HomeMy WebLinkAbout6163 EL CAMINO REAL; ; AS1201477/10/24, 11:52 AM A8120147 Permit Data
City of Carlsbad
Sprinkler Permit
Permit No: AS120147
6163 EL CAM INO
Job Address: Status: APPROVED
REAL
Permit Type: SPRINK Applied 11/14/2012
Parcel No: 2131002100 Approved: 12/2/2012
Lot #: 0
Reference No.: Issued: 12/2/2012
PC #: Inspector:
Project Title: VIASAT CAFETERIA NEW 13 AUTO- SPRINK SYSTEM
Applicant:
PARAMOUNT FIRE SYSTEMS, INC.
P.O. BOX 713194
SANTEE, CA
619-562-6247
Owner:
LEVINE INVESTMENTS LIMITED
PARTNERSHIP
1702 E HIGHLAND AVE #310
PHOENIX AZ
Fees ($) Add'l Fees ($) Total ($) Balance ($)
1,445 1 0 1,445 0
about:blank 1/1
IS
F ~ L E, C 0 P', A S 12-0 ) 44-
PARAMOUNT FIRE SYSTEMS, INC.
8069 WING AVENUE
EL CAJON, CA 92020
LICENSE #C16-788204
HYDRAULIC CALCULATIONS FOR
VIA SAT CAFETERIA BUILDING
6155 EL CAMINO REAL
CARLSBAD, CA 92009
KITCHEN, REMOTE AREA 1
have been reviewed toi' InparenI CL1I1IpIItllce
s itli ho iiive,it applicable ctxIe tad sItllilalds in Orce
Ikltttfl lht i)ii tel 1)1 Coll lraerl)r lilac utilize
Ii st011 of all I[)plleIlloll 11w a I)llildl((IL
II he espless ulldcvst llC thai this teStIly
II' el Ses the OSVILCI ((I CI'itactol Iii (lieu
nrat etietneer or architect or sole rcspottsihiltiv
LIII L_I)IIIpI(LIICC with said codes and standards.
IrlIllilhlllli (ItC hlltichllli) C(I(IC Ill hot ally rCspotlslhthty for
IletierelIcleS CItlitS i)lliI5SIIill5 Ill tteiihtaettce ill these
1(115 wltethiet UI lot limed Ill this review.
(ire: #19114 Res iewer:'
RFCOMMENI) APPROVAL
RECOblhlhiNl) APPROVAL. AS NOTED
FILE NUMBER: VIA SAT CAFETERIA AREA 1.SDF
DATE: 11/5/2012
-DESIGN DATA-
OCCUPANCY CLASSIFICATION: ORDINARY HAZARD GRP. I
DENSITY:
AREA OF APPLICATION:
NUMBER OF SPRINKLERS CALCULATED:
TOTAL SPRINKLER WATER FLOW REQUIRED:
.15 gpm/sq. ft.
1500 sq. ft.
17 sprinklers
(130 SF max per sprinkler)
408.9 gpm
TOTAL WATER REQUIRED (including hose): 658.9 gpm
(250 gpm Hose Allow)
FLOW AND PRESSURE (@ NODE BOR): 408.9 gpm @ 81.6 psi
SPRINKLER K-FACTOR (ORIFICE SIZE):
DESIGN/LAYOUT BY: PARAMOUNT FIRE SYSTEMS
AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT
WATER FLOW AVAILABILITY DATA: STATIC: 110.0 psi (99.0 @ 90%)
RESIDUAL: 105.0 psi (94.5 8 90%)
FLOW: 1177 gpm
SOURCE: EXISTING FIRE FLOW
TEST; 3/9/2005
WESTERN FIRE PROTECTION
AS SJBilTTD
F'ILE U
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1
DATE: 11/5/2012 C:\HASS DATA\VIA SAT CAFETERIA AREA 1.SDF
JOB TITLE: VIA SAT CAFETERIA BUILDING, KITCHEN AREA 1
WATER SUPPLY DATA
SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D
NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS.
TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI)
SRC 99.0 94.5 1177.0 97.5 658.9 93.7
AGGREGATE FLOW ANALYSIS:
TOTAL FLOW AT SOURCE 658.9 GPM
TOTAL HOSE STREAM ALLOWANCE AT SOURCE 150.0 GPM
OTHER HOSE STREAM ALLOWANCES 100.0 GPM
TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 408.9 GPM
NODE ANALYSIS DATA
NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE
(FT) (PSI) (GPM)
SRC -2.0 SOURCE 93.7 508.9
UG1 -2.0 - - - - 93.5 - - -
DPi -2.0 - - - - 93.2 - - -
DCIN 3.0 - - - - 91.0 - - -
DCOUT 3.0 - - - - 83.0
DP2 -2.0 - - - - 85.1 - - -
POC -2.0 - - - - 84.9 - - -
UG2 -2.0 - - - - 84.0 - - -
STL -2.0 - - - - 83.0 - - -
BOR 1.0 HOSE STREAM 81.6 100.0
3" 2.0 - - - - 79.2 - - -
TOR 15.8 - - - - 70.2 - -
1 15.8 - - - - 60.9 - - -
2 15.8 - - - - 41.7 - - -
3 15.8 - - - - 33.8 - - -
