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HomeMy WebLinkAbout5923 FARNSWORTH CT; ; AS140303; PermitCity of Carlsbad Sprinkler Permit Permit No: AS140303 5923 FARNSWORTH Job Address: CT Permit Type: SPRINK Parcel No: 2120700800 Lot #: 0 Reference No.: PC #: Status: ISSUED Applied 11/25/2014 Approved: 12/1/2014 Issued: 12/1/2014 Inspector: Project Title: GOOD FEET ALL DESIGN AND INSTALLATION TO BE PER NFPA 13 AND THE CFD. SEE THE TECHNICAL REPORT FOR ALL INFORMATION REGARDING STORAGE OF COMMODITIES, TYPES, AND ARRANGEMENTS, DESIGN OF ONE LEVEL OF IN- RACKS WITH AN OVERHEAD DENSITY OF 45/2000 IS PER THE TECHNICAL REPORT. Applicant: EPIC FIRE PROTECTION, INC. 765 TURTLE POINT WY SAN MARCOS, CA 760-310-6122 Owner: GROWING PAINS L L C P 0 BOX 339 VISTA CA Fees ($) Add'I Fees ($) Total ($) Balance ($) 280 0 280 0 / 'Pest Hydrant Location Hydrant ID No. Flow Test Record Main Static.............UO Residual ......... lop Pressure Drop.. _JD_.. (PDI 1).....K factor for PDI I 34 Flow Hydrant(s) Hydrant 1 location______________________________ Hydrant 2 location Hydrant 3 location Hydrant I Pitot PSI GPM: Size of Orifide ' Hydrant 2 Pitot PSI GPM: Size of Orifice__________ Hydrant 3 Pitot PSI GPM: Size of Orifice.__________ Total: IA1 Calculated test and flow data - Q x PD2 k =Q2 PDI*k Static........................ Desired Residual.......20 Pressure Drop (PD 2).."t ( K factor PD 2:1 ( 3G 1t x 1 .3G divided by _3.4l equal s_45d1- GPM at 20 psi residual Q PD2k PDIk Q2 Comments: Test conducted for: Conducted by: Date: 9.tCt.t4 Time: _'2.tc7 ?t'1 upply I Demand (iraph 160 140 120 100 0. 40 20 n A S l4o6ôS E3 8:8 oo Hydraulics Summary Sheet DasIthoardHydsullcc Project Information Calculation Date: 10/14/2014 2:32:00 PM GOODFEET IN-RACKS system ID drawing ref 1 OF 1 5923 FARNSWORTH CT. CARLSBAD, CA 92008 contract # Contractor Information Epic Fire Protection, Inc. 765 Turtle Point Way San Marcos, CA 92069 calculated by Adam Boisvert telephone 760-310-6122 fax 760-798-0556 email epicflre@cox.net .__!__ •_I___ I. ..s.. Pu. No. Mfgr Mod SlN# Size K 25 VICTAULIC ELO SSU 1 1 3I4 11.2 8 VIKING SSP I VK302 1 1/2" 15.6 building EXISTING construction CONCRETE! WOOD occupancy authority Hydraulics Criteria density .45 GPM/ft2 system type WET design std NFPA 13 remote area 2000 ft2 hazard EXTRA spr coverage 82 ft2 sprs flowing 33 figure 17.2.1.2.1 calcd volume 377.3 gal curve D IrnA, Tact static pressure 99.00 psi residual pressure 90.00 psi quantity flowing 1,385.0 GPM elevation from if 0.00 ft date & time of flow test 9-19-14 location of flow test SITE 0250 500 750 1000 1250 1500 1750 2000 Water Flow (GPM) Demand at sprinkler and interior hose flows .Total 9Y stem Demand including Hose Flows at Zero © Copyright 2013 Sigma Development Group, Inc. AS Page 1 of 11 QT8JOd_ Dashboard Hydraulics Supply