HomeMy WebLinkAbout2708 LOKER AVE WEST; ; AS050243; Permit10/16/25, 4:01 PM AS050243 Permit Data
City of Carlsbad
Sprinkler Permit
Job Address:
2708 LOKER AV
WEST
Permit Type: SPRINK
Parcel No: 2090810100
Lot#: 0
Reference No.:
Permit No: AS050243
Status: ISSUED
Applied 12/1/2005
Approved: 1/6/2006
Issued: 1/6/2006
PC #: Inspector:
Project Title: LOKER BUSINESS CENTER, BLDG B FIRE SPRINKLER PLAN
CHECK & INSPECTIONS
Applicant: Owner:
LIFEGUARD FIRE PROTECTION
STE F
2605 TEMPLE HEIGHTS DR
OCEANSIDE, CA
760-806-9997
about blank
Fees($)
1,150
Add'I Fees ($)
0
FRANZ-LOKER L LC
2710 LOKER AV
CARLSBAD CA
Total($)
1,150
Balance($)
0
1/1
LIFEGUARD FIRE PROTECTION, I~
2 6 0 5 T E M P L E H E I G H T S D R . S TE : F , 0 C E A N S I D E , C A 9 2ft,t: A
( 7 6 0) 8 0 6 -9 9 9 7 • FAX ( 7 6 0) 8 0 6 -4 8 1 3 (,~;
Hydraulic Design Information Sheet
Name: LOKER BUSINESS CENTER Date: January 4, 2006
Location: 2708 LOKER A VE. WEST
Building: _;;:......B _____________________ System No. .c.Rc..cOOc...c..cF _____ _
Contractor: LIFEGUARD FIRE PROTECTION, INC. Contract No.
Calculated By: LCH Drawing No. 2 OF 3
Construction: ~ Combustible O Non-Combustible Ceiling Height-'-1""4--"-o-'-----F-t-.
SYSTEM DESIGN
[8J NFPA 13: LJ Light Hazard Ordinary Hazard Group D I [8J 2 LJ 3 LJ Extra Haz.ard 0 NFPA231 0 NFPA23JC: Figure: Curve: D Other (Specify)
□Specific Ruling Made By Date
Area of Sprinkler Operation 1500 System T)11e
Density .20 ~ Wet □Dry D Deluge 0 Pre-Action
Area Per Sprinkler 130 SQ.FT. MAX. S(!rinkler or Nozzle
Hose Allowance GPM: Inside 0 Make TYCO Model TY-B
Hose Allowance GPM: Outside 250 Size ½ K-Factor: 5.6
Rack Sorinkler Allowance NIA Temoerature Ratim1 200DEG.
CALCULATION SUMMARY
GPM Required -'3'--'7-"l.;;c.2;;:;.5~-----PSI Required ....c.10;.:3'-C.4;.:9 ______ At Base of Riser
"C" Factor Used: Overhead 120 Under ound 150
WATER SUPPLY
Water Flow Test Pump Data Tank or Reservoir
Date& Time 10-6-05/J0:15AM Rated Capacity Capacity
Static PSI 140 At PSI Elevation
Residual PSI 138 Elevation
GPMFlowing 1680 Well
Elevation 0 Proof Flow GPM
Location SITE
Source of Information LIFEGUARD FIRE WITII CARLSBAD FIRE
COMMODITY STORAGE
Commodity Class Location
Storage Height Area Aisle Width
Storage Method: Solid Piled % Palletized %Rack
Rack D SingleRow D Conventional Pallet 0 Automatic Storage D Encapsulated D DoubleRow 0 Slave Pallet 0 Solid Shelving D Non-Encapsulated D Multiple Row D Open
Flue Spacing In Inch1,s Clearance From Top of Storage to Ceiling
Longitudinal Transverse Ft. In.
Horizontal Barriers Provided
250
240
230
220
210
200
190
180
170
160
150
140
130
120
110
100
90
80
70
60
50
40
30
20
10
•
loker bldg b roof .20/1500
I ,,
.. -I r •1 T
'
I
;f
0/
0 200 400 --600 800 1000
System Demand ..
Sprinkler Demand 107.32 PSI@
Additional Flows
371. 25
250.00
0.00
108.31 PSI@ 621.25
Hose at Source
Total Demand
1200
GPM
GPM
GPM
GPM
1400
Water Flow (GPM)
Sigma Dynamic• Corporation
7700 Supply / Demand Graph
Margin
Pressure 17.41 PSI
Flow
•
1600 1800
Water Supply ..