4 15.8 - - - - 31.1 - - -
5 15.8 - - - - 30.5 - -
6 15.8 - - - - 29.9 - - -
7 15.8 - - - - 29.9 - - -
8 15.8 - - - - 29.7 - - -
9 15.8 - - - - 30.5 - - -
10 15.8 - - - - 21.2 - - -
1.1 15.8 - - - - 22.1 - - -
1.2 15.8 - - -- 20.5 - - -
1.5 15.8 - - - - 22.1 - - -
1.6 15.8 - - - - 15.2 - - -
1.7 15.8 - - - - 13.7 - - -
1.8 15.8 - - - - 12.1 - - -
1.11 15.8 - - - - 22.6 - - -
1.13 16.3 - - - - 21.2 - - -
1.14 16.3 - - - - 15.2 - - -
1.15 16.3 - - - - 13.2 - - -
1.16 16.3 - - - - 12.5 - - -
101 10.2 K= 5.60 22.1 26.3
102 12.0 K= 5.60 20.6 25.4
103 12.0 K= 5.60 19.8 24.9
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2
DATE: 11/5/2012 C:\HASS DATA\VIA SAT CAFETERIA AREA 1.SDF
JOB TITLE: VIA SAT CAFETERIA BUILDING, KITCHEN AREA 1
NODE ANALYSIS DATA
NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE
(FT) (PSI) (GPM)
104 9.0 K= 5.60 30.1 30.7
105 8.0 K= 5.60 22.4 26.5
106 10.2 K= 5.60 15.3 21.9
107 12.0 K= 5.60 13.9 20.9
108 8.8 K= 5.60 12.8 20.0
109 12.0 K= 5.60 12.1 19.5
110 9.0 K= 5.60 29.0 30.2
111 9.0 K= 5.60 22.6 26.6
112 10.8 K= 5.60 21.5 26.0
113 9.0 K= 5.60 22.0 26.3
114 10.8 K= 5.60 15.7 22.2
115 10.2 K= 5.60 14.1 21.1
116 12.0 K= 5.60 13.3 20.4
117 12.0 K= 5.60 12.8 20.0
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3
DATE: 11/5/2012 C:\HASS DATA\VIA SAT CAFETERIA AREA 1.SDF
JOB TITLE: VIA SAT CAFETERIA BUILDING, KITCHEN AREA 1
PIPE DATA
PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.
END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.
NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)
Pipe: 1 508.9 7.980 PL 67.00 PF 0.2
SRC -2.0 SRCE 93.7 (N/A) 3.3 150 FTG T PE 0.0
UG1 -2.0 0.0 93.5 0.0 0.002 TL 126.00 PV
Pipe: 2 508.9 7.980 PL 95.00 PF 0.3
UG1 -2.0 0.0 93.5 0.0 3.3 150 FTG TL PE 0.0
DPi -2.0 0.0 93.2 0.0 0.002 TL 176.00 PV
Pipe: 3 508.9 8.510 PL 5.00 PF 0.0
DPi -2.0 0.0 93.2 0.0 2.9 140 FTG L PE -2.2
DCIN 3.0 0.0 91.0 0.0 0.001 TL 27.00 PV
Pipe: 4 FIXED PRESSURE LOSS DEVICE
DCIN 3.0 0.0 91.0 0.0 8.0 psi, 508.9 gpm
DCOUT 3.0 0.0 83.0 0.0
Pipe: 5 508.9 8.510 PL 5.00 PF 0.1
DCOUT 3.0 0.0 83.0 0.0 2.9 140 FTG T PE 2.2
DP2 -2.0 0.0 85.1 0.0 0.001 TL 64.00 PV
Pipe: 6 508.9 7.980 PL 75.00 PF 0.2
DP2 -2.0 0.0 85.1 0.0 3.3 150 FTG L PE 0.0
POC -2.0 0.0 84.9 0.0 0.002 TL 97.00 PV
Pipe: 7 508.9 6.080 PL 64.00 PF 0.9
POC -2.0 0.0 84.9 0.0 5.6 150 FTG TLG PE 0.0
UG2 -2.0 0.0 84.0 0.0 0.007 TL 130.00 PV
Pipe: 8 508.9 6.080 PL 127.00 PF 1.0
UG2 -2.0 0.0 84.0 0.0 5.6 150 FTG 2L PE 0.0
STL -2.0 0.0 83.0 0.0 0.007 TL 155.00 PV
Pipe: 9 508.9 6.357 PL 10.00 PF 0.2
STL -2.0 0.0 83.0 0.0 5.1 120 FTG L PE -1.3
BOR 1.0 H.S. 81.6 100.0 0.008 TL 21.00 PV
Pipe: 10 408.9 3.260 PL 3.67 PF 1.9
BOR 1.0 H.S. 81.6 100.0 15.7 120 FTG 2L PE -0.4 311 2.0 0.0 79.2 0.0 0.138 TL 13.67 PV
Pipe: 11 408.9 3.314 PL 13.75 PF 3.0
3" 2.0 0.0 79.2 0.0 15.2 120 FTG B PE -6.0
TOR 15.8 0.0 70.2 0.0 0.128 TL 23.75 PV
Pipe: 12 408.9 2.703 PL 19.00 PF 9.3
TOR 15.8 0.0 70.2 0.0 22.9 120 FTG 2L PE 0.0
1 15.8 0.0 60.9 0.0 0.344 TL 27.00 PV
Pipe: 13 408.9 2.703 PL 43.75 PF 19.2
1 15.8 0.0 60.9 0.0 22.9 120 FTG T PE 0.0
2 15.8 0.0 41.7 0.0 0.344 TL 55.75 PV
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4
DATE: 11/5/2012 C:\HASS DATA\VIA SAT CAFETERIA AREA 1.SDF
JOB TITLE: VIA SAT CAFETERIA BUILDING, KITCHEN AREA 1
PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.
END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.
NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)
Pipe: 14 408.9 2.703 FL 19.17 PF 8.0
2 15.8 0.0 41.7 0.0 22.9 120 FTG L FE 0.0
3 15.8 0.0 33.8 0.0 0.344 TL 23.17 PV
Pipe: 15 332.2 2.703 FL 11.38 PF 2.7
3 15.8 0.0 33.8 0.0 18.6 120 FTG ---- FE 0.0
4 15.8 0.0 31.1 0.0 0.235 TL 11.38 PV
Pipe: 16 301.5 2.703 PL 2.92 PF 0.6
4 15.8 0.0 31.1 0.0 16.9 120 FTG ---- PE 0.0
5 15.8 0.0 30.5 0.0 0.196 TL 2.92 PV
Pipe: 17 192.7 2.703 PL 7.08 PF 0.6
5 15.8 0.0 30.5 0.0 10.8 120 FTG ---- PE 0.0
6 15.8 0.0 29.9 0.0 0.086 TL 7.08 PV
Pipe: 18 162.5 2.703 FL 0.29 PF 0.0
6 15.8 0.0 29.9 0.0 9.1 120 FTG ---- FE 0.0
7 15.8 0.0 29.9 0.0 0.062 TL 0.29 PV
Pipe: 19 109.9 2.703 FL 5.88 PF 0.2
7 15.8 0.0 29.9 0.0 6.1 120 FTG ---- PE 0.0
8 15.8 0.0 29.7 0.0 0.030 TL 5.88 PV
Pipe: 20 76.7 1.639 FL 10.50 PF 3.3
3 15.8 0.0 33.8 0.0 11.7 120 FTG T FE 0.0
9 15.8 0.0 30.5 0.0 0.178 TL 18.50 PV
Pipe: 21 76.7 1.408 PL 16.42 PF 8.4
9 15.8 0.0 30.5 0.0 15.8 120 FTG 2E FE 0.0
1.1 15.8 0.0 22.1 0.0 0.373 TL 22.42 PV
Pipe: 22 50.4 1.408 FL 5.25 PF 0.9
1.1 15.8 0.0 22.1 0.0 10.4 120 FTG ---- FE 0.0
10 15.8 0.0 21.2 0.0 0.171 TL 5.25 PV
Pipe: 23 50.4 1.080 FL 1.08 PF 0.7
10 15.8 0.0 21.2 0.0 17.6 120 FTG FE 0.0
1.2 15.8 0.0 20.5 0.0 0.624 TL 1.08 PV
Pipe: 24 26.3 1.080 FL 6.00 PF 2.4
1.1 15.8 0.0 22.1 0.0 9.2 120 FTG ET FE 2.4
101 10.2 5.6 22.1 26.3 0.187 TL 13.00 PV
Pipe: 25 25.4 1.080 FL 3.75 PF 1.5
1.2 15.8 0.0 20.5 0.0 8.9 120 FTG T PE 1.6
102 12.0 5.6 20.6 25.4 0.176 TL 8.75 PV
Pipe: 26 24.9 1.080 FL 11.75 PF 2.3
1.2 15.8 0.0 20.5 0.0 8.7 120 FTG E FE 1.6
103 12.0 5.6 19.8 24.9 0.170 TL 13.75 PV
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5
DATE: 11/5/2012 C:\HASS DATA\VIA SAT CAFETERIA AREA 1.SDF
JOB TITLE: VIA SAT CAFETERIA BUILDING, KITCHEN AREA 1
PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.
END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.
NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)
Pipe: 27 30.7 1.080 PL 8.88 PF 4.0
4 15.8 0.0 31.1 0.0 10.8 120 FTG ET FE 2.9
104 9.0 5.6 30.1 30.7 0.250 TL 15.88 PV
Pipe: 28 108.8 1.408 FL 5.88 PF 8.5
5 15.8 0.0 30.5 0.0 22.4 120 FTG T PE 0.0
1.5 15.8 0.0 22.1 0.0 0.713 TL 11.88 PV
Pipe: 29 82.3 1.408 PL 16.08 PP 6.8
1.5 15.8 0.0 22.1 0.0 17.0 120 FTG ---- PE 0.0
1.6 15.8 0.0 15.2 0.0 0.425 TL 16.08 PV
Pipe: 30 60.4 1.408 PL 6.33 PP 1.5
1.6 15.8 0.0 15.2 0.0 12.4 120 FTG ---- PE 0.0
1.7 15.8 0.0 13.7 0.0 0.240 TL 6.33 PV
Pipe: 31 39.5 1.080 FL 4.08 PF 1.6
1.7 15.8 0.0 13.7 0.0 13.8 120 FTG ---- PE 0.0
1.8 15.8 0.0 12.1 0.0 0.398 TL 4.08 PV
Pipe: 32 26.5 1.080 FL 8.75 PF 3.0
1.5 15.8 0.0 22.1 0.0 9.3 120 FTG ET PE 3.4
105 8.0 5.6 22.4 26.5 0.190 TL 15.75 PV
Pipe: 33 21.9 1.080 PL 7.00 PF 2.3
1.6 15.8 0.0 15.2 0.0 7.7 120 FTG 2T FE 2.4
106 10.2 5.6 15.3 21.9 0.134 TL 17.00 PV
Pipe: 34 20.9 1.080 PL 4.75 PF 1.4
1.7 15.8 0.0 13.7 0.0 7.3 120 FTG ET PS 1.6
107 12.0 5.6 13.9 20.9 / 0.122 TL 11.75 PV
Pipe: 35 20.0 1.080 PL 11.00 PP 2.4
1.8 15.8 0.0 12.1 0.0 7.0 120 FTG 2T FE 3.0
108 8.8 5.6 12.8 20.0 0.113 TL 21.00 PV
Pipe: 36 19.5 1.080 PL 8.75 PF 1.6
1.8 15.8 0.0 12.1 0.0 6.8 120 FTG 3E PE 1.6
109 12.0 5.6 12.1 19.5 0.108 TL 14.75 PV
Pipe: 37 30.2 1.080 PL 8.88 PP 3.8
6 15.8 0.0 29.9 0.0 10.6 120 FTG ET PE 2.9
110 9.0 5.6 29.0 30.2 0.241 TL 15.88 PV
Pipe: 38 52.6 1.080 FL 5.88 PF 7.3
7 15.8 0.0 29.9 0.0 18.4 120 FTG T PE 0.0
1.11 15.8 0.0 22.6 0.0 0.675 TL 10.88 PV
Pipe: 39 26.6 1.080 PL 8.00 PP 2.9
1.11 15.8 0.0 22.6 0.0 9.3 120 FTG ET PE 2.9
111 9.0 5.6 22.6 26.6 0.192 TL 15.00 PV
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6
DATE: 11/5/2012 C:\HASS DATA\VIA SAT CAFETERIA AREA 1.SDF
JOB TITLE: VIA SAT CAFETERIA BUILDING, KITCHEN AREA 1
PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS.
