HomeMy WebLinkAboutReg 2011-10-03 Item 6A - Blue Star - Attachment J - Fire Safety Analysis for Blue Star Gas Prepared by GT Engineering Dated 6/13/2011G T ENGINEERING
FIRE SAFETY ANALYSIS
BLUE STAR GAS SEATTLE, CO.
PREPARED BY:
Adam Farnham, P.E., C.S.P.
Sr. Fire Protection Engineer
GT Engineering
Redmond, Washington
June 13, 2011
Attachment 3
'18372 Redmond -Fall City Road Redmond, WA 98052 Tel 425- 556 -5555 Fax 425 556 -5556 www.gt -engineering.com
PROJECT LOCATION: 10802 East Marginal Way South
Tukwila, Washington
FACILITY PURPOSE: Liquefied Petroleum Gas (LPG) storage, fleet dispensing
and bulk distribution
CONSTRUCTION FEATURES:
1 30,000 gallon water capacity ASME compliant
horizontal product storage tank
1 —1150 gallon water'capacity ASME compliant vertical
product storage tank
Two position fleet fueling island
Office building
CODE COMPLIANCE:
2009 International Building and Fire Codes
NFPA 58 2011 ed. Liquefied Petroleum Gas Code
NFPA 15 2007 ed. Standard for Water .Spray Fixed
Systems for Fire Protection
NFPA 24 2007 ed. Standard for the Installation of
Private Fire .Service Mains and their Appurtenances
NFPA 70 2008 ed. National Electrical Code
PURPOSE AND BASIS
The purpose of this Fire Safety Analysis (FSA) is to determine the overall safety of the
facility, including any fire protection features provided beyond the specific requirements
of NFPA 58. This FSA is based on the procedure recommended in Fire Safety Analysis
Manual for LP -Gas Storage Facilities (2008) which is published by the NFPA and
National Propane Gas Association.
Additional information is contained in the following appendices, which are attached to
this report:
1. A Fire Safety Analysis Forms
2. B Site Improvement Drawings
3. C Piping Schematics
4. D Equipment Specifications
FACILITY INFORMATION
The overall facility layout and site improvements are shown in the attached drawings in
Appendix B "Site Improvement Drawings for Blue Star Gas Seattle, Co". Individual
storage tank data, facility information and contacts are shown in Forms 4.1, 4.2 and 4.3,
which are attached in Appendix A. The facility will be a fenced bulk receiving and
distribution center. It will take product delivery from tanker trucks and distribute product
via local delivery vehicles. A fleet fueling island will also be supplied from a vertical
product tank via underground product lines. The facility is located on a paved, level lot
2
and will have a manufactured office building staffed during regular business hours for
administrative and access control purposes.
PRODUCT CONTROL
Product filling and distribution to /from the horizontal storage container will be via the
piping schematic shown in Appendix C. The liquid and vapor lines for the storage tank
service a bulk filling rack.
An analysis of the code requirements for the bulk filling system tank appurtenances is
shown on Appendix A, Form 5.4. The tank will be provided with NFPA 58- required
redundant fail -safe product control valves.
LPG transfer piping will be protected by product control systems. The horizontal tank
will be provided with internally- mounted excess flow valves, which will automatically
shut off if the flow exceeds 250 gpm. Similarly, product piping to the distribution system
will be provided with excess flow valves.
An emergency shutoff valve (ESV) will be provided on the liquid line at the distribution
and receiving filling rack. The ESV will be provided with a fusible link automatic
shutoff, set to actuate at approximately 250 F. A manual shutoff feature and manual
emergency shutoff at a remote location will also be provided. ESVs will also be installed
on the vapor transfer lines on both the distribution and tank filling systems.
Breakaway stanchions will be provided for the filling connections. These will provide
protection in the event of vehicle movement while the transfer hoses are still attached.
Appendix A, Form 5.8 summarizes the redundant, fail -safe equipment provisions. The
facility will use low emission transfer equipment on all points of connection. This will
minimize both vapor emissions to the atmosphere and product released during hose
connect/disconnect operations. Low emission transfer equipment provisions are
summarized in Appendix A, Form 5.9. Automatic closure of product control valves on
both the liquid and vapor lines will occur in the event of fire or hose pull -away. The
remote .shutdown equipment will de- energize the electrical power supply for the transfer
pump, as well as closing all valves.
Signs will be posted at the facility advising of the no smoking policy and emergency
shutdown procedures.
PHYSICAL PROTECTION
Physical protection features are summarized in Appendix A, Form b.1.
Lighting will be provided for nighttime operations. This will include illumination for the
storage container, vehicle being loaded /unloaded, control valves and other equipment on
site.
Vehicle impact protection will be provided. A perimeter fence will be installed around
the facility, with a separate fence isolating the horizontal storage tank. Two openings
Will be provided in the perimeter fencing to allow emergency access. A minimum 3 foot
clearance will be maintained around all means of egress.
3
OTHER CONTROLS
An ignition source control assessment is summarized in Appendix A, Form 6.2. No
combustible foliage will be present. No other types of fuel will be dispensed at the
facility. Electrical equipment will be installed to the requirements of NFPA 70. Portable,
dry chemical extinguishers will be provided at each fuel transfer location. Smoking will
be prohibited at the facility.
Separation distances will be provided in accordance with NFPA 58, Tables 6.3.1 and
6.5.3. These are summarized in Appendix A, Forms 6.3 and 6.4.
FIRE PROTECTION
Fire protection features are summarized in Appendix A, Form 6.6. A fixed monitor
nozzle will be provided. A Firepro Model FP4 -750 monitor (or approved equivalent)
with a Firepro Model FP -500B (or approved equivalent) master stream nozzle will be
positioned to the south of the horizontal tank installation. The monitor nozzle will be
positioned such that it can effectively wet the exposed tank surface area and
appurtenances.
