.000 1.156 118 90.39 0.0780 0.0 12.670 0.988 Vel = 8.64 0.0 90.39 21.193 KFactor= 19.63 128 22.56 1.049 IT 5.0 0.500 16.236 K Factor = 5.60 to 120 0.0 5.000 0.0 111 22.56 0.1625 0.0 5.500 0.894 Vel= 8.37 0.0 22.56 17.130 KFactor= 5.45 124 20.57 1.049 1 2.0 0.500 13.488 K Factor= 5.60 to 120 0.0 2.000 0.0 125 20.57 0.1372 0.0 2.500 0.343 Vel = 7.64 125 0.0 1.38 0.0 12.000 13.831 to 120 0.0 0.0 0.0 126 20.57 0.0360 0.0 12.000 0.432 Vel = 4.41 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. Fitting Pipe Pt Pt Ref. "C" or Ftng's Fe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 126 20.58 1.38 0.0 12.000 14.263 to 120 0.0 0.0 0.0 127 41.15 0.1300 0.0 12.000 1.560 Vel= 8.83 127 21.68 1.38 iT 6.0 5.410 15.823 to 120 0.0 6.000 0.0 112 62.83 0.2846 0.0 11.410 3.247 Vel = 13.48 0.0 62.83 19.070 KFactor= 14.39 123 20.42 1.049 IT 5.0 0.500 13.290 K Factor = 5.60 to 120 0.0 5.000 0.0 103 20.42 0.1353 0.0 5.500 0.744 Vel = 7.58 0.0 20.42 14.034 K Factor = 5.45 122 21.51 1.049 1 5.0 0.500 14.752 K Factor = 5.60 to 120 0.0 5.000 0.0 104 21.51 0.1489 0.0 5.500 0.819 Vel = 7.99 0.0 21.51 15.571 KFactor= 5.4 119 22.37 1.049 1 2.0 0.500 15.953 K Factor =5.60 to 120 0.0 2.000 0.0 120 22.37 0.1600 0.0 2.500 0.400 Vel = 8.30 120 0.0 1.38 0.0 12.000 16.353 to 120 0.0 0.0 0.0 121 22.37 0.0421 0.0 12.000 0.505 Vel= 4.80 121 22.38 1.38 1 6.0 6.580 16.858 to 120 0.0 6.000 0.0 105 44.75 0.1518 0.0 12.580 1.910 Vel = 9.60 0.0 44.75 18.768 KFactor= 10.33 113 22.77 1.049 1E 2.0 0.500 16.530 K Factor =5.60 to 120 0.0 2.000 0.0 114 22.77 0.1652 0.0 2.500 0.413 VeI= 8.45 114 0.0 1.38 0.0 12.000 16.943 to 120 0.0 0.0 0.0 115 22.77 0.0435 0.0 12.000 0.522 Vel= 4.88 115 22.78 1.38 1 6.0 5.410 17.465 to 120 0.0 6.000 0.0 116 45.55 0.1570 0.0 11.410 1.791 Vel= 9.77 116 45.34 2.067 1 10.0 2.080 19.256 to 120 0.0 10.000 0.901 117 90.89 0.0787 0.0 12.080 0.951 Vel = 8.69 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. licit or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 117 0.0 3.26 0.0 10.000 21.108 to 120 0.0 0.0 0.0 118 90.89 0.0085 0.0 10.000 0.085 Vet = 3.49 118 90.39 3.26 0.0 10.000 21.193 to 120 0.0 0.0 0.0 106 181.28 0.0307 0.0 10.000 0.307 VeI= 6.97 0.0 181.28 21.500 KFactor= 39.10 109 22.55 1.049 1E 2.0 0.500 16.212 K Factor = 5.60 to 120 0.0 2.000 0.0 110 22.55 0.1624 0.0 2.500 0.406 Vet = 8.37 110 0.0 1.38 0.0 12.000 16.618 to 120 0.0 0.0 0.0 111 22.55 0.0427 0.0 12.000 0.512 VeI= 4.84 III 22.56 1.38 IT 6.0 6.580 17.130 to 120 0.0 6.000 0.0 112 45.11 0.1542 0.0 12.580 1.940 VeI= 9.68 112 62.83 2.067 IT 10.0 3.830 19.070 to 120 0.0 10.000 1.659 107 107.94 0.1082 0.0 13.830 1.496 VeI= 10.32 0.0 107.94 22.225 KFactor= 22.90 101 20.40 1.049 1 E 2.0 0.500 13.270 K Factor = 5.60 to 120 0.0 2.000 0.0 102 20.4 0.1352 0.0 2.500 0.338 Vet = 7.57 102 0.0 1.38 0.0 12.000 13.608 to 120 0.0 