END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM.
NODES (FT) (K) (PSI) (GPM) FL/FT (PSI)
Pipe: 40 26.0 1.080 PL 12.50 PF 3.2
1.11 15.8 0.0 22.6 0.0 9.1 120 FTG T PE 2.1
112 10.8 5.6 21.5 26.0 0.183 TL 17.50 PV
Pipe: 41 109.9 1.408 PL 2.46 PF 8.3
8 15.8 0.0 29.7 0.0 22.7 120 FTG ET PE -0.3
1.13 16.3 0.0 21.2 0.0 0.726 TL 11.46 PV
Pipe: 42 83.7 1.408 PL 13.50 PF 5.9
1.13 16.3 0.0 21.2 0.0 17.2 120 FTG ---- PE 0.0
1.14 16.3 0.0 15.2 0.0 0.438 TL 13.50 PV
Pipe: 43 61.5 1.408 PL 8.25 FE' 2.0
1.14 16.3 0.0 15.2 0.0 12.7 120 FTG ---- PE 0.0
1.15 16.3 0.0 13.2 0.0 0.248 TL 8.25 PV
Pipe: 44 40.4 1.408 PL 6.33 PF 0.7
1.15 16.3 0.0 13.2 0.0 8.3 120 FTG ---- PE 0.0
1.16 16.3 0.0 12.5 0.0 0.114 TL 6.33 PV
Pipe: 45 20.0 1.080 PL 11.75 PF 1.6
1.16 16.3 0.0 12.5 0.0 7.0 120 FTG E FE 1.9
117 12.0 5.6 12.8 20.0 0.113 TL 13.75 PV
Pipe: 46 26.3 1.080 PL 7.33 PF 2.3
1.13 16.3 0.0 21.2 0.0 9.2 120 FTG T PE 3.2
113 9.0 5.6 22.0 26.3 0.187 TL 12.33 PV
Pipe: 47 22.2 1.080 FL 7.00 FE' 1.9
1.14 16.3 0.0 15.2 0.0 7.8 120 FTG ET PE 2.4
114 10.8 5.6 15.7 22.2 0.137 TL 14.00 PV
Pipe: 48 21.1 1.080 FL 6.58 PF 1.7
1.15 16.3 0.0 13.2 0.0 7.4 120 FTG ET PE 2.6
115 10.2 5.6 14.1 21.1 0.124 TL 13.58 PV
Pipe: 49 20.4 1.080 FL 4.33 PF 1.1
1.16 16.3 0.0 12.5 0.0 7.1 120 FTG T PE 1.9
116 12.0 5.6 13.3 20.4 0.117 TL 9.33 PV
NOTES (HASS)
Calculations were performed by the HASS 7.9 computer program
under license no. 16080621 granted by
MRS Systems, Inc.
4792 LaVista Road
Tucker, GA 30084
The system has been calculated to provide an average
imbalance at each node of 0.001 gpm and a maximum
imbalance at any node of 0.058 gpm.
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7
DATE: 11/5/2012 C:\HASS DATA\VIA SAT CAFETERIA AREA 1.SDF
JOB TITLE: VIA SAT CAFETERIA BUILDING, KITCHEN AREA 1
Total pressure at each node is used in balancing the system.
Maximum water velocity is 22.9 ft/sec at pipe 12.