Static 126.00 PSI
Residual 124.20 PSI
Elevation 0.00 PSI
5149.85 GPM
's°' ' "
-
@ 1680.00 GPM
~
'--
N1.as
2000
SUBMITI'AL SERIAL N0:4144HY1
laker bldg b roof .20/1500
FLOW TEST RESULTS
Water Supply
STATIC 126.00 PSI
RESIDUAL 124.20 PSI @ 1680.00 GPM
CITY PRESSURE AVAILABLE AT 621.3 GPM 125.71 PSI
SUMMARY OF SPRINKLER OUTFLOWS
ACTUAL MINIMUM
SPR FLOW FLOW K-FACTOR PRESSURE ----------------
100 36.86 24.58 5.60 43.32
101 28.67 24.58 5.60 26.21
102 27.16 24.58 5.60 23.52
103 36.36 24.58 5.60 42.16
104 27.29 24.58 5.60 23.75
105 25.85 24.58 5.60 21.30
106 36.22 24.58 5.60 41.84
107 26.47 24.58 5.60 22.34
108 25.06 24.58 5.60 20.03
110 26.08 24.58 5.60 21.68
111 24.69 24.58 5.60 19.43
113 25.97 24.58 5.60 21. 50
114 24.58 24.58 5.60 19.27
TOTAL WATER REQUIRED FOR SYSTEM 371.25 GPM
OUTFLOWS AT 3 250.00 GPM
TOTAL WATER REQUIREMENT 621.25 GPM
PRESSURE REQUIRED AT 0 108.31 PSI
MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.00 PSI
MAXIMUM VELOCITY FROM 8 TO 9 20.76 FPS
01-04-2006 PAGE 1
SUBMITTAL SERIAL NO:4144HY1 01-04-2006 PAGE 2
loker bldg b roof .20/1500
Location Flow Pipe Fittings Equiv Friction Pressure
in Size & Length Loss Summary
From To GPM IN Devices Ft PSI/Ft PSI
111 114 1,728 L 9.83 C=l20 PT 19.27 (114)
Q 24,58 F=0 F 0.00 PE 0.00
BN T 9.83 0.0168 PF 0.17
108 lllDQ 24.69 1.728 L 9.83 c~120 PT 19.44 (111)
Q 49.27 F=0 F 0.00 PE 0.00
BN T 9.83 0.0607 PF 0.60
105 108DQ 25.06 1.728 L 9.83 C=l20 PT 20.04 (108)
Q 74.33 F=0 F 0.00 PE 0.00
BN T 9.83 0.1298 PF 1.28
102 105DQ 25.85 1.728 L 9.83 C=l20 PT 21. 32 (105)
Q 100.17 F=0 F 0.00 PE 0.00
BN T 9.83 0.2255 PF 2.22
23 102DQ 27.16 1.728 L 123.75 C=l20 PT 23.54 (102)
Q 127.33 F=T, 4E F 23.80 PE 0.00
BN T 147.55 0.3515 PF 51.86
PT 75.40 ( 23) ------------------110 113 1.728 L 9.83 C=l20 PT 21.50 (113)
Q 25.97 F=0 F 0.00 PE 0.00
BN T 9.83 0.0186 PF 0.18
107 ll0DQ 26.08 1.728 L 9.83 C=l20 PT 21. 68 (110)
Q 52.04 F=0 F 0.00 PE 0.00
BN T 9.83 0.0672 PF 0.66
104 107DQ 26.47 1.728 L 9.83 C=l20 PT 22.34 (107)
Q 78.51 F=0 F 0.00 PE 0.00
BN T 9.83 0.1437 PF 1.41
101 104DQ 27.29 1.728 L 9.83 C=120 PT 23.75 (104)
Q 105.81 F=0 F 0.00 PE 0.00
BN T 9.83 0.2495 PF 2.45
22 l0lDQ 28.67 1.728 L 118.75 C=l20 PT 26.20 (101)
Q 134.47 F=T F 9.00 PE 0.00
BN T 127.75 0.3889 PF 49.68
PT 75.88 ( 22) ------------------103 106 1. 728 L 9.33 C=l20 PT 41.84 ( 106)
Q 36.22 F=0 F 0.00 PE 0.00
BN T 9.33 0.0344 PF 0.32
100 103DQ 36.36 1.728 L 9.33 C=l20 PT 42.16 (103)
Q 72.59 F=0 F 0.00 PE 0.00
BN T 9.33 0.1243 PF 1.16
'
SUBMITI'AL SERIAL NO:4144HY1 01-04-2006 PAGE 3
loker bldg b roof .20/1500
Location Flow Pipe Fittings Equiv Friction Pressure
in Size & Length Loss Summary
From To GPM IN Devices Ft PSI/Ft PSI
21 l00DQ 36.86 1.728 L 120.67 C=120 PT 43.32 (100)
Q 109.45 F=T F 9.00 PE Q.00
BN T 129.67 0.2657 PF 34.45
PT 77.77 21) ------------------
22 23 2.703 L 12.50 C=120 PT 75.39 23)
Q 127.33 F=0 F 0.00 PE 0.00
FMl T 12.50 0.0398 PF 0.50
21 22DQ 134.47 2.703 L 12.50 C=120 PT 75.89 ( 22)
Q 261. 81 F=0 F 0.00 PE 0.00
FMl T 12.50 0.1509 PF 1.89
10 21DQ 109.45 2.703 L 1. 75 C=120 PT 77.78 ( 21)
Q 371.25 F=T F 16.70 PE 0.00
FMl T 18.45 0.2880 PF 5.31
9 10 2.703 L 25.00 C=120 PT 83.09 ( 10)
Q 371.25 F=0 F 0.00 PE 0.00
FM T 25.00 0.2880 PF 7.20
8 9 2.703 L 14.83 C=120 PT 90.29 9)
Q 371. 25 F=2E F 13.20 PE 5.13
FR T 28.03 0.2880 PF 8.07
5 8 6.340 L 7.00 C=140 PT 103.49 8)
Q 371.25 F=2E F 46.22 PE 0.00
UN T 53.22 0.0034 PF 0.18
3 5 5.914 L 50.00 C=150 PT 103.67 5)
Q 371. 25 F=2T,3E,DCA F 157.15 PE 0.00
UN T 207.15 0.0042 PF 0.87
6 11 DOUBLE CHECK DETECTOR ASSEMBLY 2.16
1 3DQ 250.00 7.758 L 269.00 C=150 PT 106.70 3)
Q 621.25 F=T, 3GV, E F 98.20 PE 0.00
UN T 367.20 0.0029 PF 1.06
0 1 7.758 L 120.00 C=150 PT 107.76 1)
Q 621. 25 F=T,2GV F 64.98 PE 0.00
UN T 184.98 0.0029 PF 0.54
PT 108.30 0)
LIFEGUARD FIRE PROTECTION, INC.