A listed deluge control valve will actuate the monitor, in.accordance with NPFA 15,
paragraph 5.7.1. The deluge control valve will be actuated by either automatic flame
detection or manually by a release on the pneumatic actuation system.
In addition, the deluge system will be provided with afire department connection at the
public way. The connection will be provided in compliance with NFPA 15, paragraph
5.10 and consist of two 2 %z inch diameter hose connections. This connection will
provide water downstream of the deluge valve and allow a redundant backup water
supply.
A flame detection system will be provided to monitor the horizontal tank. When a fire is
sensed, the system will sound a local alarm, close product control valves, stop power to
the transfer pump and actuate the monitor. The flame detection and alarm system will
use equipment listed and approved for this function. The system will transmit the alarm
to a central station monitoring facility for fire department notification.
EXPOSURE EVALUATION
An evaluation of hazards to exposed properties from an in -plant LPG release is
summarized in Appendix A, Form 7.2 using data from Form 7.1. Adjacent occupancies
within 250 ft of the facility's property line include:
1. A supply warehouse /garage —100 ft north
2. Sound Transit Light Rail Overhead guideway at 40 ft. elevation approximately
27 ft south of east storage tank.
3. Warehousing Gene Juarez distribution center approximately 200 ft. south.
4. Police training facility approximately 250 ft southeast.
5. South Boeing Access Rd 200 ft. north
6. East Marginal Way South West side of property
2
7. Chevron fuel station 200 ft. west. An event at this fuel station could possible
pose a hazard for the LPG facility. However, separation distance is sufficient that
a conceivable fuel release and fire would likely have a negligible impact on the
temperature of product stored in the LPG containers.
No assembly, institutional or educational occupancies are exposed by this facility. Fixed
population densities are low. Transient population densities vary, depending upon the
time of day. It is estimated that a maximum of 220 people could be present on one two
car light rail train. The light rail operates every 7.5 minutes during peak periods. Trains
traverse the overhead guideway at the facility on a two -track system. The rail cars are
operated by trained personnel. The extent of training of the staff is not known.
The number of persons in automobiles adjacent to the facility also varies depending upon
the time of day. An intersection to the northwest of the facility is busy most of the day.
The number of vehicles transiting the adjacent roads is not known. Facility exposure to
and from these transportation modes is low.
FIRE DEPARTMENT
This location is served by the City of Tukwila Fire Department.
WATER SUPPLY
Fire protection water will be supplied from the City of Tukwila. The water main in East
Marginal Way South, which is immediately west of the project site, is reported to be able
to supply a static pressure of 120 psi and a residual pressure of 20 psi at 10,000 gallons
per minute of flow.
Two public fire hydrants are located within 60 feet of the project property line to the west.
and south. These hydrants are 180 and 260 feet from the facility entrance on East
Marginal Way South. The site utilizes approximately 220 feet of frontage on East
Marginal Way South, which allows a good field of view for application of water via
aerial apparatus.
SUMMARY
This LPG bulk transfer and storage facility is located in an area with minimal exposures.
It will be equipped with redundant product controls, an automatic fire detection and
suppression system and excess pressure venting appurtenances. Management procedures
specify elimination of ignition sources (smoking, engine shutoff) for transfer operations.
Management also maintains a prescriptive maintenance program for hoses, check valves,
fire extinguishers and suppression equipment in compliance with state and local codes.
Following a review of facility features and controls, GT Engineering finds the proposed
facility to be in compliance with the codes specified in this document. No unusual
conditions are present which require additional protection outside the scope of NFPA 58,
the Liquefied Petroleum Gas Code.
GT Engineering
Veritox, Inc. dba
Adam` P.E., C.S.P:
Sr. Fire Protection Engineer
2
Appendix A
LSA Forms
Appendix A
Form 4.1
Initial Data on the LP-Gas Facility
X IB L C
Item Information Item Data
-Gas Plant Owner or Blue Star Gas Seattle, Co:
I
Name of the LP Operator
2 Contact Name Chris Mastrup
3 Contact Telephone Fax Numbers 707-573-3130 707-573-3132
4 Contact Email Address cmastr1m(&.blues-taraas.co I m
"Street 1; 10850 E Marginal Way.S.
5 Mailing Address Street 2:.
City, State, Zip: Tukwila, WA. 98788
Form 4.2
Facility, Storage Capacity
B I C 1
A D .1
Individual Total
Container Number of Water Capacity (wc)
Water Capacity containers of each container
(we) j.: size
(gallons) (gallons)
500 1
LOW 'I
2,000 1A 1150
4,000
10,000,
!8,000 1,
30;060 1 1 1 30,000 ;1,
60,0001
Other:
Other:
Other:.
I Other: 1,
2 Aggregate Water 1 31,150
Capacity
Notes.- (I) Coldirin D Column B x Column C.
(2) Parked bobtails, transports and tank cars should not be considered for aggregate
capacity calculations.
(3) Do not consider containers that are not connected for use.
(4) For the purpose of this manual, "Aggregate Water Capacity" means any group of
single ASME storage containers separated from each other by distances less than
those stated in the aboveground containers column of Table 6.3.1.
If the aggregate water capacity of the LP-Gas facility is less than or equal
to 4,000 gallon (w.c.), no further assessment is required.
YOU CAN STOP HERE.