Analysis GOODFEET IN-RACKS Sprinkler Flow: 1,268.0 GPM Additional Flows: None Hose Flow at Zero: 500.0 GPM Total System Flow: 1,768.0 GPM Maximum velocity in pipe 11 - 16 is 23.6 ft/sec Nodes Analysis Minimum Node Actual Node Elev Device KFactor Flow Pressure Discharge Notes ft-1 GPM psi GPM 207 11.0 Sprinkler 5.60 21.69 22.57 26.60 206 11.0 Sprinkler 5.60 21.69 22.62 26.63 205 11.0 Sprinkler 5.60 21.69 22.79 26.74 204 11.0 Sprinkler 5.60 21.69 23.17 1 26.96 203 11.0 Sprinkler 5.60 21.69 23.81 27.33 202 11.0 Sprinkler 5.60 21.69 24.79 27.88 201 11.0 Sprinkler 5.60 21.69 26.18 28.66 200 11.0 Sprinkler 5.60 21.69 28.06 29.67 177 28.0 Sprinkler 11.20 36.90 10.85 36.90 176 28.0 Sprinkler 11.20 36.90 10.91 37.00 173 28.0 Sprinkler 11.20 36.90 10.93 37.02 172 28.0 Sprinkler 11.20 36.90 10.98 37.12 175 28.0 Sprinkler 11.20 36.90 11.12 37.35 169 28.0 Sprinkler 11.20 36.90 11.19 37.46 171 28.0 Sprinkler 11.20 36.90 11.19 37.47 168 28.0 Sprinkler 11.20 36.90 11.25 37.56 167 28.0 Sprinkler 11.20 36.90 11.46 37.92 165 28.0 Sprinkler 11.20 36.90 11.75 _38.39 164 28.0 Sprinkler 11.20 36.90 11.81 38.49 163 28.0 Sprinkler 11.20 36.90 12.03 38.86 161 28.0 Sprinkler 11.20 36.90 12.72 39.94 160 28.0 Sprinkler 11.20 36.90 12.79 40.05 159 28.0 Sprinkler 11.20 36.90 13.03 40.42 157 28.0 Sprinkler 11.20 36.90 14.22 42.24 156 28.0 Sprinkler 11.20 36.90 14.30 42.35 0 Copyright 2013 Sigma Development Group, Inc. Page 2 of 11 E < - > > C L i = Nodes Analysis Minimum Node Actual Node Elev Device KFactor Flow Pressure Discharge Notes ft GPM psi GPM 155 28.0 Sprinkler 11.20 36.90 14.56 42.74 153 28.0 Sprinkler 11.20 36.90 16.41 45.36 152 28.0 Sprinkler 11.20 36.90 16.49 45.48 151 28.0 Sprinkler 11.20 36.90 16.80 45.90 162 28.0 Sprinkler 11.20 36.90 21.67 52.14 158 28.0 Sprinkler 11.20 36.90 21.81 52.31 154 28.0 Sprinkler 11.20 36.90 22.31 52.91 150 28.0 Sprinkler 11.20 36.90 23.38 54.16 0 0.0 Hose@Zero 78.33 500.0 © Copyright 2013 Sigma Development Group, Inc. Page 3 of 11 4800 hfraidHy Pipe Information Da thauIks GOODFEET IN-RACKS From Elevl ft Pipe ID Flows Added GPM Inside Diameter in I Fittings Length C Value [Total (Pt) psi Notes I Fitting ft I I Elev (Pe) psi To Elev2 I Type Friction Lossi [ psi/ft Total jTotal ft Frict (Pt) psi 127 27.00 1" Dyna lhead 1.0800 1 Len 1.0 Ftg 5.8 0=120 Pt 177) 10.854 Pe 0.433 Pf 2.371 177 28.00 SG 36.9 0.35065 Total 6.8 123 27.00 2 Dyna Flow 2.2030 0 Len 8.0 Ftg 0.0 c = 120 Pt 127) 13.658 Pe 0.000 Pt 0.087 Total 8.0 127 27.00 BN 36.9 0.01089 Total Pressure at Node 123) 13.745 psi 206 11.00 2" Dyna Flow 2.2030 0 Len 3 8. Ftg 0.0 0=120 Pt 207) 22.568 Pe 0.000 Pt 0.049 207 11.00 BN2 26.6 0.00595 Total 8.3 205 11.00 2" Dyna Flow 26.6 2.2030 0 Len 8.3 Ftg 0.0 0= 120 Pt 206) 22.617 Pe 0.000 Pt 0.177 206 11.00 BN2 53.2 0.02146 204 11.00 2" Dyna Flow 26.7 2.2030 0 Len 3 8. Ftg 