2605 TEMPLE HEIGHTS DR. STE: F, OCEANSIDE, CA 92056
(760) 806-9997 • FAX (760) 806-4813
Hydraulic Design Information Sheet
Name: LOKER BUSINESS CENTER Date: October 20, 2005
Location: 2708 LOKER AVE WEST
Building: _B"'----------,-----,----,---------System No. .::.R;;.;OccO;;.;F;__ ____ _
Contractor: LIFEGUARD FIRE PROTECTION, INC. Contract No.
Calculated By: LCH Drawing No. 3 OF 3
Construction: 1:8;) Combustible O Non-Combustible Ceiling Height_l_4_-0 _____ F_t __
SYSTEM DESIGN
~ NFPA 13: LJ Light Hazard Ordinary Hazard Group LJ I t;::g 2 LJ 3 LJ Extra Hazard
0 NFPA231 0 NFPA231C: Figure: Curve:
D Other (Specify)
□Specific Ruling Made By Date
Area of Sprinkler Operation 1500 System TYJle
Density .20 [8J Wet □ Dry D Deluge 0 Pre-Action
Area Per Sprinkler 130 SQ.FT. MAX. S11rinkler or Nozzle
Hose Allowance GPM: Inside 0 Make TYCO Model TY-B
Hose Allowance GPM: Outside 250 Size ½ K-Factor: 5.6
Rack Sprinkler Allowance NIA Temperature Rating 200DEG.
CALCULATION SUMMARY
GPM Required -'3'-'7-"0.;..;.8.c.0 ______ PSI Required ....c..10;;.;2:c..4.;..;3;__ _____ At Base of Riser
"C" Factor Used: Overhead 120 Under ound 150
WATER SUPPLY
Water Flow Test Pum11 Data Tank or Reservoir
Date& Time 10-6-05/10:15 AM Rated Capacity Capacity
Static PSI 140 At PSI Elevation
Residual PSI 138 Elevation
GPMFlowing 1680 Well
Elevation 0 Proof Flow GPM
Location SITE
Source Qf Information LIFEGUARD FIRE WITH CARLSBAD FIRE
I :I I II II I .. ~TOR ... ,-.-r,
Commodity Class Location
Storage Height Area Aisle Width
Storage Method: Solid Piled % Palletized %Rack
Rack D SingleRow D Conventional Pallet 0 Automatic Storage D Encapsulated D DoubleRow D Slave Pallet 0 Solid Shelving D Non-Encapsulated D Multiple Row □ Open
Flue S11acing In Inches Clearance From To11 ofStorl!ge to Ceiling
Longitudinal Transverse Ft. In.
Horizontal Barriers Provided
250
240
230
220
210
200
190
180
170
160
150
140
130
120
110
100
90
80
70
60
50
40
30
20
10
loker bldg b roof .20/1500
I • •
U, 88 t --. I f
I! I
~
Q
0200 400 600 800 1000 1200
System Demand ..
Sprinkler Demand 108.88 PSI@
Additional Flows
Hose at Source
Total Demand 109.86 PSI@
370.80 GPM
250.00 GPM
0.00 GPM
620.80 GPM
1400
Water Flow (GPM)
Sigma Dynamic■ Corporation
7700 Supply/ Demand Graph
Margin
Pressure 15.85 PSI
Flow
•
. --1600 . --1800
Water Supply ..
Static 126.00 PSI
Residual 124.20 PSI
Elevation 0.00 PSI
4870.27 GPM
rs\
@ 1680.00 GPM
~
~
N1.as
2000
SUBMITTAL SERIAL N0:4144HY1
loker bldg b roof .20/1500
FLOW TEST RESULTS
Water Supply
STATIC 126.00 PSI
RESIDUAL 124.20 PSI @ 1680.00 GPM
CITY PRESSURE AVAILABLE AT 620.8
SUMMARY OF SPRINKLER OUTFLOWS
ACTUAL MINIMUM
SPR FLOW FLOW K-FACTOR --------
100 36.50 24.58 5.60
101 28.80 24.58 5.60
102 27.16 24.58 5.60
103 36.01 24.58 5.60
104 27.42 24.58 5.60
105 25.85 24.58 5.60
106 35.87 24.58 5.60
107 26.59 24.58 5.60
108 25.06 24.58 5.60
110 26.19 24.58 5.60
111 24.69 24.58 5.60
113 26.08 24.58 5.60
114 24.58 24.58 5.60
TOTAL WATER REQUIRED FOR SYSTEM
OUTFLOWS AT 3
TOTAL WATER REQUIREMENT
PRESSURE REQUIRED AT 0
MAXIMUM PRESSURE UNBALANCE IN LOOPS
MAXIMUM VELOCITY FROM 8 TO 9
GPM 125.71 PSI
PRESSURE --------
42.49
26 .44
23.52
41.35
23.97
21.30
41.04
22.54
20.03
21.88
19.43
21. 70
19.27
370.80 GPM
250.00 GPM
620.80 GPM
109.87 PSI
0.00 PSI
20.73 FPS
10-19-2005 PAGE 1
SUBMITTAL SERIAL NO:4144HY1 10-19-2005 PAGE 2
loker bldg b roof .20/1500
Location Flow Pipe Fittings Equiv Friction Pressure