A-1
Form 4.3
Additional Information on the LP -Gas Facility
Existing Facility; Built to NFPA 58 Edition 2011. X Proposed Facility
a) Name of the Facility (if applicable) Blue Star Gas Seattle, Co.
b) Type of LP -Gas Facil
e) Facility is located in
d) Facility neighbors
(Check all that apply)
overhead in casement.
ity Commercial Industrial X Bulk Plant
Rural. Area, Suburban Area, X City Commercial Zone
City Industrial Zone
Agri. fields X Commercial Bldgs. Flammable Liquids Storage
Industrial Activity (metal fabrication, cutting and welding, etc)
X Manufacturing X Others (explain) Sound Transit Light Rail
e) Geographic Location of Facility /Address, 10850 East Marcinal Wav South
Tukwila, WA. 98.1.88
f) Landmarks, if any:
g) LP -Gas liquid supply by Bobtail X Truck Transport Rail Tank Car
(Check all that apply) Pipeline
h) LP -Gas Distribution. by: X Bobtail Truck Transport Vapor Piping
(Check all that apply) Liquid Piping X Dispensing or Vehicle Liquid fueling
i) Number of Vehicle Entrances: X One Two More than two
j) Type of Access Roads to the Facility Rural City or Town X Highway
(One check per line) Entrance 1 Dirt road Gravel road X Paved
(One check per line) Entrance 2 Dirt road Gravel road Paved
k) Staff presence Not staffed Only during transfer operations
Staffed always (24/7) X Only during business hours
Other (Explain)
1) Location and distances to Institutional Occupancies surrounding the facility, if any, within 250 ft
from the facility boundary in the direction of the assets.
None present
m) Overview plot plan of the facility attached? X Yes No
All properties either abutting the LP -Gas facility or within 250 feet of the container or transfer point nearest to
facility boundary.
A -2
If in Form 5.1 an one of the numbers in column D is less than
Y the
number in Column C of the corresponding row, then these items
must be addressed and brought into compliance with the specific
edition of NFPA 58 that the facility was constructed to.
Form 5.2
Compliance with Code Requirements for Appurtenances on Containers
Of water capacity 2001 gallons through 4,000 gallons
Used in Residential and Commercial Facilities
I__ A L B 1 C G .b E I
Number of Product Release NFPA 58
Service Control Appurtenances Section
Container Configuration Required by lnsta.11ed on Reference
Sub Figure NFPA 58 the (2011
(in Figure 5 -1) (applicable Container edition)
edition)
2
3 I I I 5.7.7.1 and
4 I Table 5.7.7.1
I
I,
I 6
If, in Form 5.2, any one of the numbers in column D is less than the
number in Column C of the corresponding.row, these items must be
addressed and brought into compliance with the specific edition of
NFPA 58 that the facility was constructed to.
A -3
Form 5.1
Compliance with
Code Requirements for Appurtenances on Containers of
2,000 Gallons Water Capacity or Less
!a►
1 13 C I D I E
Number of Product Release
Service Control Appurtenances NFPA 58
Container
Configuration Required by Section
Sub Figure NFPA 58 Installed on
Reference (2011
the
(in Figure 5-1) (applicable Container edition)
edition).
1
I 5.1E I 3 3
2
1 I
3
I I 1 5.7.7.1 and
4
I I I Table 5.7.7.1
i 6
I I
If in Form 5.1 an one of the numbers in column D is less than
Y the
number in Column C of the corresponding row, then these items
must be addressed and brought into compliance with the specific
edition of NFPA 58 that the facility was constructed to.
Form 5.2
Compliance with Code Requirements for Appurtenances on Containers
Of water capacity 2001 gallons through 4,000 gallons
Used in Residential and Commercial Facilities
I__ A L B 1 C G .b E I
Number of Product Release NFPA 58
Service Control Appurtenances Section
Container Configuration Required by lnsta.11ed on Reference
Sub Figure NFPA 58 the (2011
(in Figure 5 -1) (applicable Container edition)
edition)
2
3 I I I 5.7.7.1 and
4 I Table 5.7.7.1
I
I,
I 6
If, in Form 5.2, any one of the numbers in column D is less than the
number in Column C of the corresponding.row, these items must be
addressed and brought into compliance with the specific edition of
NFPA 58 that the facility was constructed to.
A -3
Form 5.3
Compliance with Code Requirements for Appurtenances on Containers Having a
Water Capacity of 2,001 through 4,000 Gallons
Used in Bulk Plants and Industrial Plants
I A I B 1 C D E F G
Total of
Product Release Control
LP -Gas inlet to Appurtenances NFPA 58
Container Figure Required Section
and outlet from
the container by NFPA Installed Reference (2011
58 on the edition)
(applicable container
edition)
inlet 5 -2
j Vapor Outlet 5 -3 f
1
Liquid 1, Inlet 1: 5 -4
1 Outlet 1, 5 -5
Vapor Inlet 5
2 Outlet 5 -3 j
Liquid I Inlet 54 See Table
-Outlet 1 5 -5 1 5.7.7.3
Vapor Inlet 5 -2
3 J Outlet` 5 73
Liquid Inlet 5-4_ 1
Outlet 5 -5
Vapor Inlet 5 -2
4
Outlet 5 -3 J
Liquid Inlet 54:
I Outlet 1. 5 -5 1.
If the container does not provide an opening for the specific function listed, enter 0
(zero) in columns E and F corresponding to that row.
F
If, in Form 5.3, any one of the numbers in column F is less than the
number in Column E of the corresponding row, these items must be
addressed and brought:into compliance with the specific edition of NFPA
58 that the facility was constructed to.
A -4
E If in Form 5.4 any one of the numbers in column F is less than the
number in Column E of the corresponding row, these items must be
addressed and brought into compliance with the specific edition of
NFPA 58 that the facility was constructed to.
'F
A -5
Form 5.4
Compliance with Code Requirements for Appurtenances on Containers Having a
Water Capacity Greater Than 4,000 Gallons
Used in Bulk Plants and Industrial Plants
A f' B E C
P L F G
E
Total Number of Product
Release Control
LP -Gas inlet to
Appurtenances NFPA 58
Container
and outlet from
Figure Required Section
the container
by NFPA Installed Reference
58 on the (2011 edition)
(applicable container
edition).
Vapor`
.572 1:..- 2
Outlet
l
5.3 L 2 2
1 Inlet........
Liquid
5_6 2
I
Outlet
5 -7 2 2
Vapor Inlet
5 -2 1..