0.0 0=120 Pt 205) 22.794 Pe 0.000 Pt 0.376 205 11.00 BN2 80.0 0.04556 Total 8.3 203 11.00 2 Dyna Flow 27.0 2.2030 0 Len 3 8. Ftg 0.0 0=120 Pt 204) 23.170 Pe 0.000 Pf 0.643 204 11.00 BN2 106.9 0.07798 Total 8.3 202 11.00 2° Dyna Flow 27.3 2.2030 0 Len 8.3 Ftg 0.0 0=120 Pt 203) 23.814 Pe 0.000 Pf 0.980 203 11.00 BN2 134.3 0.11881 Total 8.3 201 11.00 2 Dyna Flow 27.9 2.2030 0 Len 8.3 Ftg 0.0 C = 120 Pt 202) 24.794 Pe 0.000 Pf 1.390 202 11.00 BN2 162.1 0.16845 Total 8.3 200 11.00 2" Dyna Flow 28.7 2.2030 0 Len 8.3 Ftg 0.0 0 120 Pt 201) 26.184 Pe 0.000 Pt 1.878 201 11.00 BN2 190.8 0.22763 Total 8.3 44 11.00 2Dyna Flow 29.7 2.2030 T Len 20.0 Ftg 13.6 C = 120 Pt 200) 28.062 Pe 0.000 Pt 10.004 200 11.00 BN2 220.5 0.29740 Total 33.61 Total iressure at NoueK) ao.uou pi 126 I 27.00 1' Dyna lhead 1 1.0800 T Len 1.0 Ftg 5.8 = 120 1 Pt 176) 10.911 Pe 0.433 Pt 2.383 176 28.00 SG 37.0 I 0.352371 Total 6.8 © Copyright 2013 Sigma Development Group, Inc. Page 4 of 11 Aft Oas y ou- auI,cs Pipe Information GOODFEET IN-RACKS From Elvi ft Pipe ID Flows Added GPM Inside Diameter in Fittings Length ft l C Value I I Loss' psi/ft jTotal (Pt) psi Notes Fitting ft'Friction Elev (Pe) psi To Elev2 Type Total Total ft1 1Frict (PQ psi - 122 27.00 2' Dyna Flow 2.2030 0 Len 8.0J Ftg 0.0 c = 120 I-1 0.01095] ft 126) 13.727 Pe 0.000 0.088 126 27.00 BN 37.0 :Total -01 Total Pressure at Node 122) 13.815 psi 125 27.00 1' Dyna Thead 1.0800 T Len 1.0 Ftg 5.8 C = 120 0.35858 Pt 175) 11.120 Pe 0.433 Pt 2.425 175 28.00 SG 37.3 Total 6.8 121 27.00 2' Dyna Flow 2.2030 0 Len 8.0 Ftg 0.0 C = 120 Pt 125) 13.977 Pe 0.000 Pf 0.089 125 27.00 BN 37.3 Total 8.00.01114 Total Pressure at Node 121) 14.066 psi 112 27.00 1' Dyna lhead 1.0800 1 Len 1.0J10 Ftg 5.8 Pt 162) 21.674 Pe 0.433 pf 4.495 162 28.00 SG 52.1 0.66481 Total 6.8 Total Pressure at Node 112) 26.603 psi 123 27.00 1' Dyna Thead 1.0800 T Len 1.0 Ftg 5.8 c = 120 0.35282 Pt 173) 10.926 Pe 0.433 Pt 2.386 173 28.00 SG 37.0 Total 6.8 119 27.00 2"DynaFlow 36.9 2.2030 0 Len 8.0 Ftg 0.0 C= 120 0.03939 Pt 123) 13.745 Pe 0.000 pf 0.315 123 27.00 BN 73.9 Total Pressure at Node 119) 14.060 psi 122 27.00 Dyna Thead 1.0800 T Len 1.0 Ftg 5.8 C= 120 Pt 172) 10,984 Fe 0.433 Pt 2.397 172 28.00 SG 37.1 0.35455 Total 6.8 118 27.00 Dyna Flow 370 2.2030 0 Len 8.0 Ftg 0.0 C= 120 Pt 122) 13.815 Pe 0.000 Pt 0.317 122 27.00 BN 74.1 0.03959 Total 8.0 Total Pressure at Node 118) 14.131 psi 121 27.00 1" Dyna lhead 1.0800 T Len 1.0 Ftg 5.8 C = 120 Pt 171) 11.194 Pe 0.433 Pt 2.440 171 28.00 SG 37.5 0.36079 Total 6.8 117 27.00 2 Dyna Flow 37.3 2.2030 0 Len 8.0 Ftg 0.0 = 120 Pt 121) 14.066 Pe 0.000 Pt 0.322 121 27.00 BN 74.8 0.04028 Total 8.0 Total Pressure at Node 117) 14.389 psi 0 Copyright 2013 Sigma Development Group, Inc. Page 5 of 11 Da d8OO" Pipe Information GOODFEET IN-RACKS From Elevi ft Pipe ID Flows