PIPE FITTINGS TABLE
Pipe Table Name: STANDARD.PIP
PAGE: B MATERIAL: S10 HWC: 120
Diameter Equivalent Fitting Lengths in Feet
(in) E T L C B G A D N
Eli Tee LngEil ChkVlv BfyVlv GatVlv AlmChk DPViv NPTee
3.260 7.00 15.00 5.00 16.00 10.00 1.00 13.00 18.00 20.00
6.357 18.00 38.00 11.00 40.00 10.00 3.00 35.00 35.00 38.00
PAGE: C MATERIAL: Dynaf 1 HWC: 120
Diameter Equivalent Fitting Lengths in Feet
(in) E T L C B G A D N
Eli Tee LngEli ChkVlv BfyVlv GatVlv AlmChk DPViv NPTee
2.703 6.00 12.00 4.00 14.00 7.00 1.00 10.00 13.00 15.00
3.314 7.00 15.00 5.00 16.00 10.00 1.00 13.00 16.00 19.00
PAGE: D MATERIAL: DIRON HWC: 140
Diameter Equivalent Fitting Lengths in Feet
(in) E T L C B G N
Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee
8.510 31.00 59.00 22.00 76.00 20.00 7.00 59.00
PAGE: E MATERIAL: PVC150 HWC: 150
Diameter Equivalent Fitting Lengths in Feet
(in) E T L C B G N
Eli Tee LngEli ChkVlv BfyVlv GatVlv NPTee
6.080 22.00 47.00 14.00 51.00 16.00 5.00 47.00
7.980 31.00 59.00 22.00 76.00 20.00 7.00 59.00
PAGE: G MATERIAL: Dynath HWC: 120
Diameter Equivalent Fitting Lengths in Feet
(in) E T L C B G A D N
Eli Tee LngEii ChkVlv BfyVlv Gatviv
1.080 2.00 5.00 2.00 5.00 6.00 1.00 0.00 0.00 0.00
1.408 3.00 6.00 2.00 7.00 6.00 1.00 0.00 0.00 0.00
1.639 4.00 8.00 2.00 9.00 6.00 1.00 0.00 0.00 0.00
120.0
100.0
G
A
U
G
E 80.0
1
2
WATER SUPPLY ANALYSIS
Static: 99.00 psi Resid: 94.50 psi Flow: 1177.0 gpm
LEGEND
Available pressure
97.46 psi @ 658.9 gpm
Required pressure
2 93.73psi 8 658.9 gpm
Source Supply Curve
System Demand Curve
P
R
E
S
S 60.0
U
R
E
40.0
p
S
i
20.0
0.0
-14.71 I I I I I I I
4UU 600 800 1000 1200 1400 1600 1800 2000
FLOW (GPM)
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9
DATE: 11/5/2012 C:\HASS DATA\VIA SAT CAFETERIA AREA 1.SDF
JOB TITLE: VIA SAT CAFETERIA BUILDING, KITCHEN AREA 1
WATER SUPPLY CURVE
108+
99*\\\\\\\\\\\
I 0 \\\\\\\\\\\\
I X * <-94.5 psi @ 1177 gpm
Flow Test Point
90+
81+
P 72+
R I
E I
S I
S 63+
U I
R I
E I
54+
P I
S I
I 45+
36+
27+
18+ LEGEND
I I,
I X = Required Water Supply
I 93.73 psi 8 658.9 gpm
9+
I 0 = Available Water Supply "
I 97.46 psi 8 658.9 gpm
0++_+___+____+-----+ ------+ --------+ --------+ ---------+ -----------+
400 600 800 1000 1200 1400 1600 1800 2000
FLOW (GPM)
APPLICATION
Designed for installation on potable water fire protection
lines to protect against both backsiphonage and
backpressure of polluted water into the potable water sup-
ply. Assembly shall provide protection where a potential
. health hazard does not exist
STANDARDS COMPLIANCE
ASSEO Listed 1048 (Horizontal and Vertical Flow-Up)
FEATURES AWVA Compliant C510 (Horizontal & Vertical Flow-Up)
Sizes: U 21/2" U 3" U 8" U 10" UL® Classified (Horizontal)
C-UL@ Classified (Horizontal)
Maximum working water pressure 175 PSI CSA® Certified (Horizontal and Vertical Flow-Up) Maximum working water temperature 140°F FM Approved (Horizontal and Vertical Flow-Up) Hydrostatic test pressure 350 PSI
End connections Flanged ANSI B16.1 Approved by the Foundation for Cross Connection
Class 125 Control and Hydraulic Research at the University of
Southern California (Horizontal and Vertical Flow-Up,
OPTIONS except 10" vertical)
(Suffixes can be combined) MATERIALS
Main valve body Cast Iron ASTM A126 Class B
U - with OS & V gate valves (standard) Access covers Cast Iron ASTM A126 Class B
U G - with groove end OS&Y gate valves Coatings FDAApproved Epoxy finish
U L - less shut-off valves Internals Stainless Steel, 300 Series
U LM - less water meter Cast Bronze ASTM B 584
U - with remote reading meter Elastomers EPDM (FDA approved)
U - with gpm meter (standard) Buna Nitrile (FDA approved)
U - with cu ft/min meter Polymers DelrinTM, NSF Listed
Springs Stainless steel, 300 series
ACCESSORIES
U Repair kit (rubber only)
U Thermal expansion tank (Model WXTP)
U Gate valve tamper switch (OSY-40)
DIMENSIONS & WEIGHTS (do not include pkg.)
B
A
DIMENSIONS (approximate) WEIGHT
MODEL B E E WITHOUT WITH OS&Y
A WITHOUTSiZE C D OS&Y GATE OS&Y F GATE GATE GATE VALVES GATE VALVES VALVES VALVES OPEN VALVES
in. lmm in. lmm in. !mm in. lmm in. I mm in. lmm in. 'mm in. 'mm I lbs.! kg ibs.! kg
2 1/21 65 1 37 1/81 943 22 I559 1 4 1102 10 I 254 163/8 416 137/8! 352 4 1102 101 I 45.9 211 I 95.8
80 381/8 968 22 I 4 1102 10 I 254 187/81 479 155/81 397 4 102 101 I 45.9 231 104.9
8 1 200 71 1/8! 1807 48 I 1219 71/21191 16 I 406 373/41 959 291/41 743 71/21191 847 384.5 1323 600.6
10 1250 841/8! 2137 58 I 1473 1 9 I 229 18 1 457 453/41 1162 135 3/8 899 9 229 14101 640.1 1 2228 1011.5
FLOW CHARACTERISTICS
MODEL 950DA 2 1/2" & 3" (STANDARD & METRIC)
FLOW RATES (us)
12.6 25.2 37.9 50.5
04 i
200 400 600
FLOW RATES (GPM)
MODEL 950DA 8" & 10" (STANDARD & METRIC)
FLOW RATES (us)
63.1 126.2 189.3
CL 0 1000 2000 3000
FLOW RATES (GPM)
*Rated Flow (Established by approval agencies)
cc 0
39 In
35
C,)
LU Ci)
800
252.4
04j
39
35
4000 for
0
TYPICAL INSTALLATION
Local codes shall govern installation requirements. Unless oth-
erwise specified, the assembly shall be mounted at a minimum
of 12' (305mm) and a maximum of 30" (762mm) above adequate
drains with sufficient side clearance for testing and maintenance.