2 Outlet 1
5 -3 I I
Liquid
5 76
[Outlet
5 -7 See Table
Vapor Inlet..
5-2 1 5.7.4.2
3 Outlet
5 -3 I I
Liquid Inlet
Outlet
5 I I
Vapor Inlet
5 -2 1
Outlet 1
4
5 3
Liquid #Inlet I
5 -6
Outlet I'
5-7.
If the container does not provide an opening for the specific function listed, enter 0
(zero) in columns E and F corresponding to that row.
E If in Form 5.4 any one of the numbers in column F is less than the
number in Column E of the corresponding row, these items must be
addressed and brought into compliance with the specific edition of
NFPA 58 that the facility was constructed to.
'F
A -5
Form 5.5
Requirements for Transfer Lines of 1% -inch Diameter or Larger,
Liquid into Containers
A B_
Item Appurtenance
(Either No. I
or No. 2)
1
2
4c
_C D E
F
Installed in
NFPA 58
Appurtenance Provided with the the facility?
Section
Feature
Reference
Yes No
(2011
Automatic shutoff through thermal (fire) d6tuation
edition)
A -6
lnstalled within 20 ft. of-lineal pipe from the
X
nearest end of the hose or swivel -type
6.12.2
connections.
Automatic shutoff through thermal (fire) d6tuation
X
6.12.6
with melting point of thermal element 250 °F
Temperature sensitive element (fusible link)
X
installed within 5 ft from the nearest end of the
6.12.6
hose or swivel type piping connected to liquid
transfer line.
Emergency
Manual shutoff feature provided at ESV installed
X
6.12.10(l)
Shutoff Valve
location.,.
(ESV)
Manual shutoff device provided at a remote
X
location, not less than 25 ft., and not more than
6.12.10 (2)
(Ref 6.12. 1)
100 ft. from the ESV.
An ESV is installed on each leg of a multi leg
X
piping each of which is connected to a hose or a
6.12.5
swivel type connection on one side and to a
6.18.2.6 (1)
header of size 1 %a inch in diameter or larger on the
,,other_side.
Breakaway stanchion is provided such that in any
X
pull -away break will occur on the hose or swivel
6.12.8
type connection side while retaining intact the
valves_and,piping.on the-plant-side.
Installed downstream of the hose or swivel -type
X 6.12 .8
connection___
BCV is designed for this specific application:
X 6.12.3
and 6. l 2.4
A BCV is installed on each leg of a multi leg
X
Back flow
piping each of which is connected to a hose or a
Check Valve
swivel type connection on one side and to a
6.12.5
(BCV)**
header of 1' /z inch in diameter or larger on the
other side.
Breakaway stanchion is provided such that in any
X
pull -away break will occur on the hose or swivel-
6.12.8
type connection side while retaining intact the
valves and piping on the plant side.
The backflow check valve (BCV) is only permitted when flow is only into
the container and shall have a
metal to-metal seat or a primary resilient seat with metal backup, not hinged with a combustible material.
A -6
Form 5.6
Requirements for Transfer Lines of 1' /2-inch Diameter or Larger,
Liquid Withdrawal From. Containers
A B C D I' E F
Installed in NFPA 58
Item the facility? Section
Appurtenance Appurtenance Provided with the Feature Reference
Yes No (2011
Edition)
Installed within 20 ft. of lineal pipe from the nearest
end of the hose or swivel -type. connections. N.A. N.A. 6.12.2
Automatic shutoff through thermal (fire) actuation N.A. N.A. 6.12.6
with melting point of thermal element 250 F..
Temperature sensitive element installed within 5 ft N.A. N.A.
from the nearest end of the hose or swivel type 6.12.6
Piping connected, to liquid transfer line.
Manual shutoff feature provided at E SV installed N.A. N.A. 6.12.10
Emergency ...location. _(1)
Shutoff Valve Manual shutoff device provided at a remote location, N.A. r' N.A. 6.12.10
1 ESV not less than 25 ft., and not more than 100 ft. from
the ESV.
Ref 6.12. 1)
An ESV is installed on each leg of a multi leg piping I N.A., N.A. 6 12.5
each of which is connected to a hose or a swivel type 6.1 8.2.6
connection on one side and to a header of 1'12 inch in
diameter- orlarger on .the _other side. (1)
Breakaway stanchion is .provided such that in any N.A. N.A.
pull -away break will occur on the hose or swivel- 6 12 8
type connection side while retaining intact the valves
and ,piping on the plant side.
Number of ESV's in liquid withdrawal service 4
Note: If more than one ESVis installed in the facility, use one Form 5.6 for each ESV.
A -7
Form 5.7
Requirements for Vapor Transfer Lines 1'/. -inch Diameter or Larger
A B E
I C D J I
F
Installed in
NFPA 58
Item the facility?
Section
Appurtenance Appurtenance Provided with the Feature
Reference;
Yes No
(2011
edition)
Installed within 20 ft. of lineal pipe from the nearest end X
6.12.2
of.the hose .or.swivel-type connections.
AutofiMc shutoff through'thermal (fire) actuation with X
6.12.6
melting:point of thermal element 250 O F f
Temperature sensitive element installed within 5 ft from X...
the nearest end of the hose or swivel type piping
6.12.6
connected to liquid transfer line.
Emergency Manual shutoff- feature provided at E SV installed X
l 6.12.10
Shutoff Valve location.
1 shutoff device provided at a remote location, not X
(ESV)
6.12.10 (2)
less than 25 ft., and not more than 100 ft. from the ESV.
less
(Ref 6 .12. 1) An ESV is installed on each leg of a multi leg piping X
each of which is connected to.a hose or a swivel type
6.12.5
connection on one side and to a header of 1 %z inch in
6.18.2.6(1)
diameter or larger on the other side.