in Size & Length Loss Summary
From To GPM IN Devices Ft PSI/Ft PSI
111 114 1. 728 L 9.83 C=120 PT 19.27 (114)
Q 24.58 F=0 F 0.00 PE 0.00
BN T 9.83 0.0168 PF 0.17
108 lllDQ 24.69 1.728 L 9.83 C=120 PT 19.44 (111)
Q 49.27 F=0 F 0.00 PE 0.00
BN T 9.83 0.0607 PF 0.60
105 108DQ 25.06 1.728 L 9.83 C=120 PT 20.04 (108)
Q 74.33 F=0 F 0.00 PE 0.00
BN T 9.83 0.1298 PF 1.28
102 105DQ 25.85 1. 728 L 9.83 C=120 PT 21. 32 (105)
Q 100.17 F=0 F 0.00 PE 0.00
BN T 9.83 0.2255 PF 2.22
23 102DQ 27.16 1.728 L 107.75 C=120 PT 23.54 (102)
Q 127.33 F=T,4E F 23.80 PE 0.00
BN T 131.55 0.3515 PF 46 .24
PT 69.78 ( 23)
------------------
110 113 1. 728 L 9.83 C=120 PT 21. 70 (113)
Q 26.08 F=0 F 0.00 PE 0.00
BN T 9.83 0.0187 PF 0.18
107 ll0DQ 26.19 1.728 L 9.83 C=120 PT 21. 88 (110)
Q 52.28 F=0 F 0.00 PE 0.00
BN T 9.83 0.0677 PF 0.67
104 107DQ 26.59 1. 728 L 9.83 C=120 PT 22.55 ( 107)
Q 78.87 F=0 F 0.00 PE 0.00
BN T 9.83 0.1449 PF 1.42
101 104DQ 27.42 1.728 L 9.83 C=120 PT 23.97 (104)
Q 106.28 F=0 F 0.00 PE 0.00
BN T 9.83 0.2516 PF 2.47
22 101DQ 28.80 1.728 L 102.75 C=120 PT 26.44 ( 101)
Q 135.08 F=T F 9.00 PE 0.00
BN T 111.75 0.3921 PF 43.82
PT 70.26 ( 22) ------------------103 106 1. 728 L 9.33 C=120 PT 41.04 ( 106)
Q 35.87 F=0 F 0.00 PE 0.00
BN T 9.33 0.0337 PF 0.31
100 103DQ 36.01 1.728 L 9.33 C=120 PT 41.35 (103)
Q 71. 89 F=0 F 0.00 PE 0.00
BN T 9.33 0.1221 PF 1.14
SUBMITTAL SERIAL NO:4144HY1 10-19-2005 PAGE 3
loker bldg b roof .20/1500
Location Flow Pipe Fittings Equiv Friction Pressure
in Size & Length Loss Summary
From To GPM IN Devices Ft PSI/Ft PSI
21 l00DQ 36.50 1.728 L 104.67 C=120 PT 42.49 (100)
Q 108.39 F=T F 9.00 PE 0.00
BN T 113.67 0.2609 PF 29.66
PT 72.15 21)
------------------
22 23 2.703 L 12.50 C=120 PT 69.76 23)
Q 127.33 F=0 F 0.00 PE 0.00
FMl T 12.50 0.0398 PF 0.50
21 22DQ 135.08 2.703 L 12.50 C=120 PT 70.26 ( 22)
Q 262.41 F=0 F 0.00 PE 0.00
FMl T 12.50 0.1516 PF 1. 90
10 21DQ 108.39 2.703 L 1. 75 C=120 PT 72.16 ( 21)
Q 370.80 F=T F 16.70 PE 0.00
FMl T 18.45 0.2874 PF 5.30
9 10 2.703 L 41. 00 C=120 PT 77.46 ( 10)
Q 370.80 F=0 F 0.00 PE 0.00
FM T 41.00 0.2874 PF 11.78
8 9 2.703 L 14.83 C=120 PT 89.24 9)
Q 370.80 F=2E F 13.20 PE 5.13
FR T 28.03 0.2874 PF 8.06
5 8 6.340 L 7.00 C=140 PT 102.43 8)
Q 370.80 F=2E F 46.22 PE 0.00
UN T 53.22 0.0034 PF 0.18
3 5 5.914 L 50.00 C=150 PT 102.61 5)
Q 370.80 F=T,4E,DCA F 132.50 PE 0.00
UN T 182.50 0.0042 PF 0.77
6 11 DOUBLE CHECK DETECTOR ASSEMBLY 4.89
1 3DQ 250.00 7.758 L 269.00 C=150 PT 108.27 3)
Q 620.80 F=T, 3GV, E F 98.20 PE 0.00
UN T 367.20 0.0029 PF 1.06
0 1 7.758 L 120.00 C=150 PT 109.33 1)
Q 620.80 F=T, 2GV F 64.98 PE 0.00
UN T 184.98 0.0029 PF 0.54
PT 109.87 0)
LIFEGUARD FIRE PROTECTION, INC.
October 6, 2005
Carlsbad Fire Department
1635 Faraday Ave.
Carlsbad, CA 92008
Fax (760) 602-8561
Re: Loker Business Center Phase I
Carlsbad, CA
Fire Protection Design & Installation .........
The following are results from a fire flow test performed for the proposed Loker Business Center in Carlsbad,
CA. The test was conducted by Lifeguard Fire Protection, Inc. and witnessed by the Carlsbad Fire Department
and the water department. The test was conducted on hydrants located on Loker Ave West near the intersection of
Palomar Airport Rd. and Loker. The results are as follows:
Date:
Time:
Static:
Residual:
Pitot:
Port:
Flow:
Hydrant C:
Please call if you have any questions.