The installation shall be made so that no part of the unit can be
submerged.
Capacity thru Schedule 40 Pipe (GPM)
Pipe size 5 ft/sec 7.5 ft/sec 10 ft/sec 15 ft/sec
2 1/2" 75 112 149 224
115 173 230 346
198 298 397 595
6" 450 675 900 1351
8" 1 780 1 1169 1 1559 2339
10" 1 1229 1 1843 1 2458 3687
PROTECTIVE
ENCLOSURE
12" MIN.
30" MAX.
SUPPORT
DIRECTION OF FLOW
MAIN INLET
OUTDOOR INSTALLATION VERTICAL INSTALLATION
SPECIFICATIONS
The Double Check Detector Backflow Preventer shall be ASSE® Listed 1048, and supplied with full port OS&Y gate valves. The
main body and access covers shall be epoxy coated cast iron (ASTM A126 Class B), the seat ring and check valve shall be cast
bronze (ASTM B 584), the stem shall be stainless steel (ASTM A 276) and the seat disc elastomers shall be EPDM. The first and
second check valves shall be accessible for maintenance without removing the device from the line. The Double Check Detector
Backflow Preventer shall be a WILKINS Model 9500A.
Page 2 of 2
WILKINS OPERATION OF ZURN INDUSTRIES, 1747 Commerce Way, Paso Robles, CA 93446 Phone:805/238-7100 Fax:805/238-5766
IN CANADA: ZURN INDUSTRIES LIMITED, 3544 Nashua Dr., Mississauga, Ontario L4V 11_2 Phone: 905/405-8272 Fax:905/405-1292
Product Support Help Line: 1-877-BACKFLOW (1-877-222-5356) • Website: http://www.zurn.com
-r- ;:; (jJ •t -' A%As,JR'/ SWT
A DCI 200 3X D0 5
- '(_ 3 )
-1) •Ui "-
-
A 6 12-o Wl-
Contractor's Material and Test Certificate for Aboveground Piping
PROCEDURE
Upon completion of work, inspection and tests shall be made by the contractors representative and witnessed by an owners
Representative. All 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: VIASAT CAFETERIA BUILDING DATE 2-13-13
PROPERTY ADDRESSELCAMINO REAL, CARLSBAD, CA --J
ACCEPTED BY APPROVING AUTHORITIES:(NAMES) CARLSBAD FIRE DEPARTMENT
ADDRESS:
PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS D YES D NO
EQUIPMENT USED IS APPROVED YES 0 NO
IF NO, EXPLAIN DEVIATIONS
HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO YES 0 NO
LOCATION OF CONTROL VALVES AND CARE & MAINTAINENCE OF THIS
NEW EQUIPMENT?
INSTRUCTIONS HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES? 0 YES 0 NO
SYSTEM COMPONENTS INSTRUCTIONS ID YES C] NO
CARE AND MAINTENANCE INSTRUCTIONS 0 YES 0 NO
NFPA#25 YES [J NO
LOCATION OF SUPPLIES BUILDINGS: SAME
SYSTEM
YEAR OF ORAFICE TEMPERATURE
MAKE MODEL MANUFACTURER SIZE QUANTITY RATING
TYCO UPRIGHT TY-FRB 2012 1/2 12 200
TYCO REC PENDENT TY-FRB 2012 1/2 58 155 SPRINKLERS
TYCO DRY PEND. DS-1 2012 1/2 2 155
0
0
PIPE AND Type of pipe Steel
FITTINGS Type of fittings Steel
MAXIMUM TIME TO OPERATE
ALARM VALVE ALARM DEVICE THROUGH TEST CONNECTION
OR FLOW TYPE MAKE MODEL MINUTES SECONDS
INDICATOR VANE POTTER VSR-SF 0 55
TIME TO TRIP WATER AIR TRIP POINT AIR TIME WATER ALARM
DRY PIPE THROUGH TEST PRESSURE PRESSURE PRESSURE REACHED OPERATED
OPERATING CONNECTION TEST OUTLET PROPERLY
TESTS MIN SEC PSI PSI PSI MIN SEC YES NO
WITHOUT N/A 0 0
Q.O.D.
WITH N/A 0 0
Q.O.D.
IF NO EXPLAIN:
OPERATION 0 PNEUMATIC 0 ELECTRIC 0 HYDRAULIC
PIPING SUPERVISED 0 YES 0 NO DETECTING MEDIA 0 YES 0 NO
SUPERVISED
DELUGE AND
DOES VALVE OPERATE FROM THE MANUAL TRIP, REMOTE, OR BOTH
CONTROL STATIONS? 0 YES O NO PREACTION
VALVES
IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT FOR
TESTING? C] YES 0 NO
IF NO EXPLAIN:
MAKE MODEL DOES EACH CIRCUIT OPERATE DOES EACH CIRCUIT MAXIMUM TIME TO
SUPERVISION LOSS ALARM? OPERATE VALVE OPERATE RELEASE
RELEASE?
YES NO YES NO MIN SEC
LOCATION & MAKE & MODEL SETTING STATIC PRESSURE RESIDUAL FLOW RATE
PRESSUJW FLOOR: PRESSURE
REDUCING (FLOWING)
VALVE INLET OUTLET INLET OUTLET FLOW (GPM) TEST (PSI) (PSI) (PSI) (PSI)
HYDROSTATIC- Hydrostatic test shall be made at not less than 200ps1 (13.6 bars) for 2 hours or 50psi (3.4 bars) above static pressure in
excess of 150psi (10.2 bars) for 2 hours. Differential thy-pipe valve clappers shall be left open during the test to prevent damage.