Breakaway stanchion is provided such that in any pull- X
away break will occur on the hose or swivel -type
6.12.8
connection side while retaining intact the valves and
Liping.on the plant side.
If a checkmark is made in the "No" column of any one of Form 5.5, Form 5.6 or
Form 5.7, then these items must be addressed and brought into compliance with
the specific edition of NFPA 58 that the facility was constructed to.
A -8
Form 5.8
Evaluation of Redundant Fail-Safe Design
A B
C D E
Installed in the NFPA 58
t
facility? Section
Description Features Reference
M
Yes No i (2011
i edition)
Redundant Fail-Safe equipment and Low
Container Sizes for which Emission transfer lines are provided for 6.26.3 and
the appurtenances are each container of water capacity 2,001 gal X 6.26.4
provided
through 30,000.gal_..
LIQUID OR VAPOR 1 Internal Valve with integral excess I flow
WITHDRAWAL (1-1/4 in. valve or excess flow protection X 6.26.3.1
2
or larger) Positive'Shut ff Valve installed as close as
possible to the Internal Valve X 6.26.3.4
internal Valve with integral excess flow
LIQUID OR VAPOR valve or excess flow protection or Back X 6.26.3.5
3 INLET Flow Check valve
Positive Shutoff Valve installed as close as
possible to the Internal Valve or the back X 6.26.1.5
flow check valve
Flow
Into or Internal Valve installed in the transfer hose 6,18.2.6 (1)
Out of or the swivel-type piping at the tank car end N/A N/A and 6.26.4.1
Railroad
Railcar Transfer tank car
4 Flow
Only Internal valve or backflow check valve 6.18.2.6 (2)
into installed in the transfer hose or the swivel- and 6.26.4.1
railroad type piping at the tank car end
N/A N/A
tank car
Cargo Tank
Protection provided in accordance with
5 Transfer 6.12. N/A
N/A 6.26.4.1
Automatic closure of all Actuated by Fire De I. te cti o n
X 6.26.4.2
6 primary valves (IV ESV)
in an Emergency Actuated by a hose pull-away X 6.26.4.2
Remote shutdown station within 15 ft of the
point of transfer? X 6.26.4.3 (A)
Another remote shutdown station between
X 6.26.4.3 (B)
Manually operated remote
25 ft and 100 ft of the transfer point?
1 7
shutdown of IV and ESV Shutdown stations will shut down electrical
power supply, if any, to the transfer X 6.26.43
equipment and-primary valves?
Signs complying with the requirements of X 6.26.4.3 (C)
pro ided?,
Note: If the facility does not have a rail terminal, write the word NA in both the "Yes" column and the "No" column
in item 4 of this Form in the railroad tank car row. Similar option is also available if there is no cargo tank
vehicle transfer station.
A-9
IM"
Form 5.9
A-10
Evaluation of Low Emission Transfer Equipment
A
B
E C I
D I E
F I
I
Installed
NFpA 58
t
in the
Section
e
Description
Features
facility?
Reference
m
(2011
Yes No
Edition)
Transfer into
Delivery Nozzle and Fixed Maximum Liquid
1
Cylinders or
Filler Valve- Max. Level Gage not used
X
13 b.26.5.1
ASME Containers
Liquid Release after during transfer
on Vehicles
transfer .of4.cc. operations
Transfer into
does not exceed 4 cc
During product 3
(0.24 in) from a hose
X
Stationary ASME
transfer or post of nominal size 1 in or
6.26.5.1 (A)
Containers.
transfer uncoupling
smaller
2
Delivery valve and
of the hose
does exceed 15 cc
X
nozzle
me
product volume 3 from a hose
(0.91 in)
combination
released to the
of nominal size larger
6.26.5.2 (B)
atmosphere
than :l in.
Transfef into
Do containers of less than 2,001 gal (w.c.) have
Stationary ASME
an overfilling prevention device or another
X
6.26.5.2 (F)
3
Containers
approved device?
Maximum filling
Do containers of greater than 2,000 gal (w.c.)
X
6.26.5.2 (E)
limit
have a float gage or other non venting device?
Transfer into
Stationary ASME
Not used during routine transfer operations but
6.26.5.2
4
Containers
used to calibrate other non venting liquid level
X
(C, D)
Fixed Maximum
gages in the container
Liquid Level gage
Note:
1) If the facility does not have a particular feature described in the table, write "NA" in
both the "Yes"
and "No" columns
corresponding to the row in item 2.
A-10
Form 6.1
Evaluation of Physical Protection and Other Measures
A !1` B.
C D E
F
Installed in
NFPA 58
Item
the facility?
Features
Section
Reference
Yes No
(2011
Edition)
1 Lighting:
Provide lighting for nighttime operations to illuminate storage containers, X
container being loaded, control valves, and other equipment
6.18.5
Protection against vehicular (traffic) impacts on containers, transfer piping X
i
Vehicle impact
and other appurtenances is designed and provided commensurate with the
6.9.3.10
2
protection
size of vehicles and type of traffic in the facility. (Example protection
and
systems include but not limited to 1 Guard rails (2 Steel bollards or
y O
6.1.9.3.2
crash posts, (3) Raised sidewalks.
Protection against
Provide protection. against corrosion where piping is in contact with X
6.9.3.11
3
supports or corrosion causing substances.
and
corrosion
ss h,. &.�.��':�,.a �`,�`rot"C,.. v. ✓'3
..max •fix
�a rA� -s.1
N.
Is an industrial type or chain link of at least 6 fl high or equivalent 4
+5���� may.
protection provided to enclose (all around) container appurtenances,
6.18.4.2
pumping equipment,.aoadin ..and unloading and container filling: facilities?
Are at least tw& means of emergency accesses (gates) from the enclosure X
provided?
