HomeMy WebLinkAbout2681 GATEWAY RD; BLDG G; AS080051; Permit8/17/22,10:49 AM AS080051 Permit Data
City of Carlsbad
Sprinkler Permit
Permit No: AS080051
Job Address: 2681 GATEWAY RD Status: ISSUED
Permit Type: SPRINK Applied 3/26/2008
Parcel No: 2131910600 Approved: 3/26/2008
Lot #: 0
Reference No.: Issued: 3/26/2008
PC #: Inspector:
Project Title: VILLAGE CENTER, SHP G THREE FIRE SPRINKLER
INSPECTIONS @ $65/00
Applicant:
G & A FIRE PROTECTION
SUITE 40
14141 COVELLOST
VAN NUYS,CA
818-780-9080
Owner:
LNR CPI BRESSI RETAIL L L C
C/O LNR PROPERTY CORP
4350 VON KARMAN AVE #200
NEWPORT BEACH CA
Fees ($) Add'I Fees ($) Total ($) Balance ($)
195 0 195 0
1/1
Lc C 66365,84
G & A FIRE PROTECTION CORP.
14141 COVELO ST. #4D
VAN NUYS, CALIFORNIA. 91405
avigafirepro.com
FAX 780-8076
Job Name : SHOP G (SSU CALC#1)
Building
Location : 2681 GATEWAY RD. CARLSBAD, CALIFORNIA
System
Contract
Data File : 07032-C shop ssu.WXI
APPROV4UBIUilTTED
cATLSBADF! EDEPARTMENT
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
G & A FIRE PROTECTION CORP. Page 1
SHOP G (SSU CALC#1) Date 04/10/08
Hydraulic Design Information Sheet
Name - SHOP 'G' BRESSI RANCH VILLAGE CENTER. Date - 04/10/08
Location - 2681 GATEWAY RD. CARLSBAD, CALIFORNIA
S ( ) NFPA 13 ( ) Lt. Haz. Ord.Haz.Gp. ( ) 1 (X) 2 ( ) 3 ( ) Ex.Haz.
Y ( ) NFPA 231 ( ) NFPA 231C ( ) Figure Curve
E
M Area of Sprinkler Operation - 1057 System Type Sprinkler/Nozzle
Density - 0.20 (X) Wet Make VIKING
D Area Per Sprinkler - 130 ( ) Dry Model VK350
S Hose Allowance - Inside - 250 ( ) Preaction K-Factor 8.0
Calculation Flow Required - 510 Press Required - 43
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Water Supply Curve (C)
G & A FIRE PROTECTION CORP. Page 2
SHOP G (SSU CALC#1) Date 04/10/08
City Water Supply: Demand: Cl - Static Pressure : 49.5 Dl - Elevation : 5.414
C2 - Residual Pressure: 18 D2 - System Flow : 260.06
C2 - Residual Flow : 2140 D2 - System Pressure : 43.730
Hose (Adj City)
Hose ( Demand) : 250
D3 - System Demand : 510.06
Safety Margin : 3.551
150
140
130
p120
R°
E10°
S90
s 80
u 70
Cl R6°
E5° :z
—e
40
30
C2 20
10
300 600 900 1200 1500 1800 2100 2400 2700
FLOW ( N A 1.85)
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
How Diagram
G & A FIRE PROTECTION CORP. Page 3
SHOP G (SSU CALC#1) Date 04/10/08
29.5
9 -10
26.8
21 <- 20
30.3
18 - 11
T
I 91.1
31.1
17 -. 12
26.2
16 -. 3
28.1
15 - 4
I 107
30.