Added T I Inside Length ftl I c Value 1Total (Pt) psi GPM I Diameter I .n I I Fittings Fitting ft I IFriction Lossl psi/ft I Elev (Pe) psi Notes IFriCt (Pf) psi To Elev2 Type Total Total ft1 119 27.00 1" Dyna Thead 1.0800 1 Len 1.0 Ftg 5.8 c = 120 0.36064 Pt 169) 11.189 Pe 0.433 Pt 2.439 169 28.00 SG 37.5 Total 6.8 115 27.00 2 Dyna Flow 739 2.2030 0 Len 8.0 Ftg 0.0 C = 120 0.08410 Pt 119) 14.060 1 Pe 0.000 Pt 0.673 Total 8.0 119 27.00 BN 111.4 Total Pressure at Node 115) 14.733 psi 118 27.00 1 Dyna Thead 1.0800 T Len 1.0 Ftg 5.8 c = 120 Pt 168) 11.248 Pe 0.433 Pt 2.451 168 28.00 SG 37.6 0.36241 Total 6.8 114 27.00 2" Dyna Flow 74.1 2.2030 0 Len 8.0 Ftg 0.0 C= 120 Pt 118) 14.131 Pe 0.000 Pt 0.676 Total 8.0 118 27.00 BN 111.7 0.08452 Total Pressure at Node 114) 14.808 psi 117 27.00 1" Dyna Thead Len 1.0 C= 120 Pt 167) 11.462 1.0800 T Ftg 5.8 Pe 0.433 167 28.00 SG 37.9 0.36878 Pf 2.494 Total 6.8 113 27.00 2" Dyna Flow 74.8 Len 8.0 C =120 Pt 117) 14.389 2.2030 0 Ftg 0.0 Pe 0.000 117 27.00 BN 112.7 008601 Pf 0.688 Total 8.0 Total Pressure at Node 113) 15.077 psi 115 27.00 1' Dyna Thead 1.0800 T Len 1.0 Ftg 5.8 c = 120 Pt 165) 11.749 Pe 0.433 Pt 2.551 165 28.00 SG 38.4 0.37731 Total 6.8 111 27.00 2" Dyna Flow 111.4 2.2030 0 Len 8.0 Ftg 0.0 C= 120 Pt 115) 14.733 Pe 0.000 Pt 1.164 115 27.00 BN 149.8 0.14546 Total 8.0 Total Pressure at Node 111) 15.897 psi 114 27.00 1' Dyna Thead 1.0800 T Len 1.0 Ftg 5.8 C = 120 Pt 164) 11.811 Pe 0.433 Pf 2.564 164 28.00 SG 38.5 0.37915 Total 6.8 110 27.00 2" Dyna Flow 111.7 2.2030 0 Len 8.0 Ftg 0.0 = 120 Pt 114) 14.808 Pe 0.000 Pf 1.169 114 27.00 BN 150.2 1 0.14618 Total 8.0 Total Pressure at Node 110) 15.911 psi 0 Copyright 2013 Sigma Development Group, Inc. Page 6 of 11 Pipe Information G000FEET IN-RACKS From Elevi ft Pipe ID Flows Added GPM Inside Diameter Fittings Length ft I C Value I I Friction Loss psi/ft 1 Total (Pt) psi I Notes Fitting ft I Elev (Pe) psi I To Elev2 Type Total Total ft Frict (Pt) psi 113 27.00 1° Dyna Thead 1.0800 1 Len 1.0 Ftg 5.8 c = 120 Pt 163) 12.035 Pe 0.433 Pt 2,609 163 28.00 SG 38.9 0 38 . 580 Total 6.8 109 27.00 2" Dyna Flow 112.7 2.2030 0 Len 8.0 Ftg 0.0 c = 120 0.14875 Pt 113) 15.077 Pe 0.000 Pt 1.190 113 27.00 BN 151.6 Total 8.0 Total Pressure at Node 109) 16.267 psi 111 27.00 1' Dyna Thead 1.0800 1 Len 1.0 Ftg 5.8 c = 120 Pt 161) 12.718 Pe 0.433 Pf 2.746 161 28.00 SG 39.9 0.40603 Total 6.8 107 27.00 2" Dyna Flow 149.8 2.2030 0 Len 8.0 Ftg 0.0 C= 120 0.22526 Pt 111) 15.897 Pe 0.000 Pf 1.802 111 27.00 BN 189.7 Total 8.0 Total Pressure at Node 107) 17.699 psi 110 27.00 1' Dyna lhead 1.0800 T Len 1.0 Ftg 5.8 C= 120 0.40800 Pt 160) 12.785 Pe 0.433 Pt 2.759 160 28.00 SG 40.0 Total 6.8 106 27.00 2" Dyna Flow 150.2 2.2030 0 Len 8.0 Ftg 0.0 C= 120 Pt 110) 15.977 Pe 0.000 Pf 1.811 110 27.00 BN 190.2 022636 Total 8.0 Total