;::_~
Chuck Hollands
Lifeguard Fire Protection, Inc.
October 6, 2005
10:15 AM
140 psi
138 psi
100 psi
2 ½"
1680 gpm
.90
2605 TEMPLE HEIGHTS DRIVE .& SUITE F .& OCEANSIDE, CA 92056 .& 760/806-9997 .& FAX 760/806-4813
ES-A-3000SS
Series 3000SS A
AMES
Double Check Detector Assemblies
Sizes: 2½" -12" (65 -300mm)
l"IRIE •WATll:RWORK■
Features
• Patented Cam-Check Assembly valve
provides low head loss
• Short lay length is ideally suited for
retrofit installations
• Stainless Steel body is half the weight
of competitive designs reducing
installation and shipping cost
• Stainless steel construction provides
long term corrosion protection and
maximum strength
• Single top access cover with two-bolt
grooved style coupling for ease of
maintenance
• No special tools required for servicing
• Compact construction allows for
smaller vaults and enciosures
• Furnished with %' x ¾' bron"8 meter
(gpmorcfm)
• Detects underground leaks and unsuthorlZed water use
• Maybe Installed horizontal or vertical
"flow up• position
Available Models
Suffix:
LG -less shutoff valves
OSY -UL/FM outside stem end yoke
res!Hent eeated gate valvee
'OSY FxG -flanged Inlet gale COi o iectlon aoo
grooved outlet gat'e connection
·osv GxF -grooved Inlet gate connection
end flanged outlet gate connec--·osv GxG -grooved Inlet gale COi o -· -grooved outlet gate connection
CFM -cubtc feet w minute
GPM -gallons per minute -
Available with grooved NRS gate valves -
consult factory*
Post Indicator plate aoo operating nut
available -consul factory'
'Consult factory for dimensions
Series 3000$8 Double Check Detector Assemblies are designed for use in accordance
with water utility non-health hazard containment requirements. It is mandatory to
prevent the reverse flow of fire protection system substances, i.e., glycerin wetting
agents, stagnant water and water of non-potable quality from being pumped or
siphoned Into the potable water supply.
Specifications
A Double Check Detector Assembly shall be Installed on fire protection systems when
connected to a potable water supply. Degree of hazard present Is determined by the
local authority having Junsdlctlon. The main valve body shall be manufactured from
300 Sen es stainless steel to provide conroelon resistance, 100% lead lr8e through the
waterway. The double check detector assembly consists of two ~ operating,
spring loaded check valves, two UL, FM, OSY resilient seated gate valves, and bypass
assembly. The bypass assembly consists of a mater (cubic ft. or gallons), a double check
Including shutoff valves and required test cocks. Each cam-check shall be Internally
loaded and provide a positive dnp tight closure against reverse flow. Cam-check
Includes a stainless steel cam arm and spring, rubber faced disc and a replaceable
seat. There shall be no brass or bronze parts ueed within the cam-check valve
assembly. The check valve seats shall be of molded lhennoplastic conatructlon. The
use of seat SCl8W8 aa a retention method Is prohibited. All Internal parts shall be
accesslble through a single cover on the valve assembly. The valve cover shall be held
In place through the use of a single grooved style two-bolt coupling. The bypass line
shall be hydraulically sized to accurately measure low flow. The bypass line shall con-
sist of a mater, a small diameter double check assembly with -cocks and Isolation
valves. The bypass line double check valve shall have a single access cover, two
Independently operating modular poppet check valves, and lop mounted test cocks.
The assembly shall be an Ames 3000SS.
Materials
All Internal metal parts: 300 Serles stainless steel, Main valve body: 300 Serles stanless
steel, Check assembly: Noryl" Flange dimension In accordance with AWWA Class D.
No,yl" Is a registered trademark of General 8ectrfc Company.
Job Name _________________ Contractor
Job Location Approval ----------------
Engl.-ContraciD"sP.O. No. ____________ _
Approval _________________ Representa11ve ______________ _
Ames product apaclflcations In U.S. cummary 1,111ts and meb'lc are approximate and are provided fof r8fnnce ony. fo.r preolse m8B8l1'81tlents, please contact Ames Technical Service. Ames reaerves the right to r.hanQe or modfy product design, conatructlon, 8')8Clflcatlons, or materials Ytffl1out prior notice and Mlhout Incurring any obligation to make such changes and modllcatlona on Ames products pmiously or
-yojd, www.amesfirewater.com
Pressure -Temperature
Temperatun, Range: 33°F -110'F (S'C -43'C)
Maximum Working Pressure: 175psi (12.06 bar)
Capacity
Flow curves as tested by Undelwritors Laboratory per UL 1469,
1996. • Rated flow -UL Tested
St.anclards
AWWAC510-92, UL 1469
Approvals
For 12• approvals consult factory.
9 ~ ~
cOOus
1048 (alzN 2'/z" -10", (OSY Dnly)
.,, 2¼" (65mm) 0SY om,)
nwJ I I I I I Ettl ng1 111 llTI kl R4l
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95 190 B 570 160 ll50 1140 1330 1520 1710 111111 1995 -380 760 1140 1520 191111 2280 2680 3040 3420 3800 4180 4560 4840 5320 5700 -
15 ... 5 10 16 ...
4.1 ... 1.5 :, 4.1 ..