14 - 5
31.3 60.8 122.8
22 <-23 <--10€-Il <-12 <-13 <-8
31.3 91.1 122.8
26 52.2 107 137.2 260.1 260.1 260.1
1 <-2 <-3 <-20<-4 <-5 <-6 <-7 <-8 <-- MI <-TOR<-B0F4--BFL<-SRC
26 79 137.2 137.2 260.1 260.1
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Fittings Used Summary
G & A FIRE PROTECTION CORP. Page 4
SHOP G (SSU CALC#1) Date 04/10/08
Fitting Legend
Abbrev. Name /2 % 1 1% 11/2 2 2% 3 3% 4 5 6 8 10 12 14 16 18 20 24
B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 9 10 12 19 21 0 0 0 0 0
E 90 Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61
Fsp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow
G Generic Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13
I 90' Flow thruTee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121
Zai Ames 4000SS Fitting generates a Fixed Loss Based on Flow
Units Summary
Diameter Units
Length Units
Flow Units
Pressure Units
Inches
Feet
US Gallons per Minute
Pounds per Square Inch
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Pressure I Flow Summary - STANDARD
G & A FIRE PROTECTION CORP. Page 5
SHOP G (SSU CALC#1) Date 04/10/08
Node Elevation K-Fact Pt Pn Flow Density Area Press
No. Actual Actual Req.
9 15.5 8 13.63 na 29.54 0.2 130 7.0
21 15.5 8 11.21 na 26.79 0.2 130 7.0
18 15.5 8 14.31 na 30.27 0.2 130 7.0
17 15.5 8 15.75 na 31.75 0.2 130 7.0
16 15.5 8 10.7 na 26.17 0.2 130 7.0
15 15.5 8 12.31 na 28.07 0.2 130 7.0
14 15.5 8 14.24 na 30.19 0.2 130 7.0
22 15.5 8 15.29 na 31.29 0.2 130 7.0
23 15.5 15.42 na
10 15.5 16.07 na
11 15.5 16.86 na
12 15.5 18.54 na
13 15.5 22.98 na
1 15.5 8 10.56 na 26.0 0.2 130 7.0
2 15.5 12.49 na
3 15.5 12.65 na
20 15.5 13.25 na
4 15.5 14.53 na
5 15.5 16.78 na
6 15.5 22.23 na
7 14.5 26.3 na
8 14.5 26.37 na
Ml 14.5 27.03 na
TOR -3.0 35.26 na
BOR -3.0 38.87 na
BFL -3.0 39.21 na
SRC 3.0 43.73 na 250.0
The maximum velocity is 18.77 and it occurs in the pipe between nodes 5 and 6
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Final Calculations - Hazen-Williams
G & A FIRE PROTECTION CORP. Page 6
SHOP C (SSU CALC#1) Date 04/10/08
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. 'C' or Ftng's Pe Pv Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
*P-1
9 29.54 1.08 2T 10.0 0.500 13.633 K Factor =8.00
to 120 0.0 10.000 0.0
10 29.54 0.2324 0.0 10.500 2.440 Vel = 10.35
0.0
29.54 16.073 K Factor = 7.37
*P2
21 26.79 1.08 2T 10.0 0.500 11.213 K Factor = 8.00
to 120 0.0 10.000 0.0
20 26.79 0.1939 0.0 10.500 2.036 Vel = 9.38
0.0
26.79 13.249 K Factor = 7.36
*P6
18 30.27 1.08 2T 10.0 0.500 14.313
to 120 0.0 10.000 0.0
11 30.27 0.2430 0.0 10.500 2.551
0.0
30.27 16.864
*P-9
17 31.75 1.08 2T 10.0 0.500 15.748
to 120 0.0 10.000 0.0
12 31.75 0.2654 0.0 10.500 2.787
0.0
31.75 18.535
*P12
K Factor = 8.00
Vel = 10.60
K Factor = 7.37
K Factor = 8.00
Vel= 11.12
K Factor= 7.37
16 26.17 1.08 2T 10.0 0.500 10.703 K Factor = 8.00
to 120 0.0 10.000 0.0
3 26.17 0.1857 0.0 10.500 1.950 Vel = 9.17
0.0
26.17 12.653 K Factor= 7.36
*P_15