Perimeter Fence
NOTE: Write "N.A." (not applicable) if
6.18.4.2
4A
(i) The area enclosed is less than 100 ft or
(A)
(ii) The point of transfer is within 3 ft of the gate, or
containers are not filled within the enclosure
is a clearance of at least 3 feet all around to allow emergency access to the
X
6.18.4.2.
required means of egress been provided?
I
(B)
If a guard service is provided, does this service cover the LP -Gas plant N.A. N.A.
Guard Service
and are the guard personnel provided with appropriate LP -Gas related
6.18.4.3
tiratzaia per section 4.4 of NFPA 58?
Lock -in- Place
Are Lock-in-Place devices provided to prevent unauthori2ed use or N,A N A,
4B
devices
operation of any container appurtenance, system valves, or equipment in
6.18.4.2
lieu,of the fence requirements above2.....
C
Note: Fill only items 1, 2, 3, and 4A or 48. Indicate with "NA" when not filling the "Yes" or "No" column.
Indicate with "NA" if the facility is not operated at night.
A -11
i`4�
Form 6.2
Ignition Source Control Assessment
A
l B I
C 1 D
E..
Is the Facility
NFPA 58
_..._compliant?
Section
ignition Control Requirement
Reference
'Yes No
(2011
E.
Edition)
Are combustible materials, weeds and tall
X'
1
grass not closer than 10 ft. from each
6.4.5.2
container
Is a distance at least 20 ft. provided between
2
containers and tanks containing flammable
N.A., N.A.
liquids with flash.point less than 200 T (ex.,
6.4.5.5
gasoline, diesel)?
3
Are electrical equipment and wiring installed per
X
6.22
Code requirements?
2
4
Is open flame equipment located and used
I..
N.A. N.A.
6.22.3
accordm gtoCode?
5
Are ignition control procedures and requirements
X
7
during liquid transfer operations followed?
"2'3'2
Is an:approved portable dry chemical fire
X
6
extinguisher having a minimum capacity of 18
6.23.4.2
lb. (8.2 kg) with a B:C rating provided in the
..,i facility?
I Is an approved, portable, dry chernical'fire
3X:
extinguisher having a minimum capacity of 18
j
7
i' lb. (8.2 kg) with a B:C rating provided on each
9.4.7
i truck or trailer used to transport portable
containers?
8
Is the prohibition on smoking within the facility
X
7.2.3.2
(B)
premises strictly enforced?
f 9.4.10
Note: 1)
Insert "NA" in both "Yes" and "No" columnso
any items that are not applicable.
A -12
Form 6.3
Separation Distances from Containers to Buildings, Property Lines that can be
Built upon, Inter container Distances, and Aboveground Flammable or
Combustible Storage Tanks
A B I C I D... C E.- E' F E G
Container is the Facility NFPA 58
Separation Between
Size Minimum compliant? Section
Range in Property lines, important building or Distance Reference
other property and the nearest
gal
gal container which is (ft) Yes No (2011
Edition)
501 Above Ground 25 x
through Underground or Mounded 10 N.A. N.A.
2,000 Between containers 1' 3 1 N.A. J' N.A. I
Above Ground 50 x
2,001 g g:r i
2 through Under ound or Mounded 50 N.A. i'N.A.
30,000 1 Between containers 5 N.A. f; N.A.
Above Ground 75 I N A. J` N.A.
Underground or Mounded 50 N.A N.A.
30,001 sum Of Table
3 through
70,000 diameters 6.3.1
I Between containers of N.A. N.A.
j adjacent
containers
Above Ground 100 N.A N.A.
Underground or .Mounded A
50 ['N.A.
N
70,001 ''A sum of
4 through diameters
90,000 Between containers of N.A. N.A.
adjacent
contain_ ers
Separation distance between a LP -Gas
All sizes container and an above ground storage N.A. N.A.
5 greater than 20 6.4.5.5
125 gal tank containing flammable or combustible
liquids.. -of flash points below 200 F,
Note: If any of the container sizes indicated in the above form are not present in the facility,
enter "NA" in both Yes and No columns.
A -13
Form 6.4
Separation Distances between Points of Transfer and other Exposures
A B C 1 D 1 E F G
Check if Minimum Is the Facility NFPA 58
Type of Exposure within or outside the facility exposure Distance compliant? Section
boundary Reference
is present (ft) Yes E No
(2011 Edition)
1 Buildings, mobile homes, recreational vehicles, X 10 X
and modular homes with fire- resistive walls
2 Buildings with other than fire resistive walls J 25
3 Building wall openings or pits at or below the 25
level of the point of transfer
4 J Line of adjoining.property that_can,be .built upon... X 25 1 X
5 Outdoor places of public assembly, including 50
school yards.,.athletic fields, and ejay. grounds-
Public ways, including From points of transfer
in LP -Gas dispensing X 10 X
public streets, stations and at vehicle Section 6.5.3
6 highways, fuel dispensers. Table 6.5.3
thoroughfares, and From other points of
sidewalks transfer 25
7:_- j Driveways X, 5 X
f 8 Mainline railroad track centerlines 25 i
9 i; Containers other than those being filled i l0
Flammable and Class II combustible liquid
10 dispensers and aboveground and underground 20
containers
Flammable and Class II combustible liquid
11 dispensers and the fill connections of LPG 1.0
containers
LP -Gas dispensing device located close to a
12 Class -I.- liquid dispensing device. 10 b.22.4.33
NOTE: Place a checkimark in column C against an exposure that is present in or around the facility. Fill columns
E or F for only those rows for which there is a checkmark in column C:
If the facility contains low emission transfer equipment (Le, all equipment identified in Form 5.9
are installed and are in working order), then the minimum separation distances in column D of
Form 6.4 can be reduced to one half of the indicated values.
If the containers in the LP-Gas facility are provided with SPECIAL
PROTECTION MEASURES, then continue the analysis below.