Pressure at Node 106) 17.788 psi 109 27.00 1' Dyna lhead Len 1.0 C= 120 Pt 159) 13.027 1.0800 T Ftg 5.8 Pe 0.433 159 28.00 SG 40.4 0.41512 Pt 2.807 Total 6.8 105 27.00 F Dyna Flow 151.6 Len 8.0 C = 120 Pt 109) 16.267 2.2030 0 Ftg 0.0 Pe 0.000 109 27.00 BN 192.0 0.23034 Pf 1.843 Total 8.0 Total Pressure at Node 105) 18.109 psi 108 27.00 1" oynalhead Len 1.01 c = 120 Pt 158) 21.813 1.0800 T e 0.433 P 158 28.00 SG 52.3 0.66874 Pt 4.522 Total 6.81 Total Pressure at Node 108) 26.768 psi 107 27.00 1" Dyna Thead Len 1.0 Pt 157) 14.222 1.0800 T c 0.433 P 157 28.00 SG 42.2 0.45023 Pf 3.044 Total 6.8 0 Copyright 2013 Sigma Development Group, Inc. Page 7 of 11 8OO Pipe Information GOODFEET IN-RACKS From ft Elevi Pipe ID T Flows I Added Inside Length ftl I C Value I I Total (Pt) psi I I Fifting I Elev (Pe) psi ft GPM Diameter Fittings I Friction Loss psi/ft I Notes kict() psil To Elev2 Type Total Total ft[ 103 27.00 2' Dyna Flow 189.7 2.2030 0 Len 8.0J Ftg 0.0 C = 120 0.32673 Pt 107) 17.699 Pe 0.000 Pf 2.614 107 27.00 BN 232.0 Total 8.0 Total Pressure at Node 103) 20.313 psi 106 27.00 1" Dyna lhead 1.0800 T Len 1.0 Ftg 5.8 C= 120 Pt 156) 14.296 Pe 0.433 Pf 3.059 156 28.00 SO 42.3 0.45240 Total 6.8 102 27.00 2" Dyna Flow 190.2 2.2030 0 Len 8.0 Ftg 0.0 c = 120 Pt 106) 17.788 Pe 0.000 Pf 2.627 106 27.00 BN 232.6 0.32832 Total Pressure at Node 102) 20.414 psi 105 27.00 1" Dyna lhead 1.0800 1 Len 1.0 Ftg 5.8 c = 120 0.46025 Pt 155) 14.564 Pe 0.433 Pf 3.112 155 28.00 SO 42.7 Total 6.8 101 27.00 Dyna Flow 192.0 2.2030 0 Len 8.0 Ftg 0.0 C= 120 0.33407 Pt 105) 18.109 Pe 0.000 Pf 2.673 105 27.00 BN 234.8 Total 8.0 Total Pressure at Node 101) ZU.71 psi 1 104 27.00 1" Dyna Thead ILen i.o[ C=120 TPt154) 22.314 1.0800 1 Ftg 5.8 LH --- Pe 0.433 154 28.00 SG 52.9 0.68295 Pf 4.618 ITotal 6,8 Total Pressure at Node 104) 21.65 psi 103 27.00 Dyna lhead Len 0 1. C = 120 Pt 153) 16.405 1.0800 T Ftg 5.8 Pe 0.433 153 28.00 SO 45.4 0.51382 Pf 3.474 Total 6.8 18 27.00 2' Dyna Flow 232.0 Le 0n 6. C = 120 Pt 103) 20.313 2.2030 1 Ftg 13.6 Pe 0.000 103 27.00 BN 277.3 0.45468 Pf 8.929 13 26.00 Dyna Flow Len 1. 0 C = 120 Pt 18) 29.242 2.2030 T Ftg 13.6 Pe 0.433 18 27.00 NR 277.3 0.45468 Pf 6.656 Tot al 14.6 Total iressure at NOae iJ) ib.1 psi 102 27.00 1" Dynalhead Len 1.0 C = 120 Pt 152) 16.490 1 1.0800 T Pe 0.433 I 152 28.00 SG 45.5 0.51628 Pf 3.491 j Total 6.81 © Copyright 2013 Sigma Development Group, Inc. Page 8 of 11 UJOO OashbdHydiuIk Pipe Information GOODFEET IN-RACKS From Elevi ft Pipe ID Flows J Added Inside Length ft C Value I [Total (Pt) psi I GPM Diameter in Fittings Fitting ft Friction Loss [ psi/ft I Elev (Pe) psi I Notes I Frict (Pt) psi To E ft v2 Type 1 Total Total ft 17 27.00 2" Dyna Flow 232.6 2.2030 1 Len 6.0 Ftg 13.6 c = 120 Pt 102) 20.414 Pe 0.000 Pf 8.973 102 27.00 BN 278.1 0.45689 Total 19.6 12 26.00 