15 28.07 1.08 2T 10.0 0.500 12.312 K Factor = 8.00
to 120 0.0 10.000 0.0
4 28.07 0.2114 0.0 10.500 2.220 Vel = 9.83
0.0
28.07 14.532 K Factor = 7.36
*P18
14 30.19 1.08 2T 10.0 0.500 14.244 K Factor =8.00
to 120 0.0 10.000 0.0
5 30.19 0.2419 0.0 10.500 2.540 Vel = 10.57
0.0
30.19 16.784 KFactor= 7.37
*P21
22 31.29 1.08 0.0 0.500 15.293 K Factor = 8.00
to 120 0.0 0.0 0.0
23 31.29 0.2580 0.0 0.500 0.129 Vel = 10.96
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Final Calculations - Standard
G & A FIRE PROTECTION CORP. Page 7
SHOP C (SSU CALC#1) Date 04/10/08
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv ******* Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
23 0.0 1.728 2T 16.0 8.833 15.422
to 120 0.0 16.000 0.0
10 31.29 0.0262 0.0 24.833 0.651 Vel = 4.28
10 29.53 1.728 0.0 8.833 16.073
to 120 0.0 0.0 0.0
11 60.82 0.0896 0.0 8.833 0.791 Vel = 8.32
11 30.27 1.728 0.0 8.833 16.864
to 120 0.0 0.0 0.0
12 91.09 0.1892 0.0 8.833 1.671 Vel = 12.46
12 31.75 1.728 IT 8.0 5.500 18.535
to 120 0.0 8.000 0.0
13 122.84 0.3289 0.0 13.500 4.440 Vel = 16.81
13 0.0 1.728 IT 8.0 1.000 22.975
to 120 0.0 8.000 0.433
8 122.84 0.3289 0.0 9.000 2.960 Vel = 16.81
0.0
122.84 26.368 K Factor= 23.92
*P24
1 26.00 1.08 2T 10.0 0.500 10.562 K Factor =8.00
to 120 0.0 10.000 0.0
2 26.0 0.1835 0.0 10.500 1.927 Vel = 9.11
2 0.0 1.728 0.0 8.833 12.489
to 120 0.0 0.0 0.0
3 26.0 0.0186 0.0 8.833 0.164 Vel = 3.56
3 26.17 1.728 0.0 8.833 12.653
to 120 0.0 0.0 0.0
20 52.17 0.0675 0.0 8.833 0.596 Vel = 7.14
20 26.79 1.728 0.0 8.833 13.249
to 120 0.0 0.0 0.0
4 78.96 0.1453 0.0 8.833 1.283 Vel = 10.80
4 28.07 1.728 0.0 8.833 14.532
to 120 0.0 0.0 0.0
5 107.03 0.2550 0.0 8.833 2.252 Vel = 14.64
5 30.19 1.728 1T 8.0 5.500 16.784
to 120 0.0 8.000 0.0
6 137.22 0.4037 0.0 13.500 5.450 Vel = 18.77
6 0.0 1.728 IT 8.0 1.000 22.234
to 120 0.0 8.000 0.433
7 137.22 0.4037 0.0 9.000 3.633 Vel = 18.77
7 0.0 4.31 0.0 14.500 26.300
to 120 0.0 0.0 0.0
8 137.22 0.0047 0.0 14.500 0.068 Vel = 3.02
8 122.84 4.31 1E 10.0 33.083 26.368
to 120 0.0 10.000 0.0
Ml 260.06 0.0154 0.0 43.083 0.663 Vel = 5.72
Ml 0.0 4.31 1 10.0 32.083 27.031
to 120 0.0 10.000 7.579
TOR 260.06 0.0154 0.0 42.083 0.647 Vel = 5.72
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Finl Calculations - Standard
G & A FIRE PROTECTION CORP. Page 8
SHOP G (SSU CALC#1) Date 04/10/08
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftngs Pe Pv Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
TOR 0.0 4.31 1E 10.0 18.000 35.257
to 120 lFsp 0.0 22.000 3.000 * Fixed loss = 3
BOR 260.06 0.0154 1 12.0 40.000 0.614 Vel = 5.72
BOR 0.0 5.914 3E 63.465 93.910 38.871
to 150 0.0 63.465 0.0
BFL 260.06 0.0022 0.0 157.375 0.343 Vel = 3.04
BFL 0.0 5.914 IT 45.332 27.410 39.214
to 150 1G 4.533 71.020 4.301 * Fixed loss = 6.9
SRC 260.06 0.0022 1 21.155 98.430 0.215 Vel = 3.04
lZai 0.0
250.00 Qa = 250.00
510.06 43.730 K Factor 77.13
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Lie. C-I 6 b636594•
C & A FIRE PROTECTION CORP.