0.0 0.0 103 20.4 0.0355 0.0 12.000 0.426 Vet = 4.38 103 20.42 1.38 0.0 12.000 14.034 to 120 0.0 0.0 0.0 104 40.82 0.1281 0.0 12.000 1.537 Vet = 8.76 104 21.50 1.38 1 6.0 5.410 15.571 to 120 0.0 6.000 0.0 105 62.32 0.2802 0.0 11.410 3.197 Vet = 13.37 105 44.76 2.067 IT 10.0 2.420 18.768 to 120 0.0 10.000 1.408 106 107.08 0.1066 0.0 12.420 1.324 Vel= 10.24 106 181.28 3.26 0.0 10.000 21.500 to 120 0.0 0.0 0.0 107 288.36 0.0725 0.0 10.000 0.725 Vet= 11.08 107 107.94 3.26 4E 37.631 57.950 22.225 to 120 IT 20.159 57.790 -4.764 108 396.3 0.1305 0.0 115.740 15.105 VeI= 15.23 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. or Ftng's Fe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 108 0.0 6.357 1 17.603 44.200 32.566 to 120 1 37.72 55.323 0.0 TRP 396.3 0.0050 0.0 99.523 0.502 Vet = 4.01 TRP 0.0 8.249 1Z 21.141 22.000 33.068 to 120 2E 42.282 63.423 10.178 BRP 396.3 0.0014 0.0 85.423 0.121 Vet = 2.38 BRP 0.0 8.249 1L 15.269 10.000 43.367 to 120 0.0 15.269 1.949 P1 396.3 0.0014 0.0 25.269 0.036 Vet = 2.38 P1 0.0 7.98 2E 54.365 106.000 45.352 to 150 0.0 54.365 0.0 P2 396.3 0.0011 0.0 160.365 0.177 VeI= 2.54 P2 0.0 8.27 2E 56.936 16.000 45.529 to 140 iT 55.354 112.290 4.500 * Fixed loss = 4.5 P3 396.3 0.0011 0.0 128.290 0.135 Vet = 2.37 P3 0.0 7.98 1 6.041 85.000 50.164 to 150 iT 52.855 58.895 0.0 P 396.3 0.0011 0.0 143.895 0.159 Vet = 2.54 0.0 396.30 50.323 KFactor= 55.87 A -23.62 7.98 2F 27.183 352.000 50.695 to 150 IG 6.041 33.222 0.0 B -23.62 0.0 0.0 385.222 -0.002 Vet = 0.15 B 0.0 7.98 1E 27.183 405.000 50.693 to 150 1G 6.041 86.077 0.0 C -23.62 0.0 IT 52.855 491.077 -0.003 Vet = 0.15 C 170.88 7.98 2F 27.183 180.000 50.690 to 150 2T 105.71 157.054 0.0 D 147.26 0.0002 4G 24.162 337.054 0.060 Vet = 0.94 D 0.0 11.65 8G 64.398 719.000 50.750 to 150 IT 80.498 144.896 0.0 E 147.26 0.0 0.0 863.896 0.024 Vet = 0.44 E 0.0 11.65 4G 32.199 379.000 50.774 to 150 0.0 32.200 1.732 TEST 147.26 0.0 0.0 411.200 0.012 Vet = 0.44 0.0 147.26 52.518 KFactor= 20.32 C -170.89 7.98 4G 24.162 387.000 50.690 to 150 1 13.591 37.754 0.0 M -170.89 -0.0002 0.0 424.754 -0.099 Vet = 1.10 M -33.74 7.98 2G 12.081 220.000 50.591 to 150 0.0 12.082 0.0 N -204.63 -0.0003 0.0 232.082 -0.075 Vet = 1.31 Computer Programs by Hydratec Inc. 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. "C'1 or Ftng's Fe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn N 452.67 7.98 2F 27.183 281.000 50.516 to 150 4G 24.162 104.199 0.0 Q 248.04 0.0005 iT 52.855 385.199 0.178 Vel= 1.59 Q 0.0 11.65 4G 32.199 438.000 50.694 to 150 iT 80.498 130.139 0.0 R 248.04 0.0001 IF 17.441 568.139 0.042 Vet = 0.75 R 0.0 11.65 4G 32.199 620.000 50.736 to 150 1 17.441 49.641 1.732 TEST 248.04 0.0001 0.0 669.641 0.050 Vet = 0.75 0.0 248.04 52.518 KFactor= 34.23 F -33.74 7.98 IG 6.041 107.000 50.599 to 150 IT 52.855 72.487 0.0 G -33.74 0.0 IF 13.591 179.487 -0.003 Vet = 0.22 G 0.0 7.98 0.0 7.000 50.596 to 150 0.0 0.0 0.0 H -33.74 0.0 0.0 7.000 0.0 Vet = 0.22 H 0.0 7.98 0.0 42.000 50.596 to 150 0.0 0.0 0.0 J -33.74 0.0 0.0 42.000 0.0 Vet = 0.22 J 0.0 7.98 0.0 93.000 50.596 to 150 0.0 0.0 0.0 K -33.74 0.0 0.0 93.000 -0.001 Vet = 0.22 K 0.0 7.98 0.0 54.000 50.595 to 150 0.0 0.0 0.0 L -33.74 0.0 0.0 54.000 -0.001 Vet = 0.22 L 0.0 7.98 IG 6.041 200.000 50.594 to 150 IT 52.855 58.895 0.0 M -33.74 0.0 0.0 258.895 -0.003 Vet = 0.22 0.0 -33.74 50.591 K Factor= -4.74 N -452.67 7.98 1 13.591 64.000 50.516 to 150 1G 6.041 72.487 0.0 P -452.67 -0.0014 iT 52.855 136.487 -0.193 Vet = 2.90 P 646.30 7.98 SF 67.957 812.000 50.323 Qa=250 to 150 1G 6.041 126.852 0.0 F 193.63 0.0003 IT 52.855 938.852 0.276 Vet = 1.24 F 33.74 7.98 2F 27.183 153.000 50.599 to 150 2G 12.081 92.119 0.0 A 227.37 0.0004 1T 52.855 245.119 0.096 Vet= 1.46 A 23.63 7.98 2G 12.081 125.000 50.695 to 150 1T 52.855 64.937 1.732 TEST 251.0 0.0005 0.0 189.937 0.091 Vet = 1.61 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. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 0.0 251.00 52.518 KFactor= 34.64 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 APPROVED SiJBfl1JITTED TMENT - - - 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 P Location : 6186 INNOVATION WAY System : REMOTE AREA3 Contract Data File : Towers-P3.WXF 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 - 6186 INNOVATION WAY Building - BUILDING P System No. - REMOTE AREA3 Contractor - INDUSTRIAL FIRE SPRINKELR CO. Contract No. - Calculated By - M.G. Drawing No. - FP-7 Construction: (X) Combustible ( ) Non-Combustible Ceiling Height - 91 -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 - 930 System Type Sprinkler/Nozzle Density - .10 (X) Wet Make GLOBE D Area Per Sprinkler - 20'x20' ( ) Dry Model GL8109 E Elevation at Highest Outlet - 9'-2" ( ) Deluge Size 3/4" S Hose Allowance - Inside - ( ) Preaction K-Factor 8.1 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 @ 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 O Storage Ht. Area Aisle W. M Storage Method: Solid Piled % Palletized % Rack M Single Row ( ) Conven. Pallet ( ) Auto. Storage ( ) Encap. S R ( ) Double Row ( ) Slave Pallet ( ) Solid Shelf ( ) Non T A ( ) Mult. Row ( ) Open Shelf O C R K Flue Spacing Clearance:Storage to Ceiling A Longitudinal Transverse G H 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 DI - Elevation : 7.436 C2 - Residual Pressure: 74 D2 - System Flow : 203.507 stem Pressure : 65.729 C2 - Residual Flow : 1780 D2 - SrAdj Hose City)___Hose Demand) : 100 D3 - System Demand : 303.507 Safety Margin : 9.233 150 140 130 p120 R0 E100 S90 80 u 70 ii R6° E5° 40 30 20 - ....l.I.I.I.-. 10 I ... .. ... I.... .. 200 400 600 800 1000 1200 1400 1600 1800 FLOW (NAI.