... .. 3• (80mm) • •• ... .. a· (200mm) • R ~ rntu 111 W HIHd ~ lf 11111 t 111 ti
O 25 50 1110 150 200 250 300 350 400 450 500 550 600 -0 250 500 750 1000 1250 1500 1750 2000
95 1911 S80 570 760 ISO 1140 1330 1520 1710 1900 20802280. 950 1900 2950 3800 4750 5700 8650 7800 ""' ""' ... "" ... "" " "' ..... 11 • 5 10
4.1 • 1.5 3
~:PW 111 llT'I W lffl nt~ 111 lD' 1 IHII
0 50 100 150 200 250 300 350 -400 450 500 550 800 650 700 750 1111111 O 250 500 750 1000 1250 1500 1750 2000 2250 2500 3000 3500 DIii
9500 11400 13300 ,._ 111 380 1110 no 950 1140 1330 1520 1110 11100 20eo 2280 2,110 :zeilo2850 11n 950 1900 2850 3800 4750 5700 6850 7800 8550
5 1011 (pl 5 10 "' 1.5 3 4.1 lllpl 1.5 ' ...
"' .. 12" (300mm)
C
(Open)
1 ~lb-t I 1-1 I E~fi1 .. , .. , .. ... , .. ,..
5700 ,..,
,.. ... ,.. ,, .. ,.. -13300 15200
......
17100 (IIII
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' "' ...
...
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3
4
6
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A
In. ...
37 965
38 965
40 1016
48¼ 1232
52¼ 1
55¼ 1410
7'1, 1461
AMES
C (1)SV)
in. mm
16'/, 416
18'/, 479
22'I, 78
301/e 765
7¾ 959
45'/, 1162
53¼ 1349
In. ...
3'1, 89
3'/, 95
4½ 114
5'h 140 ,,, 171
8 200
9¼ 241
In.
10
10
10
15
1
15
15 I IMPORTANT: Inquire with governing authorities for
local lnslal/ation requirements.
PlRIE•WATIERWORU A Division of Watts Regulator Company ~MS1 1 www.amesfirewater.com -.
1427 North Market Blvd. • Suite #9 • Sacramento, CA 95834 • Phone: 916-928-0123 • Fax: 916-928-9333
ES-A-3000SS 0513 CAmes Co. 2005
PWEagle
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Why more specifiers choose PW Eagle C900 for
potable water systems.
PW Eagle is one of the largest
producers of PVC pipe in North
America, am;l our products
are available from distributors
throughout the Untted States.
PW Eagle produces PVC pipe
for a variety of applications
servicing the potable water, well
casing, sewer, turf, agriculture,
plumbing, communications and
2
electrical marl<ets. Our eleven
manufacturing faciltties In Oregon,
Washington, California, Utah,
Nebraska, Texas, Missouri and
West Virginia assure on-time delivery.
PW Eagle C905 high pressure water
pipe combines superior materials wtth
the latest manufacturing technology.
PW Eagle products meet or exceed
industry standards because of our
rigorous quality-control program.
PW Eagle supports the PVC pipe
industry's efforts to maintain the
highest design and manufacturing
standards. We are members of the
Uni-Bell PVC Pipe Association and
American Water Works Association
(AWWA).
Corrosion Resist-ce
C900 is immune to nearly all types
of internal and external corrosion.
Since PVC is a non-conductor, it is not
affected by electrolysis. Nor is it sus-
ceptible to alkaline or acid soil condi-
tions. A correctly installed PW Eagle.
system will provide long-term service
at reduced operating costs.
Water Quality
Extractant water purity tests
performed by independent test
laboratories ensure that our pipe
meets the requirements for water
purity as specified by ANSI/NSF
Standard 61.
Superior now
Characteristics
An extremely smooth inner surface
gives C900 a Hazen-Williams flow
coefficient of C=150. This means less
burden on pumps and reduced
pumping costs, because thera's less
friction between moving water and
pipe walls.
Am111foanW.191'Woru
~lll!MHII
Exceptional Strength a:ncl
DurlihWty
Every piece of C900 is hydrostatically
proof tested at four times its pressure
class.
A 2.5-to-1 safety factor is applied
to the long-term pressure capacity of
the pipe. The resulting value is further
reduced by a surge pressure value,
which also incorporates a 2.5-to-1
safety factor. Burst test pressure
capabUity of C900 Class 150 is at
least 755 psi, with sustained pressure
test capability of 500 psi.
Throughout the country, in all
conditions and climates, COOO has
served admirably in municipal water
mains, fire lines, and sewage force
mains.
Joint Integrity
PW Eagle's integral bell gasketed
joint meets the same strength
requirements of the C900 pipe, as
well as the demanding test criteria of
ASTM D 3139. The ability of PVC to
bend without breaking allows the joint
and pipe assembly to compensate for
minor earth movement, which
can cause problems in more rigid,
non-PVC assemblies.
Certification
COOO is periodically tested to maintain
listings from Factory Mutual System•
(FM) and Underwriters Laboratories
(UL). C900 also conforms to
applicable requirements of the
Uniform Plumbing CodeN.
•Factory Mutual is not applicable to
Class 100, DR 25 products.
◄FM ► @LISTED
Basic Assembly Instructions
1. 2. 3.
3
Factors Affecting Design
Hydraulics
C900's pipe wall is extremely
smooth and energy-efficient. It has a
Hazen-Williams coefficient of C=150.