14141 COVELO ST. #4D
VAN NUYS, CALIFORNIA. 91405
avigafirepro.com
FAX 780-8076
Job Name : SHOP G (ROOF CALC#2)
Building
Location 2681 GATEWAY RD. CARLSBAD, CALIFORNIA
System
Contract
Data File : 07032-C shop roof.WX2
APPROVED 4P
CARL BAD PA TME NT
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
G & A FIRE PROTECTION CORP. Page 1
SHOP G (ROOF CALC#2) Date 04/10/08
Hydraulic Design Information Sheet
Name - SHOP 'G' BRESSI RANCH VILLAGE CENTER. Date - 04/10/08
Location - 2681 GATEWAY RD. CARLSBAD, CALIFORNIA
S ( ) NFPA 13 (X) Lt. Haz. Ord.Haz.Gp. ( ) 1 ( ) 2 ( ) 3 ( ) Ex.Haz.
Y ( ) NFPA 231 ( ) NFPA 231C ( ) Figure Curve
E
M Area of Sprinkler Operation - MR ROOF System Type Sprinkler/Nozzle
Density - 0.10 (x) Wet Make VIKING
D Area Per Sprinkler - 120.00 ( ) Dry Model VK300
S Hose Allowance - Inside - 100 ( ) Preaction K-Factor 5.6
Calculation Flow Required - 232 Press Required - 47
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Water Supply Curve (C)
G & A FIRE PROTECTION CORP. Page 2 SHOP C (ROOF CALC#2) Date 04/10/08
City Water Supply: Demand: Cl - Static Pressure : 49.5 Dl - Elevation : 6.930 C2 - Residual Pressure: 18 D2 - System Flow : 132.042 C2 - Residual Flow : 2140 D2 - System Pressure : 47.510 Hose (Adj City) Hose ( Demand ) : 100 D3 - System Demand : 232.042 Safety Margin : 1.473
150
140
130
p120
R11°
E10°
590
s 80
u70
R6°
E5°
40 D
30 —
3
C2 20 —
10 .
300 600 900 1200 1500 1800 2100 2400 2700 FLOW ( N A 1.85)
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Flow Diagram
G & A FIRE PROTECTION CORP.
SHOP G (ROOF CALC#2)
15.7
45 <. 37
I 30.5
15.
44 -. 38
Page 3
Date 04/10/08
15.4
43 <- 38
17.4 53.5
40 <- 41 - 42 - R2
35.3 I
I 78.6
14.8 D 1.4 132 132 132 132 132 132
36 <-37 <-38 <-39 <-R2<--RI<-20 <-4 <-5 <-6 <-7 <-8 <-MI<-- TOR- BOR--BFL<--SRC
30.5 78.6 132 132 132 132 132 132
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Fittings Used Summary
G & A FIRE PROTECTION CORP. Page 4
SHOP C (ROOF CALC#2) Date 04/10/08
Fitting Legend
Abbrev. Name % % 1 11/4 1% 2 272 3 372 4 5 6 8 10 12 14 16 18 20 24
B Generic Butterfly Valve 0 0 0 0 0 0 7 10 0 12 9 10 12 19 21 0 0 0 0 0 E 90 Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61
Fsp Flow Switch Potter VSR Fitting generates a Fixed Loss Based on Flow
G Generic Gate Valve 0 0 0 0 0 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13
I 90 Flow thruTee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121
Zai Ames 4000SS Fitting generates a Fixed Loss Based on Flow
Units Summary
Diameter Units
Length Units
Flow Units
Pressure Units
Inches
Feet
US Gallons per Minute
Pounds per Square Inch
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Pressure I Flow Summary - STANDARD
G & A FIRE PROTECTION CORP. Page 5
SHOP C (ROOF CALC#2) Date 04/10/08
Node Elevation K-Fact Pt Pn Flow Density Area Press
No. Actual Actual Req.