Otherwise skip section 6.4 and go to Chapter 7. Also see Chapter 9.
A- 14
Form 6.5
Special Protection Measures Requirements for Passive Systems
A
C
D
E
Special
Is the Facility
NFPA 58
com�ant?
Section
Protection
Question
Reference
Option
Yes No
(2004
Edition)
Insulation provided on each of the
N.A. N.A
containers?
6.23.5.1
1 Container Insulation
Insulation material complies with the
N.A. N.A.
6.23.5.1
requirements of section 6.23.5.1 of NFPA
and
58
6.23.5.2._
Mounding of
Each container in the facility is mounded?
N.A,, N,A.,
6.23.5.3
2
containers
Mounding complies with each requirement
Mk N.Ar
under section 6.23.5.3 of NFPA 58.
6.23.5.3
Each container in the facility is buried?
N.A: N.A:
6.23.5.4
3 Burying of containers
Buried containers comply with each
N.A. N.A.
requirement under section 6.6.6.1 of NFPA
6.6.6.1
58.
6.23.5.4
Form 6.6
Special Protection Measures Requirements for
Active Systems
Special
Is the Facility
NFPA 5$
compliant?
Section
Protection
Question
Reference
Option
Yes No
(2004
Edition),
Are fixed water spray systems, complying with
NFPA 15' requirements, used for each
X
6.23.6.1
container in the facility?
1 Water spray systems
Do fire responsive devices actuate water spray
system automatically?
X
6.23.6.2
Can the water spray systems be actuated
manually also?
X
6.23.6.2
Are the monitor nozzles located and arranged
so that the water stream can wet the surfaces of
X
6.23.6.3
all containers exposed to a. fire?
Can the water stream from a monitor nozzle
reach and wet the entire surface of, at least, one
Monitor nozzle
half of a length from one end of each of the
X
6.23.6.3
2
systems
containers it is designed to protect
Do fixed monitor nozzles comply with NFPA
6.23.6.3
15 requirements?
X
Do fire responsive devices actuate the monitor
6.23.6.3
_nozzles
X
Can the monitor nozzles can be actuated
X
6.23.63
manually also?
1. Refer to Chapter 8 for discussion
on NFPA 15 Standard for Water Spray Fixed Systems for Fire
Protection
A -15
A 1:6
Table 7.1
Distances to Various Types of Propane Hazards Under Different Release Models"
Form 7.1
Types of Occupancies Near or Surrounding the LP -Gas Facility
Is an Occupancy
Model Hazard located within the
Type of Occupancies from Distance (Z) hazard distance
Table 7.1 (feet) from the Facility
Yes I No
Assembly Occupancies (Places of worship, Libraries, Theaters N.A. X
and Auditoriums, Food or Drink Bars, Sports Stadiums,
Amusement Parks, Transportation Centers, etc. with 50 or more
people).
Institutional Occupancies (Elderly Persons Home or Nursing N.A. X
Home, Hospitals, Alcohol Drug Rehabilitation Centers,
Prisons)
Educational Occupancies (Elementary Schools, Day Care N.A. X
facilities, etc).
NOTES: (1) Different types of occupancies are defined in NFPA 5000
(2) Table 7.1 provides a number of scenarios that can result in propane release, and the resulting area
exposed for different ignition mechanisms. Determine the scenarios that are applicable to the
facility, for the quantities that can be released. Use the hose diameters and length that will be used
at the facility if they differ from the ones in Table 7.1 and recalculate the hazard distances using a
spreadsheet method that is available at npga.org. Some scenarios may not be applicable to an
installation based on other mitigation measures taken, such as a hose management procedure to
minimize the possibility of hose :failure.
A -17
Vapor
Explosion
Fire Ball
Model
Details of the Propane .Release Model
Dispersion
Hazard
Radiation
Releases from or due to
Distance
Distance
Distance
to LFL
f ft)
(ft)
(ft).
IA
Bobtail hose failure. Release 1" ID z 150 ft hose length
250
110
50
113
of the entire inventory in the 1" ID x 120 ft hose length
230 j1.
103
45
1 L
hose, quickly. 1" ID x 75 ft hose length
190
90
40
2
Release of the inventory in`a transfei piping 1" x 30 ft
20 &pm for 10 min., due to failed excess flow valve.
135
10
25
3
Release from the container pressure relief valve
No ignitable
vapor concentration
at
around level
Release from a 1" ID x 150 ft transfer piping to a vaporizer
4
and reduced flow from a partially open excess flow valve
250
120
50
20 gpm for 10 min.
Leak from a corrosion hole in a transfer pipe at a back
5
pressure of 130 psig (corresponding to 80 °F) for 60 min.
110
120
5
Hole size is 1 /4" ID.
6
Release of the entire inventory in a 2" 1D x 20 ft., transfer
hose.
195
90
40
7
Transport hose blowdown: Hose size 2" ID, 20 ft length
release for 3min., from a Transport after the tank is flied..
75
30
<5
Results from models described in Appendix B. The results are rounded to the nearest 5 feet.
Form 7.1
Types of Occupancies Near or Surrounding the LP -Gas Facility
Is an Occupancy
Model Hazard located within the
Type of Occupancies from Distance (Z) hazard distance
Table 7.1 (feet) from the Facility
Yes I No
Assembly Occupancies (Places of worship, Libraries, Theaters N.A. X
and Auditoriums, Food or Drink Bars, Sports Stadiums,
Amusement Parks, Transportation Centers, etc. with 50 or more
people).
Institutional Occupancies (Elderly Persons Home or Nursing N.A. X
Home, Hospitals, Alcohol Drug Rehabilitation Centers,
Prisons)
Educational Occupancies (Elementary Schools, Day Care N.A. X
facilities, etc).