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 1/2 % 1 11/4 11/2 2 21/2 3 31/2 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 ThruTee 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 / Flow Summary - STANDARD INDUSTRIAL FIRE SPRINKLER CO. Page 4 TOWERS AT BRESSI Date 5/2/07 Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Req. Dl 9.17 8.1 27.45 na 42.43 0.1 400 24.4 D2 9.17 8.1 27.75 na 42.67 0.1 400 24.4 D3 9.17 8.1 24.02 na 39.7 0.1 330 16.6 D4 9.17 8.1 22.82 na 38.69 0.1 330 16.6 D5 9.17 8.1 24.4 na 40.01 0.1 400 24.4 214 9.67 28.85 na 212 9.67 25.36 na 213 10.0 27.48 na 210 9.67 23.7 na 211 10.0 27.02 na 206 9.67 24.96 na 207 10.0 27.06 na 208 10.0 28.7 na 209 10.0 28.9 na 201 9.67 28.54 na 202 10.0 30.92 na 203 10.0 32.85 na 204 10.0 38.87 na 205 10.0 39.78 na 225 10.0 43.92 na 226 24.0 45.33 na 227 24.0 45.44 na 228 24.0 45.54 na TRP 24.0 45.57 na BRP 0.5 55.79 na P1 -4.0 57.75 na P2 -4.0 57.8 na P3 -4.0 63.84 na A -4.0 63.97 na B -4.0 63.97 na C -4.0 63.97 na D -4.0 63.99 na E -4.0 63.99 na TEST -8.0 65.73 na M -4.0 63.95 na N -4.0 63.93 na Q -4.0 63.97 na R -4.0 63.98 na F -4.0 63.95 na G -4.0 63.95 na H -4.0 63.95 na J -4.0 63.95 na K -4.0 63.95 na L -4.0 63.95 na P -4.0 63.88 na 100.0 The maximum velocity is 18.66 and it occurs in the pipe between nodes 209 and 205 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams INDUSTRIAL FIRE SPRINKLER CO. Page 5 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 Dl 42.43 1.049 1E 2.0 0.500 27.446 K Factor= 8.10 to 120 0.0 2.000 -0.217 201 42.43 0.5232 0.0 2.500 1.308 Vel = 15.75 0.0 42.43 28.537 K Factor = 7.94 D2 42.67 1.049 1 2.0 0.500 27.748 K Factor = 8.10 to 120 0.0 2.000 -0.217 214 42.67 0.5284 0.0 2.500 1.321 Vel= 15.84 0.0 42.67 28.852 K Factor= 7.94 D3 39.70 1.049 1E 2.0 0.500 24.024 K Factor = 8.10 to 120 0.0 2.000 -0.217 206 39.7 0.4628 0.0 2.500 1.157 Vel= 14.74 0.0 39.70 24.964 K Factor = 7.95 D4 38.69 1.049 1 2.0 0.500 22.818 K Factor =8.10 to 120 0.0 2.000 -0.217 210 38.69 0.4416 0.0 2.500 1.104 Vel= 14.36 0.0 38.69 23.705 K Factor = 7.95 D5 40.01 1.049 1E 2.0 0.500 24.400 K Factor= 8.10 to 120 0.0 2.000 -0.217 212 40.01 0.4696 0.0 2.500 1.174 Vel= 14.85 0.0 40.01 25.357 K Factor= 7.95 214 42.67 1.049 1E 2.0 0.830 28.852 to 120 iT 5.0 7.000 -0.143 203 42.67 0.5287 0.0 7.830 4.140 Vel = 15.84 0.0 42.67 32.849 K Factor = 7.44 212 40.01 1.049 2E 4.0 0.830 25.357 to 120 0.0 4.000 -0.143 213 40.01 0.4694 0.0 4.830 2.267 Vel = 14.85 213 0.0 1.38 iT 6.0 5.500 27.481 to 120 0.0 6.000 0.0 209 40.01 0.1235 0.0 11.500 1.420 Vel = 8.58 0.0 40.01 28.901 K Factor = 7.44 210 38.69 1.049 1E 2.0 0.830 23.705 to 120 1 5.0 7.000 -0.143 211 38.69 0.4411 0.0 7.830 3.454 VeI= 14.36 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Standard 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 Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 211 0.0 1.38 iT 6.0 8.500 27.016 to 120 0.0 6.000 0.0 208 38.69 0.1160 0.0 14.500 1.682 Vel = 8.30 0.0 38.69 28.698 K Factor = 7.22 206 39.70 1.049 2E 4.0 0.830 24.964 to 120 0.0 4.000 -0.143 207 39.7 0.4627 0.0 4.830 2.235 Vel = 14.74 207 0.0 1.38 0.0 13.500 27.056 to 120 0.0 0.0 0.0 208 39.7 0.1216 0.0 13.500 1.642 Vel= 8.52 208 38.69 1.61 0.0 1.000 28.698 to 120 0.0 0.0 0.0 209 78.39 0.2030 0.0 1.000 0.203 Vel = 12.35 209 40.01 1.61 iT 8.0 17.080 28.901 to 120 0.0 8.000 0.0 205 118.4 0.4337 0.0 25.080 10.876 Vel= 18.66 0.0 118.40 39.777 K Factor = 18.77 201 42.43 1.049 2E 4.0 0.830 28.537 to 120 0.0 4.000 -0.143 202 42.43 0.5234 0.0 4.830 2.528 Vel = 15.75 202 0.0 1.38 0.0 14.000 30.922 to 120 0.0 0.0 0.0 203 42.43 0.1376 0.0 14.000 1.927 VeI= 9.10 203 42.67 1.61 iT 8.0 17.580 32.849 to 120 0.0 8.000 0.0 204 85.1 0.2354 0.0 25.580 6.021 Vel = 13.41 204 0.0 2.157 0.0 16.000 38.870 to 120 0.0 0.0 0.0 205 85.1 0.0567 0.0 16.000 0.907 Vel = 7.47 205 118.41 2.157 1 6.153 8.420 39.777 to 120 0.0 6.153 0.0 225 203.51 0.2842 0.0 14.573 4.142 Vel = 17.87 225 0.0 2.157 iT 12.307 14.000 43.919 to 120 0.0 12.307 -6.063 226 203.51 0.2842 0.0 26.307 7.477 Vel = 17.87 226 0.0 4.26 0.0 10.000 45.333 to 120 0.0 0.0 0.0 227 203.5.1 0.0103 0.0 10.000 0.103 Vel = 4.58 227 0.0 6.357 IT 37.72 36.330 45.436 to 120 0.0 37.720 0.0 228 203.51 0.0015 0.0 74.050 0.109 Vel = 2.06 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 Fe Pv ******* Notes Point Qt Pt/Ft Eqv. Ln. Total Pf Pn 228 0.0 8.249 1 41.108 26.000 45.545 to 120 0.0 41.108 0.0 TRP 203.51 0.0004 0.0 67.108 0.028 Vel = 1.22 TRP 0.0 8.249 1Z 21.141 22.000 45.573 to 120 2E 42.282 63.423 10.178 BRP 203.51 0.0004 0.0 85.423 0.035 Vel = 1.22 BRP 0.0 8.249 1L 15.269 10.000 55.786 to 120 0.0 15.269 1.949 P1 203.51 0.0004 0.0 25.269 0.010 Vel = 1.22 P1 0.0 7.98 2E 54.365 106.000 57.745 to 150 0.0 54.365 0.0 P2 203.51 0.0003 0.0 160.365 0.052 Vel = 1.31 P2 0.0 8.27 2E 56.936 16.000 57.797 to 140 1 55.354 112.290 6.000 * Fixed loss = 6 P3 203.51 0.0003 0.0 128.290 0.039 Vel = 1.22 P3 0.0 7.98 IG 6.041 85.000 63.836 to 150 IT 52.855 58.895 0.0 P 203.51 0.0003 0.0 143.895 0.047 Vel = 1.31 0.0 203.51 63.883 K Factor= 25.46 A -11.09 7.98 2F 27.183 352.000 63.975 to 150 1G 6.041 33.222 0.0 B -11.09 0.0 0.0 385.222 -0.001 Vel = 0.07 B 0.0 7.98 1E 27.183 405.000 63.974 to 150 IG 6.041 86.077 0.0 C -11.09 0.0 IT 52.855 491.077 -0.001 Vel = 0.07 C 80.25 7.98 2F 27.183 180.000 63.973 to 150 2T 105.71 157.054 0.0 D 69.16 0.0 4G 24.162 337.054 0.015 Vel = 0.44 D 0.0 11.65 8G 64.398 719.000 63.988 to 150 IT 80.498 144.896 0.0 E 69.16 0.0 0.0 863.896 0.006 Vel = 0.21 E 0.0 11.65 4G 32.199 379.000 63.994 to 150 0.0 32.200 1.732 TEST 69.16 0.0 0.0 411.200 0.003 Vel = 0.21 0.0 69.16 65.729 K Factor = 8.53 C -80.25 7.98 4G 24.162 387.000 63.973 to 150 IF 13.591 37.754 0.0 M -80.25 -0.0001 0.0 424.754 -0.024 Vel = 0.51 M -15.85 7.98 2G 12.081 220.000 63.949 to 150 0.0 12.082 0.0 N -96.1 -0.0001 0.0 232.082 -0.019 Vel = 0.62 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. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn N 212.58 7.98 2F 27.183 281.000 63.930 to 150 4G 24.162 104.199 0.0 Q 116.48 0.0001 IT 52.855 385.199 0.044 Vel= 0.75 Q 0.0 11.65 4G 32.199 438.000 63.974 to 150 1T 80.498 130.139 0.0 R 116.48 0.0 IF 17.441 568.139 0.011 Vel= 0.35 R 0.0 11.65 4G 32.199 620.000 63.985 to 150 1 17.441 49.641 1.732 TEST 116.48 0.0 0.0 669.641 0.012 Vel = 0.35 0.0 116.48 65.729 KFactor= 14.37 F -15.85 7.98 1G 6.041 107.000 63.951 to 150 IT 52.855 72.487 0.0 G -15.85 0.0 1 13.591 179.487 -0.001 Vel = 0.10 G 0.0 7.98 0.0 7.000 63.950 to 150 0.0 0.0 0.0 H -15.85 0.0 0.0 7.000 0.0 Vel = 0.10 H 0.0 7.98 0.0 42.000 63.950 to 150 0.0 0.0 0.0 J -15.85 0.0 0.0 42.000 0.0 Vel = 0.10 J 0.0 7.98 0.0 93.000 63.950 to 150 0.0 0.0 0.0 K -15.85 0.0 0.0 93.000 0.0 Vel = 0.10 K 0.0 7.98 0.0 54.000 63.950 to 150 0.0 0.0 0.0 L -15.85 0.0 0.0 54.000 0.0 Vel = 0.10 L 0.0 7.98 1G 6.041 200.000 63.950 to 150 IT 52.855 58.895 0.0 M -15.85 0.0 0.0 258.895 -0.001 Vel = 0.10 0.0 -15.85 63.949 KFactor= -1.98 N -212.58 7.98 iF 13.591 64.000 63.930 to 150 1G 6.041 72.487 0.0 P -212.58 -0.0003 IT 52.855 136.487 -0.047 Vel = 1.36 P 303.51 7.98 5F 67.957 812.000 63.883 Qa= 100 to 150 IG 6.041 126.852 0.0 F 90.93 0.0001 iT 52.855 938.852 0.068 Vel = 0.58 F 15.85 7.98 2F 27.183 153.000 63.951 to 150 2G 12.081 92.119 0.0 A 106.78 0.0001 IT 52.855 245.119 0.024 Vel = 0.68 A 11.09 7.98 2G 12.081 125.000 63.975 to 150 1 52.855 64.937 1.732 TEST 117.87 0.0001 0.0 189.937 0.022 Vel = 0.76 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 0.0 117.87 65.729 KFactor= 14.54 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 02-01-07 10:15am From—Industrial Fire Sprinkler 619 266 6035 T-221 P.001/001 F-886 \ /((J (eV—VWl Flow Test Record Teat Hydrant caon €An IOVI Hydrant It) No. Size Main Static ............. j3 JIH t€V Qs f+.;) Residual ......... _71 Pressure Drop.. ________(PD! 1) .... K factor for PDI I Flow Hydrait() Hydrant 1 location fly __c) C _QLJj ._Jirt u cth Hydrant 2 location_ Hydrant 3 location_ IVyloVrA;Hofl Calculated test and flow data - Static...................... Desired Residual.......20 GPM:C}S1>4 63DSize of Orifice GPM:- Size of Orifice_________ GPM; Size of Orifice________ Total: I7D , OxPD2k =Q2 PDI*k Hydrant 1 Pi tot __-psi Hydrant 2 Pitot PSI Hydrant 3 Pitot_-_PSI Pressure Drop (PD 2).. _________________________________K factor PD 2; _ x divided by equals GPM at 20 psi residual Q PD2k PD1k Q2 Comments: Test conducted for: rtJ1er Cal 0~, Conducted by:J) I, cv,_I Eri((k%rtcd p(( Date:J 3H Time:_ IOO 1!