45 19.0 5.6 7.87 na 15.71 0.1 120 7.0
44 19.0 5.6 7.76 na 15.6 0.1 120 7.0
43 19.0 5.6 7.6 na 15.44 0.1 120 7.0
40 19.0 5.6 9.64 na 17.39 0.1 120 7.0
41 19.0 5.6 10.19 na 17.88 0.1 120 7.0
42 19.0 5.6 10.56 na 18.2 0.1 120 7.0
36 19.0 5.6 7.0 na 14.82 0.1 120 7.0
37 19.0 8.0 na
38 19.0 8.2 na
39 19.0 5.6 9.23 na 17.01 0.1 120 7.0
R2 19.0 12.27 na
Ri 15.5 21.13 na
20 15.5 22.69 na
4 15.5 26.01 na
5 15.5 27.03 na
6 15.5 28.82 na
7 14.5 30.52 na
8 14.5 30.58 na
Ml 14.5 30.79 na
TOR -3.0 38.56 na
BOR -3.0 41.73 na
BFL -3.0 41.86 na
SRC 3.0 47.51 na 100.0
The maximum velocity is 22.86 and it occurs in the pipe between nodes R2 and Ri
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Final Calculations - Hazen-Williams
G & A FIRE PROTECTION CORP. Page 6
SHOP G (ROOF CALC#2) Date 04/10/08
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
*P6
45 15.71 1.08 0.0 1.700 7.874 K Factor= 5.60
to 120 0.0 0.0 0.0
37 15.71 0.0718 0.0 1.700 0.122 Vel = 5.50
0.0
15.71 7.996 K Factor= 5.56
*p9
44 15.60 1.08 IT 5.0 1.200 7.758 K Factor= 5.60
to 120 0.0 5.000 0.0
38 15.6 0.0713 0.0 6.200 0.442 Vel = 5.46
0.0
15.60 8.200 K Factor= 5.45
*Pi2
43 15.44 1.08 IT 5.0 3.580 7.600 K Factor = 5.60
to 120 0.0 5.000 0.0
38 15.44 0.0699 0.0 8.580 0.600 Vel = 5.41
0.0
15.44 8.200 K Factor= 5.39
*p.15
40 17.39 1.08 0.0 6.330 9.641 K Factor =5.60
to 120 0.0 0.0 0.0
41 17.39 0.0872 0.0 6.330 0.552 Vel = 6.09
41 17.88 1.536 0.0 6.330 10.193 K Factor = 5.60
to 120 0.0 0.0 0.0
42 35.27 0.0580 0.0 6.330 0.367 Vel = 6.11
42 18.19 1.536 IT 6.0 7.660 10.560 K Factor =5.60
to 120 0.0 6.000 0.0
R2 53.46 0.1253 0.0 13.660 1.711 Vel = 9.26
0.0
53.46 12.271 K Factor= 15.26
*Pi8
36 14.82 1.08 1 E 2.0 8.370 7.000 K Factor = 5.60
to 120 IT 5.0 7.000 0.0
37 14.82 0.0648 0.0 15.370 0.996 Vel = 5.19
37 15.71 1.536 0.0 4.580 7.996
to 120 0.0 0.0 0.0
38 30.53 0.0445 0.0 4.580 0.204 Vel = 5.29
38 31.04 1.536 0.0 6.330 8.200
to 120 0.0 0.0 0.0
39 61.57 0.1626 0.0 6.330 1.029 Vel = 10.66
39 17.01 1.536 IT 6.0 5.910 9.229 K Factor =5.60
to 120 0.0 6.000 0.0
R2 78.58 0.2554 0.0 11.910 3.042 Vel = 13.61
R2 53.46 1.536 iT 6.0 5.000 12.271
to 120 0.0 6.000 1.516
Ri 132.04 0.6672 0.0 11.000 7.339 Vel = 22.86
Ri 0.0 1.728 0.0 4.167 21.126
to 120 0.0 0.0 0.0
20 132.04 0.3760 0.0 4.167 1.567 Vel = 18.06
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Final Calculations - Standard
G & A FIRE PROTECTION CORP. Page 7
SHOP G (ROOF CALC#2) Date 04/10/08
Hyd. Qa Dia. Fitting Pipe Pt Pt
Ref. "C" or Ftng's Pe Pv Notes
Point Qt Pf/Ft Eqv. Ln. Total Pf Pn
20 0.0 1.728 0.0 8.833 22.693
to 120 0.0 0.0 0.0
4 132.04 0.3760 0.0 8.833 3.321 Vel = 18.06
4 0.0 2.203 0.0 8.833 26.014