2 Dyna Flow 2.2030 1 Len 1.0 Ftg 13.6 = 120 Pt 17) 29.387 Pe 0.433 Pf 6.688 Total 14.6 17 27.00 NR 278.1 0.45689 Total Pressure at Node 12) 36.508 psi 101 27.00 1' Dyna lhead 1.0800 T Len 1.0 Ftg 5.8 c = 120 Pt 151) 16.798 Pe 0.433 Pt 3.551 151 28.00 SG 45.9 0.52518 Total 6.8 16 27.00 2" Dyna Flow 234.8 2.2030 1 Len 6.0 Ftg 13.6 C= 120 Pt 101) 20.782 Pe 0.000 Pt 9.129 101 27.00 BN 280.7 0.46487 11 26.00 2" Dyna Flow 2.2030 1 Len 1.0 Ftg 13.6 c = 120 Pt 16) 29.911 Pe 0.433 Pf 6.805 16 27.00 NR 280.7 0.46487 Total 14.6 Total Pressure at Node 11) 37.149 psi 100 27.00 Dyna Thead ILen 1.01 C= 120 Pt 150) 23.385 1.0800 1 Ftg 5.8 Pe 0.433 150 28.00 SG 54.2 0.71320 Pf 4.823 fT 6.81 Total Pressure at Node 100) 28.640 psi 108 27.00 Dyna Flow 2.2030 0 Len 8.0 Ftg 0.0 C = 120 Pt 112) 26.603 Pe 0.000 Pt 0.165 112 27.00 BN 52.1 0.02065 Total 8.0 104 27.00 2' Dyna Flow 52.3 2.2030 0 Len 8.0 Ftg 0.0 C = 120 Pt 108) 26.768 Pe 0.000 Pf 0.597 108 27.00 BN 104.5 0.07468 Total 8.0 100 27.00 2" Dyna Flow 52.9 2.2030 0 Len 8.0 Ftg 0.0 C 120 Pt 104) 27.365 Pe 0.000 Pf 1.275 104 27.00 BN 157.4 0.15938 Total 8.0 15 27.00 2" Dyna Flow 54.2 2.2030 1 Len 6.0 Ftg 13.6 C = 120 Pt 100) 28.640 Pe 0.000 Pt 5.410 100 27.00 BN 211.5 0.27547 Total 19.6 10 26.00 2" Dyna Flow 2.2030 T 0 Len 1.0 Ftg 13.6 = 120 Pt 15) 34.050 Pe 0.433 Pt 4.033 15 27.00 NR 211.5 0.27547 Total 14.6 © Copyright 2013 Sigma Development Group, Inc. Page 9 of 11 AMM 'g-8OO Da Pipe Information shboaru'Hyd, uIics GOODFEET IN-RACKS From Elevi ft Pipe ID Flows Added Inside I Length ft c Value I I Total (Pt) )Sl I Fitting ft I I Elev (Pe) psi I GPM Diameter in I Fittings I Friction Loss [ psi/ft Notes To Elev2 ft Type Total 1Total ft [Frict (Pt) psi Total Pressure at Node 10) 38.516 psi 43 26.00 2W' Dyna Flow 2.7030 T,2E Len 15.0 Ftg 37.3 C = 120 0.10983 Pt 44) 38.066 Pe -6.495 Pt 5.744 44 11.00 FM 220.5 Total 52.3 42 26.00 2W Dyna Flow 2.7030 T Len 82.0 Ftg 18.7 c = 120 0.10983 Pt 43) 37.315 Pe 0.000 Pt 11.055 43 26.00 FM 220.5 Total 100.7 41 26.00 3" Dyna Flow 3.3140 E Len 16.0 Ftg 10.2 C= 120 0.04071 Pt 42) 48.370 Pe 0.000 Pt 1.066 42 26.00 FM 220.5 Total 26.2 40 7.00 3" Dyna Flow 3.3140 T,BV!E Len 20.0 Ftg 46.6 C = 120 Pt 41) 49.437 Pe 8.227 Pf 2.711 41 26.00 FR 220.5 0.04071 Total 66.6 Total Pressure at Node 40) 60.374 psi 12 26.00 4" Dyna Flow 4.3100 0 Len 10.3 Ftg 0.0 C = 120 Pt 13) 36.331 Pe 0.000 Pf 0.177 13 26.00 FM 277.3 0.01731 Total 10.3 11 26.00 4" Dyna Flow 278.1 4.3100 0 Len 10.3 Ftg 0.0 C= 120 0.06255 Pt 12) 36.508 Pe 0.000 Pt 0.641 12 26.00 FM 555.4 Total 10.3 10 26.00 4" Dyna Flow 280.7 4.3100 0 Len 10.3 Ftg 0.0 C= 120 0.13331 Pt 11) 37.149 Pe 0.000 Pt 1.366 11 26.00 FM 836.0 Total 10.3 3 26.00 4" Dyna Flow 211.5 4.3100 0 Len 54.0 Ftg 0.0 C= 120 Pt 10) 38.516 Pe 0.000 Pt 10.926 10 26.00 FM 1,047.6 0.20234 Total 54.0 2 26.00 6' Sch 