TEST
DESCRIPTION PNEUMATIC- Establish 40psi (2.7 bars) air pressure and measure drop, which shall not exceed 1 /2psi (0.1 bars) in 24 hours. Test pressure
tanks at normal water level and air pressure and measure air pressure drop, which shall not exceed 1 1/2p5i (0.1 bars) in 24 hours.
ALL PIPING HYDROSTATICALLY TESTED AT DRY PIPING PSI (200BARS) 2HRS IF NO STATE REASON:
PNEUMATICALLY TESTED EQUIPMENT OPERATES YES 0 NO PROPERLY. Z YES 0 NO
DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS SODIUM SILICATE OR
DERIVATIVES OF SODIUM SILICATE, BRINB, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS,
OR STOPPING LEAKS? D YES []NO
TESTS DRAIN TEST OF GAUGE LOCATED NEAR WATER SUPPLY TEST RESIDUAL PRESSURE WITH VALVE IN ~READING
ONNECTION: 109 PSI ( BARS) 'EST CONNECTION OPEN WIDE: 104 PSI
BARS)
UNDERGROUND MAINS AND LEAD IN CONNECTIONS TO SYSTEM RISERS OTHER EXPLAIN
LUSHEDBEFORE MADE TO SPRINKLER PIPING. 0 YES 0
NO
VERIFIED BY COPY OF THE U FORM NO. 85B FLUSHED BY INSTALLER OF
IF NO, EXPLAIN:NA UNDERGROUND SPRINKLER PIPING.
O YES ONO
IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE, HAS
REPRESENTATIVE SAMPLE TESTING BEEN SATISFACTORILY COMPLETED? o YES DNo
BLANK TESTING NUMBER USED LOCATIONS: NU MBER REMOVED
GASKETS
WELDED PIPING 0 YES O NO
IF YES
DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT
WELDING PROCEDURES COMPLY WITH THE 0 YES 0 NO
REQUIREMENTS OF AT LEAST AWS D 10.9. LEVEL AR-3?
WELDING
DID YOU CERTIFY THAT THE WELDING WAS PERFORMED
BY WELDERS QUALIFIED IN COMPLIANCE WITH THE 0 YES 0 NO
REQUIREMENTS OF ATLEAST AWS D 10.9 LEVEL AR-3?
DO YOU CERTISY THAT WELDING WAS CARRIED OUT IN
COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL
PROCEDURE TO ENSURE THAT ALL DISC ARE RETREIVED, 0 YES []NO
THAT OPENEINGS IN PIPING ARE SMOOTH, THAT SLAG AND
OTHER WELDING RESIDUE ARE REMOVED AND THAT THE
INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED?
CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE 0 YES []NO (DISCS). TO ENSURE THAT ALL CUTOUTS (DISCS) ARE RETREIVED?
HYDRAULIC NAMEPLATE PROVIDED: IF NO EXP LAIN:
DATA . 0 YES El NO
REMARKS DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN 2-13-13
NAME OF SPRINKLER CONTRACTOR: PARAMOUNT FIRE SYSTEMS INC.
TESTS WITNESSED BY
FOR PROPERTY OWNER (SIGNED) TITLE: DATE:
SIGNATURES PETE HAMILTON, PBG 4.1 SUPER 2/13/13
FOR SPRINKLER CONTRACT ç1('(SIGNED TITLE: DATE:
JAMES CHENEY, PFSI PM 2/13/13
ADDITIONAL EXPLANATIONS AND NOT,
FA
Carlsbad Fire Department
Fire Sprinkler System Testing
Check List
PERMIT #: DATE: j. IS. Zoi
PREMISES NAME: i44S,*c çt7jzI64
ADDRESS: (efa3 F
CONTRACTOR :iZjt &,.ssr TRA57
1 1 Sprinkler Pre-Test Items (ALL Systems) OK CN A Stamped, Approved Plans On Job Site oiL- B Verify Completion Of Underground Rough-In, UG Hydro, Flush of UG, Aboveground
H
y
d
r
o
,
AG Rough Pipe Inspection Has Been completed Prior To This Test
C 'Minimum of 2 Personnel Present, 2-Way Communication, Stop Watch
D. Check "Fire Sprinkler Data Plate" on riser (pipe schedule system does not nee
d
p
l
a
t
e
)
Location of design area
Discharge density over design area (s)
Required flow & residual pressure demand @ base of riser
Hose stream demand in addition to sprinkler demand 46 E Signage - Exterior (minimum of 4" letters) to Interior (minimum 2" letters) doors shall be
labeled Sprinkler Riser Room" and all valves & drains shall be labeled
F System Type - Verify what type of
G Monitoring Verify if system is monitored y a central monitoring agency Yesif-- Group R, Div. I = 20+ heads
Grdup I, Div. 1.1 & 1.2 =20+ heads
All other occupancies= 100+ heads
H 'Monitoring - Do not take system off line" - call NCJPA 858-756-3006, explain "testing" will
me
start @ time/address of building and do not have CFD respond.