to 120 0.0 0.0 0.0
5 132.04 0.1151 0.0 8.833 1.017 VeI= 11.11
5 0.0 2.203 IT 10.0 5.500 27.031
to 120 0.0 10.000 0.0
6 132.04 0.1152 0.0 15.500 1.786 Vel= 11.11
6 0.0 2.203 IT 10.0 1.000 28.817
to 120 0.0 10.000 0.433
7 132.04 0.1152 0.0 11.000 1.267 VeI= 11.11
7 0.0 4.31 0.0 15.000 30.517
to 120 0.0 0.0 0.0
8 132.04 0.0044 0.0 15.000 0.066 Vel = 2.90
8 0.0 4.31 IE 10.0 36.250 30.583
to 120 0.0 10.000 0.0
MI 132.04 0.0044 0.0 46.250 0.203 Vel = 2.90
MI 0.0 4.31 IE 10.0 33.370 30.786
to 120 0.0 10.000 7.579
TOR 132.04 0.0044 0.0 43.370 0.190 Vel = 2.90
TOR 0.0 4.31 1E 10.0 18.000 38.555
to 120 lFsp 0.0 22.000 3.000 * Fixed loss = 3
BOR 132.04 0.0044 lB 12.0 40.000 0.176 Vel = 2.90
BOR 0.0 5.914 3E 42.0 93.910 41.731
to 120 0.0 42.000 0.0
BFL 132.04 0.0009 0.0 135.910 0.127 Vel = 1.54
BFL 0.0 5.914 IT 30.0 27.410 41.858
to 120 IG 3.0 47.000 5.581 * Fixed loss = 8.18
SRC 132.04 0.0010 1E 14.0 74.410 0.071 Vel = 1.54
lZai 0.0
100.00 Qa = 100.00
232.04 47.510 KFactor= 33.66
Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087
Contractors Material and Test Certificate for Aboveground Piping
DURE
Upon completion SI work nspeclorr and tests shall be made by the conlaclors representative and witnessed by an owners
(ePe0enl8re All delecls Shall be corecled and system tell in service beloe contractor's personnel Inally leave the job
A certicare snaIl be filled out and signed by both representatives. Copes shall be prepared tar approving authorities. owners and
COAllaclot It is understood the owner representatives signature in no way prejudices any claim against contractor lor faulty material. poor
workmanship, 01 IaIure to Comply witS approving authorilys requirements or local ordinances.
PROPERrS' NAME _ 'f L& DATE/ 18-o2
PROPERTY ADDRESS OS/AT€uJA"/ VZO
G AUTHORITI ACCEOAPPRON cAKAU Fie ppft7,vj jt/
ADDRESS
PLANS
INSTALLATION CONFORMS TO ACCEPTED PLANS YES NO
' LII EQUIPMENT USED IS APPROVED YES NO
IIF NO. EXPLAIN DEVIATIONS
HAS PERSON IN CHARGE OF FIRE EOUIPMENT BEEN INSTRUCTEDAS 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 fl NO
I SYSTEM COMPONENTS INSTRUCTIONS YES LI NO
2 CARE AND MAINTENANCE INSTRUCTIONS YES fl NO
3 NFPA2S YES LJ NO
LOCATION SUPPIIESBUILDINGS SHOP c" OF SYSTEM
YEAR YEAR OF ORIFICE TEMPERATURE
MAKE MODEL SIZE QUANTITY RATING
200
SPRINKLERS
PIPE AND Type o( Pipe PNA clOA) f 1/41ZOACI
Type olFItrngs oV6 1YP ( C45 jfz.o,J TP& FIT-TINGS
MAXIMUM TIME TO OPERATE
ALARM ALARM DEVICE THROUGH TEST CONNECTION
VALVE
OR FLOW
TYPE MAKE MODEL MIN SEC
INDICATOR FT1PpTf 1 V5/2 F / ________________
DRY VALVE 0 0 D _________________
MAKE MODEL J_ALNaJ MAKE MODEL f_ SERIAL NO.