10 6.3570 1 Len 32.0 Ftg 377 C 120 0.03049 Pt 3) 49.442 Pe 0.000 Pt 2.126 3 26.00 FM 1,047.6 Total 69.7 40 7.00 6" Sch 10 6.3570 Len 19.0 Ftg 0.0 c = 120 Pt 2) 51.568 Pe 8.227 Pf 0.579 2 26.00 FR 1,047.6 0.03049 Total 19.0 1 0.00 6" Sch 10 220.5 6.3570 E Len 7.0 Ftg 17.6 C = 120 Pt 40) 60.374 Pe 3.031 Pf 1.068 40 7.00 FR 1,268.0 0.04341 Total 24.6 © Copyright 2013 Sigma Development Group, Inc. Page 10 of 11 A M 6* Pipe Information Da 138go GOODFEET IN-RACKS From ft Pipe ID Flows Added I Inside ILength C Value Tiothi (Pt) SI GPM I Diameter in Fittings Fitting Friction LossElev psi/ft (Pe) psi Notes jF (P Psi To Elev2 Type Tothi_ Total ft 0 0.00 6" PVC ci.ioo I Len 80 .0 1 c 150 1 pt 1) 64.474 DDC WILKINS 350 DA DOUBLE DETECTOR CHECK 58600 2E/DDC 0.000 6" WILKINS DOUBLE DET. ITotal 154.1 1 0.00 UN 1,268.0 0.042711pf 6.580 CHECK: Loss 7.28 Total Pressure at Node 0) 78.334 psi 0 Copyright 2013 Sigma Development Group, Inc. Page 11 of 11 A r' I A Contractor's Material and Test Certificate for Aboveground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the contractor's representative and witnessed by an owner's representative. Alf defects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices .any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. Property name ... gzi Date 1:2.1 Property addres I Accepted by approving authorities (names) -.-3t f Address .1 Plans . . Installation conforms to accepted plans . tR Yes ED No Equipment used Is approved . . A . l Yes E No If no, explain deviations Has person in charge of fire equiphient been instructed as Yes No to location of control valves and care and maintenance of this new equipment? If no, explain? Instructions . . Have copies of the following been left on the premises? Yes E No 1. System components instructions . EJ Yes No Care and maintenance instructions ES Yes E No NFPA25 . Yes D No Location of system Supplies buildings Year of Orifice Temperature Make Model manufacture size Quantity rating • ./3o2 2.oL . t5 • Sprinklers • Pipe and Type of pipe P'1'JA 1_O1.A) fittings Type of fittings . Alarm Valve or flow Indicator Alarm device . . Maximum time to operate through test connection Type Make Model Minutes Seconds SU 'OTTe.12.. (4.)D z Dry valve 0 • Model - 0. o. D. Make Serial no. Model rlalno, ., Make 'Dry pipe operating test to through test connection1 . ---Aater press re-., .. Air pressure __irip air pressure e water 're :c test outlet1 Alarm properly Operation E Electric I E Hydraulics -,Piping supervised Yes E No I Detecting media supervised es No boea4vperate from the manual trip, remote, or both Yes E No control statio1s?.. Deluge and preactlon valves Is there an accessibllIHtUeach circuit for testing? EYes_ENb- no, explain I Does each circuipps Does each circuit operate Maximum time to Make Model supervisio s