Class 100 DR 25
Nominal A-
Pipe Size 0utskle Diameter
Pnc'-l (Inches)
4 4.80
6 6.90
8 9.05
10 11.10
12 13.20
Class 150 DR 18
Nominal A-•
Pipe Size 0utakkt Diameter
(Inches) (Inches)
4 4.80
8 6.90
8 9.05
10 11.10
12 13.20
Class 200 DR 14
Nominal A_,,,,e
Pipe Size Outaide Diameter
Pnchesl pncMO)
4 4.80
6 6.90
8 9.05
10 11.10
12 13.20
Pressure ClaBB
PW Eagle offers a choice of three
pressure classes (100, 150, and 200)
which can be used where operating
pressures do not exceed the pressure
Approximate* Minimum
Inside Diametmr Wall ThlcknNa
(Inches) Pnchesl
4.38 0.192
6.30 0.276
8.27 0.382
10.15 0.444
12.07 0.528
Appn>Jdmate• Minimum
Inside Diame1Br Wall ThlcknNa
Pnc'-l pncMO)
4.22 0.267
6.08 0.383
7.97 0.503
9.78 0.817
11.83 0.733
Appn>Jdmate• Minimum
Inside Diameter Wall ThlcknNa
r,ncMO) fine'-)
4.08 0.343
5.84 0.493
7.86 0.646
9.40 0.793
11.18 0.943
'These figureo alow for rnanulac:llmg toleranoes. ~-shown Is for mlemnce pt.-poees orly.
4
class plus surge allowances. When
you have questions or encounter
unusual circumstances, call a
PW Eagle representative.
Temperature
For operation at temperatures 80"F or
higher, multiply the pressure class by
these derating factors:
T_....., Deratlng Factor
80' 0.88
90· 0.75
100' 0.62
111r o.50
120' o.40
140" 0.22
Approxlmato Appn>Jdmate
Weight C,.-Weight
llba/100 ft) Pbol
190 1870
380 1380
660 1890
1010 1610
1410 1690/2250
ApproJdmat8 Appn>Jdmate
Weight Crate Waight
Pba/100 ft) Pbol
260 2470
520 1860
890 2880
1340 2150
1910 229Ql3050
--Approximate
Weight C,.-Weight
Pba/100 fl! Pbol
320 3080
650 2350
1120 3350
1890 2710
2400 2880/3850
Product Description
Standard Specifications
Material
PVC compound meets
ASTM D 1784, cell class 12454.
Pipe
Meets AWNA C900. Class 100
meets requirements of DR 25.
Class 150 meets requirements of
DR 18. Class 200 meets
requirements of DR 14.
Elastromeric Seal
Integral bell pipe provided with
factory-installed gaskets meeting
requirements of ASTM F 477.
Gasketed Joint Assembly
Meets requirements of ASTM D 3139.
Installation
AWNA C605 and PN Eagle's
Installation Gulde for PVC Water Pipe.
Quality Assurance
Hydrostatic Proof Testing
Each standard and random length
of C900 is tested to four times the
pressure class of the pipe, for a
minimum of five seconds. The integral
bell is tested with the pipe.
Falling Weight Impact Test
C900 withstands an impact energy
of 100 ft-lbs, per the requirements
of UL 1285.
Quick Burst Test
Randomly selected C900 samples
are tested in accordance with
ASTM D 1599 to withstand pressures
listed below. Class 100 has a
minimum burst pressure of 535 psi;
Class 150, a minimum burst pressure
of 755 psi; Class 200, a minimum
burst pressure of 985 psi.
Product
C900 is suitable for use as a pressure
conduit. Expansion and contraction
are accommodated by a property
assembled gaskeled joint. Each bell
section meets the same pressure
capacity requirements as the pipe.
Standard laying lengths are 20 feet
(plus or minus 1 inch).
Pip,. Slilfr n a
C900 meets these minimum stiffness
requirements:
-Clua DR
100 25 129
150 18 364
200 14 814
JOINT INTEGRITY HYDROSTATIC PROOF TEST
5
Installation
Pipe Emhedment
All PVC pipe should be installed
with bedding that provides un~orrn
longltudinal support under the pipe.
Use embedment material that is free
of large stones, frozen matter, or
other debris. Use proper compaction
procedures to provide soil densities
as specified by the design engineer.
Service Connections
Direct Tapping: Direct taps may be
made in C900 Class 150 and Class
200 in nominal sizes 6 inch through
12 inch. Corporation stops should be
in sizes %, ¾, or 1 inch. When sizes
larger than 1 inch are requirad,
tapping saddles or sleeves should
be used.
Saddle Tapping: Saddle taps
may be made in any size or class
of C900 pipe. Maximum outlet size
recommended for saddle taps is 2
inches. FQI' sizes larger than 2 inches,
a tapping sleeve should be used.
Tapping Sleeves: Tapping sleeves
may be used on all sizes and classes
of C900. Sleeves are available up to
size-on-size.
Caution: Saddles and sleeves
should not:
• Distort the pipe when tightened
• Have lugs that dig Into the pipe
when the bolts are tightened
• Have a clamping arrangement
not fully contourad to the outside
diameter of the pipe
For more information on tapping,
see Uni-Bell's tapping video and
publications Uni-B-8 and Uni-Pub-8.
6
Table 1. Thrust Developed per 100 psi Pressure
AWWA C900 PVC Prvs un P1µe (C IO DI
Nominal Pipe Size Fitting SKr Elbow Fitting 45" Elbow Valves, T ... , Dead Ends
Onchee) {lbs force) Oba force) Obatorce)
4 2,160 1,180 1,530
6 4,460 2,420 3,160
8 7,700 4,160 5,440
10 11,600 6,260 8,190
12 16,400 8,680 11,800
Table 2. Estimated S01I Bearing Capacity -~
Muck, Peat, Etc. 0
Soft Clay 500
Sand 1,000
Sand and Gravel 1,500
Sand and Gravel With Clay 2,000
Sand and Gravel eer-rtad With Clay 4,000
Hald Pan 5,000
Note: Values are estimated for horizontal tlYusls at dep1hs of burial which exc-1 2 feet.