TIME TO TRIP TIME WATER I ALARM
O<NG
THROUGH TEST WATER AIR TRIP POINT REACHED j OPERATED
Tt CONNECTION PRESSURE PRESSURE AIR PRESSURE TEST OUTLET I PROPERLY
MIN SEC p PSI PSI MIN. NES NO
Wrlhout
ODD
-
Witt)
IF NO EXPLAIN
MEASURED FROM FIME INSPECTORS TEST CONNECTION IS OPENED.
ION
'PNEUMATIC LIELECTRIC LI HYDRAULIC
PIPING SUPERVISED YES NO DETECTING MEDIA SUPERVISED E YES
DOES VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE LII YES III NO CONTROL STATIONS
PON IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT NO. EXPilN J'IF S FOR TESTING
YES 0 NO
DOES EACH CIRCUIT OPERATE I DOES EACH CIRCUIT MAXIMUM TIME TO • MAKE MODEL SUPERVISION LOSS ALARM I OPERATE VALVE RELEASE OPERATE RELEASE
MIN. SEC. YES NO YES NO
SEE
—
PR IRE
LOCATION
I & FLOOR
MAKE &
MODEL
SETTING STATIC PRESSURE RESIDUAL PRESSURE FLOW RATE
(FLOWING)
ING INLET(PSIJ OUTLET (PSI) INLET(PSI) OUTLET (PSI) FLOW (GPM)
HYDROSTATIC Hydrostatic InSIs shall be made SI not less than 200 psi (13.6 bars) tar two hours or SO Psi (3.4 bars)
above static pressure in excess oF 150 psi (10.2 bars) For two hours. Dilierenlial dry-pipe valve clappers shall be leb
TEST open during test Ia prevent damage. 'All aboveground piping leakage shall be slopped.
DESCRIPTION EIjEUMATII1C: Establish 40 psi )2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi )0.1 bars)
in 24 hours. Test pressure lanks at normal water level and air pressure and measure air pressure drop, which shall
not exceed 1-1/2 psi (0. I bars) in 24 hours.
ALL PIPING HYDROSTATICALLY TESTED AT PSI FOR 9L HRS. IF NO. STATE REASON
DRY PIPING PNEUMATICALLY TESTED YES LI NO
EOUIPMENT OPERATES PROPERLY YES LI NO
DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THATAODITIVES 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 LII NO
DRAIN I READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VALV IN TEST
IESTS TEST SUPPLY TEST CONNECTION jØ PSI CONNECTION OPEN WIDE PSI
UNDERGROUND MAINS AND LEAD, IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE
CONNECTION MADE TO SPRINKLER PIPING.
VERIFIED BY COPY OF THE U FORM 140 85B LI YES LI NO OTHER EXPLAIN
FLUSHED BY INSTALLER OF UNDER. I
GROUND SPRINKLER PIPING LI YES LI NO L)o7,t1/zi
IF POWDER DRIVEN FASTENERS ARE USED IN .J YES LI NO IF NO. EXPLAIN
CONCRETE, HAS REPRESENTATIVE SAMPLE
TESTING BEEN SATISFACTORILY COMPLETED?
BLANK TESTING NUMBER USED LOCATIONS NUMBER REMOVED
GASKETS
WELDED PIPING LI YES O NO
- -
IF YES.,
DO YOU CERTIFY AS THE SPRINKLER CONFRACTOR THAT WELDING
PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST YES LI NO
AWS 010.9, LEVEL AR.37
I 0 WELDING DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS
OUALIFIED IN COMPLIANCE WITH THE REQUIREMENTS OF AT LEAST YES LI NO
AVIS 0109, LEVEL AR.3?
DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE
WITH A DOCUMENTED OUALITY CONTROL PROCEDURE TO INSURE
YES LI THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE NO
SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED.
AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED?
CUTOuTS 00 YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO Lk YES LI NO (DISCS) ENSURE THAT ALL CUTOUTS (DISCS)ARE RETRIEVED?
[ HYDRAULIC NAMEPLATE PROVIDED I IF NO. EXPLAIN DATA
NAMEPLATE YES 0 NO
DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN:
REMARKS
NAME OF SPRINKLER CoNTPACTo,A
fi rc
SIGNATURES TESTS WITNESSED BY
D) TITLE DATE
E
FOR SPRINK2tJ
I
D) TITLE DATE
ADDITIONAL EXPLANAT N ES
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