I Riser room - Shall be clear space around sprinkler riser (If in warehouse- falling hazards may
constitute a cage or bollards around riser for protection)
J Riser Schematic/Map - Shall denote riser floor detail / zones throughout building, shall be
located at riser, FACP annunciator panel and Knox box- Map shall ID all locations:
r
i
s
e
r
,
annunciator panel, FACP & Knox Box ii/,4. 2 Operational Trip Test for Dry System A3. A This test requires 2-way communication
- - B Verify static pressure (Number of #'s prior to water flow)- Air gauge should be l
o
w
e
r
o
n
t
h
e
system side
C If monitored, all valves shall have tamper switches- if not monitored, chain/lock OS&
Y
Valve and Water Main Valve in vault (Each water flow switch is separately zon
e
d
a
t
FACP)
Vault- Water Main- Valve
Low Air Pressure- on system side, trip @ 10# below normal pressure
OS&Y Valve
Post Indicator Valve
Isolation Valves (Ask sprinkler contractor if there are any of these valves- either
remove or provide tamper switch
D Test low air pressure, (bleed off air, fire alarm pánel shall indicate supervisory sign
a
l
)
(Tamper switch shall be located on the system side if the line)
E 24 Hour Pneumatic Leak Test on Dry System- System shall maintain a minimum
o
f
4
0
p
s
i
f
o
r
24 hrs w/ <than 1 1/2 psi (0.1 bar) of pressure loss, the 24 hr pneumatic test can be
preformed either before or after the acceptance test
- - F Accelerator or Exhauster is required on systems that exceed 500 gal. water volu
m
e
(Exception- if water can be delivered to Insp. Test connection w/in 60 sec.)
- - G Inspector's Test - Water must flow w/in 60 seconds or less, fire alarm panel shall only
indicate general alarm" and water gong/electronic bell shall ring (Shall result in audible
alarm on premises within 5 minutes of when flow begins). Signage on bell shall
r
e
a
d
"
F
i
r
e
Alarm Call 9-]-]" (* 60 second waler delivery is not required < 750 gal.-then acceptable up to 3 minutes) Time it takes for valve to trip after opening the system test valve.
A
i
r
&
water pressures before test Air pressure at trip point. Delivery time for water to
r
e
a
c
h
t
h
e
test outlet & Indication of whether or not alarms operated properly
H Sprinkler heads in penddnt position, shall be listed dry-pendant type if subject to freez
i
n
g
- - I Check air compressor refills the system within 30 minutes to original pressure (Check sei
s
m
i
c
bracing per plan for compressor)
J Alarm - Shall have interior water flow alarm @ normally occupied area
- - K Alarm - Test telephone lines (1 & 2) - Disconnect line, max. of 4 mm. to signal monitoring
gncy that a trouble signal has occurred at site, test both lines
L Dry pipe valve & supply pipe shall be protected against freezing and mechanical inju
r
y
(riser room- heater install to kick in at 40 degrees)
M Auxiliary Drains are required, drain locations shall be ID with signs & denoted on riser
z
o
n
e
map
__
OK CN
N Documentation - Shall verify results of trip test with monitoring agency, shall have test
results faxed to CFD - Fire Prevention Bureau 760-602-8561, and Contractor shall submit
signed NFPA UG/AG Material & Test Certificate
0 Telephone NCJPA, verify", tim6 of 1st call from monitoring agency and prior to Ieaiing site
explain testis complete and systemis back on line." '..
3 Flow Test for Wet System -
A Conduct General Pie-Items listed above
B Verify static pressure (Pressure gauges are requiredabove;& beIoweach alarm hëck
valve when installed; if shotgun riser- one gauge is o.k)
Psi
C If monitored, all valves shall have tamper switches- if not monitored, chain/lock OS&Y
Valve and Water Main Valve in vault (Each water flow switch is separately zoned at
FACP)
Vault- Water Main- Valve
OS&Y Valve
Post Indicator Valve
Isolation Valves (Ask sprinkler contractor if there are any of these valves- either
remove or provide tamper switch)
Test All Valves for Tamper Switches,
D - Inspector's Test Water flow, fire alarm panel shall only indidate "general alarm" and
water gong/electronic bell shall ring (Shall result in audible alarm on premises within 1.5
'minutes of when flowbegins). Signage on bell shall read Fire Alarm Call 9-1-1'
7.Sec
E Verify residual pres'suie during flow test
11 PSI hø
F Alarm Shall have interior water flow alarm @ normally occupied area
G Alarm Test telephone lines (1 & 2) - Disconnect line, max. of 4 mm. to signal monitoring
aqencv that a trouble signal has occurred at site, test b6th lines
H .Documentation Shall verify results of trip test with monitoring agency, shall have test
results faxed toCFD - Fire Prevention Bureau 760-602-8561, and Contractor shall submit
Mt signed NFPA UG/AG Material & Test Certificate
I Telephone NCJPA, verify time of 10 call from monitoring agency and prior to leaving site
explain test is complete and system is back on line."
4 ,' Fire Department Connections
A. Connections shall not be connected on the suction side of a pump . AVE-
B Shall be equipped with check valve, with NO shut off valve permitted, unless tamper
switch provided and tested
C Piping between check valve and outside hose connection shall be equipped with
automatic drip
D FDC pipe size shall be atIedst4" (Exception fort hydraulically calculated systern, FDC pipe
serving one system riser may be as small as the system riser)
5 Pre-Action Systems plA-
A, Single Interlock- Admits water to sprinkler piping upon operation of detection devices.
Non-Interlock- Admits water to sprinkler piping upon operation of detection devices or
automatic sprinklers. Double Interlock- Admits water to sprinkler piping upon operation of
both detection devices and automatic sprinklers..
6 Anti-Freeze Systems
A Solutions- Listed CPVC pipe & fittings shallbe protected from freezing w/ Glycerine.
Prohibited Solutions for CPVC are Diethylene, Ethylene, Propylene Glycols -
B Potable water connections- see NFPA 13 & 13D for specific requirements
Antifreeze solution shall be prepared with a freezing point to 0-10 degrees F -
C Connections- Between the wet & antifreeze system, shall have back flow prevention
device and pressure reducing device between each double check valve -
Verify time when DRY System will be re set & back in service -
Site Inspection: Match Plans:@or N Test Pass:or N
Corrections Needed: Y or? -
City of Carlsbad Fire Department
Name: I 14,1f
FD Representative