alarm? valve release? operate release No No Minutes Seconds 1 Location ake and Setting Static pressure ResIdu Flow rate Pressure or model (flowing)-.... al e4at Inlet (PSI) Outlet (PSI) Inlet (PSI) outlet (PSI) Fiogpm) Hydrostatic: Hydrostatic tests shall be made at not lessthan 200 psi (13.6 bar) for 2 hours or 50 psI (3.4 bar) above static pressure in excess of 150 psI (10.2 bar) for 2 hours. Differential dry-pipe valve clappers shall be left Test open during the test to prevent damage. All aboveground piping leakage shall be stopped. description Ppeumatic: Establish 40 psi (2.7 bar) air pressure and measure drop, which shall not exceed 11h ps,i (0.1 bar) In 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop, which shall not exceed 11h psi (0.1 bar) in 24 hours. All piping hydrostatically tested at'00 psi (_ bar) for ... hours If no, state reason Dry piping pneumatically tested E Yes F7 No Equipment operates properly E Yes E No Do you certify as the sprinkler contractor that additives and corrosive chemicals, sodium silicate or derivatives of sodium silicate, brine, or other corrosive chemicals were not used for testing systems or stopping leaks? Yes r7 No Tests Drain test Reading of gauge located near water supply test connection: t I ( psi (_bar) Residual pressure with valve in test connection open wide: psi (_bar) Underground mains and lead in connections to system risers flushed before connection made to sprinkler piping Verified by copy of the U Form No. 85B E Yes E No Other Explain flushed by Installer of underground ( sprinkler piping E Yes E No If powder-driven fasteners are used in concrete, has E Yes E No If no, explain representative sample testing be satisfactorily completed? R/4. Blank testing gaskets Number used Locations. Number removed Welding piping E Yes &Cr No If yes..... Do you certify as the sprinkler contractor that welding procedures comply / E Yes No with the requirements of at least AWS B21? %' ( WeldingDo you certify that the welding was performed by welders qualified in E Yes E No compliance with the requirements of at least AWS B2..1? Do you certify that the welding was carried out in compliance with a documented E Yes E No quality control procedure to ensure that all discs are retrieved, that openings In piping are smooth, that slag and other welding residue are removed, and that the Internal diameters of piping are not penetrated? Cutouts (discs) Do you certify that you have a control feature to ensure that Yes E No all cutouts (discs) are retrieved? Hydraulic Nameplate provided If no, explain data nameplate Yes E No Date left In service with all control valves open Remarks Name of sprinkler contractor Tests witnessed by Signatures For property owner (signed) Title (-q or sprinkler c ctor (signed Title j Additional explanatiork and notes Date Date