Note: These v,;ues should be used ex,~ for estimating purposes. l/alues for design should be
datermlned by an engl.-familiar with site soil conditions.
Longitudinal
Bending
Axial deflection at the pipe joints is not
recommended, However, it is possible
to curve C900 to allow for slight
changes In direction.
Bending to these minimum radii
will not jeopardize COOO's design
capability. See Pvv Eagle's Technical
Bulletin "Longitudinal Bending of PVC
Pipe" for more details.
-Pipe Size
(Inches)
4
6
6
10
12
-Bending Radius
~NII
100
145
190
235
275
Thrust Restraint
Adequate thrust restraint is
necessary for all gasketed joint
systems. The "push on' features of
our joints provide many installation
advantages, but without adequate
thrust restraint they can become
"push off' problems. The large thrust
forces present in water-distribution
systems (see Table 1) require thrust
restraints designed to handle test and
peak operating pressures.
THRUST BLOCKS
FIGURE 1: Through line connection, tee
Concrete Thrust Blocks
If concrete thrust blocks are used,
the size and type of thrust blocking
must be based on the load-bearing
capecity of the soil, pressure in the
pipe, and diameter of the pipe. Table
2 provides conservative ~mates of
load-bearing values for various soil
types. When soil conditions are not
known, samples should be tested to
determine soil properties.
FIGURE 2: Direction change, elbow
MECHANICAL THRUST RESTRAINT DEVICES
FIGURE 4: Through line connection,
cross used as tee
FIGURE 5: Direction change, elbow
Mechanical Restraints
If mechanical thrust restraint devices are
used, they should be a type designed
for use with PVC pipe. The devices
should meet the test requirements of
Uni-Bell's Specification Uni-8-13 "Joint
Restraint Devices for Use with PVC
Pipe." Design manuals and computer
software are available from the restraint
manufacturers.
For typical thrust blocking and
mechanical thrust restraint examples,
see Rgures 1 through 6.
FIGURE 3: Change line size, reducer
FIGURE 6: Direction change, tee
used as elbow
7
'
Testing of Installed Systems
Place sufficient backfill before
pipe filling and field testing. Under
conditions requiring immediate back-
filling of trenches, test after backfilling
but prior to placement of permanent
surface. Testing short lengths of pipe
first will verify proper installation and
joint assembly. ~ concrete thrust
blocks are required, allow sufficient
curing before testing.
Separate tests for pressure and
leakage may be perfonned. If
separate tests are done, the pressure
t~st should be done first. See Table 4.
Procedure
While the line is under pressure,
check for leaks in all exposed pipe,
fittings, valves, and hydrants. Repair
or replace all defective elements.
Repeat the test until all visible leaks
stop and the allowable leakage
requirements are met, per Table 5.
For detailed pressure-testing
requirements, consult your engineer
or the PW Eagle installation guide.
WARNING: Do not UH PVC pipe for
presaurlzed air systems. Injury or
death may reault due to the cata ..
atrophic nature of pipe failure ahould
failure occur. Rapid expansion of
compreuad air could propel shards
of plaltlc throughout the area.
WARNING: Expel all air from tho
plpellne during fllllng and again be-
fore testing for presaure or leaks.
Automatic air-release valvu ae rec-
ommended. Compreased entrapped
air can greatly ampllty surges or
pumping pre■-ure■. Also, com-
pre11ed air might leak through a
Joint that wlll not leak water.
Table 3. Volume of Water Required for Testing
-Pipe-Appn,xlmata-
(Incl-> (U.8-ga1t1QO 111
4 70
6 153
8 259
10 405
12 573
Table 4. System Test Methods
Pro<:ed\1'9 Proaurw Tnt Duration
Simultaneous pressure 150% of working pressure at point of test, 2hr
and leakage tests but not less than 125% of normal workJng
pressure at highest elevation•
Separate pressure test 150% of working pressure at point of test, 1 hr
but not less than 125% of normal working
pressure at highest elevation*
Separate leakage test 150% of working pressu,e of segment tested• 2hr
SoulCO: Underground lnst,;lation of PvC Pressure Pipe and Fittings fol' Wmw, AWWA C605.
U1def oo circuns1ances should test pressures exceed 305 psi fol' DR 14, 235 psi fol' DR 18, and
165 psi fol' DR 25 COOO PvC p~.
Table 5. Allowable Leakage per 50 Joints
U $ G tllrn1s f.)L'f Hnur
Nominal Pipe Size Average Test Pl'Hliure (paQ
finches) 50 100 150 200 250 300
4 0.19 0.27 0.33 0.38 0.43 0.47
6 0.29 0.41 0.50 0.57 0.64 0.70
8 0.38 0.54 0.68 0.76 0.85 0.94
10 0.48 0.68 0.83 0.96 1.07 1.17
12 0.57 0.81 0.99 1.15 1.28 1.40
1111§§
PWEagle P.O. Box 10049, Eugene, OR 97440 • (800) 347-0200 • (541) 343-0200 • FAX (541) 686-9247 • www.pweagleinc.com
Utho In USA on Fllcycled ~ • R8otder No. MKr-F-730---AIMsed J!Jy 2004