NOTES: (1) Different types of occupancies are defined in NFPA 5000
(2) Table 7.1 provides a number of scenarios that can result in propane release, and the resulting area
exposed for different ignition mechanisms. Determine the scenarios that are applicable to the
facility, for the quantities that can be released. Use the hose diameters and length that will be used
at the facility if they differ from the ones in Table 7.1 and recalculate the hazard distances using a
spreadsheet method that is available at npga.org. Some scenarios may not be applicable to an
installation based on other mitigation measures taken, such as a hose management procedure to
minimize the possibility of hose :failure.
A -17
Form 7.2
Exposure to LP -Gas Facility from External Hazards
A B C D
Hazard exists
Item to the .LP -Gas
Type of Neighboring Operation Facility
YES
NO
1 Petroleum and other hazardous material storage, wholesale
x
?,.dispensing, etc.
2_. J`, Metal cutting,.welding,,and metal fabrication...
X
3 Industrial Manufacturing That can pose external hazards
x....
4- Ports, rail yards and trans- shipment terminals handling
x
flammable and explosive materials.
Other operations that ma pose hazards (gasoline and other
5 hazardous material dispensing stations, fertilizer storage,
x
etc).
NOTE: if a particular activity indicated in column B does not exist, fill both "Yes"
and "No" columns with "N /A."
Where a "YES" has been checked in either Form 7.1 or Form 7.2:
1) For an existing facility, communicate this information to local emergency
responders for inclusion in their emergency planning.
2) For a proposed facility, implement the actions indicated in Chapter 9.
A -18
Form 8.3
Water Flow Rate and Total Water Volume Required to Cool Containers Exposed to
a Fire
it B 1, D E F G
EI
ASME Total Surface Surface Water flow Number of Total Water Total volume
Area of each of water
Item Container Area of each rate required containers flow rate
container to required for
Size Container be Cooled per container of the size requiredl 10 min
(gallons) (ft) f (gpm) indicated
(gal)
500 86 43 1 1!..,.
1,000 172 8.6
2,000 I 290 145 3b.3 1
1 .36.3
14,000 374 187 46.8
570 285 7.1.3 i
9,200 790 395 98.8;
l f
1 12,000 990 495 123.8
18,000 1,160 580, 145.0
30,000 1,610 805 261.3 1 201.3
45,000 2,366 1, 295.8
66,000 3,090 1,545
386.3
190,000 4,600 2,300 575.0
Other Size. 18,000 550
i� 130
Calculated water flow rate for
a r� 237.6 2376
container protections g� r s
2b Water flow rate rounded up to��� ��k,' 2500
250
W f firefighter
nearest multiple o 125 Y k
3
Water or refighter protection ift7z 250 2500
req uired
4 Total water flow rate and volume -500k 5000
lAk Column D (1/2) x Column C Column E 0.25 z Column D
Column G Column F x Column E Column H 19 x luol [t► .C'
Line 2a, Column G and Column H are the sum of numbers in each row" ove line 2 of each column.
Line 4, Column G and Column H are the sum of numbers in rows 2 and 3.
Consider only 3 containers for water supply evaluations even if the number of containers in a group is more
than 3.
3' ASME container dimensions obtained from www.standbv.com /products /storage tanks.html
The total water requirement for the facility is indicated in item 4, column G (water
flow rate) and column H (total water volume or quantity) of Form 8.3. If multiple
groups of containers are present in the facility, repeat the calculations in Form 8.3
for each group of containers. The total water requirement for the facility is the
largest value for any single group of containers.
A -19
Form 8.4
Evaluation of Water Availability in or Near the LP -Gas Facility
A
Item
B C
Water from... Available?
Public supply or from another
D
Quantitative information
Available
Hydrant Distance from water flow
data Facility gate rate from all
(feet) hydrants
piped -in supply through one or
1
more fire hydrants in or near the X Yes No
Hydrant 1 180
y
facility
Hydrant 2 260
5000
Hydrant 3
A nearby static water source
Distance to water source
_Feet
2 (stream, pond, lake, etc). Yes X No
Time to set up relay
min.
Rate of delivery =pm
Only through mobile water tanker
3 ❑Yes No
Time to set u shuttle
p
min.
shuttle.
Sustainable flow rate
gpm
NOTE: (1) Obtain the flow rate in eachhydrapt from the local municipal
water authority or the entity that supplies
water to the hydrant or conduct a test to determine total available flow rate.
1. For an exiting facility, communicate this information to
local responders for inclusion in their emergency
planning.
2. For a proposed new facility, refer to Chapter 9
A -20
Form 9.1
Analysis Summary on Product Control and Local Conditions of Hazard
A B C
I D,.
E
Item
Reference
Number of
CHAPTER Title Section Title
FORM
"NO"
NO
checked§
5.1: Product Control in
5.1 or 5.2 or 5.3
Containers
or 5.4
0
Product Control Measures in
I 5.5
0
1 Containers &Transfer Piping 5:2 Product Control in
5,
Transfer Piping
5.8
U
5.9..
o...
6.1 Physical Protection
0
Measures,_
6.1
6.2 Ignition Source
0
Control
6.2
i 6.3.1 Separation distances;
0
Analysis of Local Conditions Container and
6.3
2 outside exposures
of Hazard
6.3.2 Separation distances;'
0
Transfer points and
6.4
outside exposures
i
0
6.4 Special Protection
6.5 f
0
Measures
6,6
0 J
T ie number of "No" for Forms from Chapter 5 are the difference between NFPA 58 -2004
required number of
appurtenances and a lesser number actually installed on the container or
the transfer piping.
If in any row of column E ("No of Form 9. 1, the entry number is greater than zero, the
proposed LP -Gas facility is not in compliance with the 2011 NFPA 58 Code .requirements for
product control appurtenances or other safety measures. The design of the proposed facility must
be modified to conform to the Code requirements. In addition, the following items should be
noted.
If there are any "No" checks in Form 6.3, then the separation distance requirements for
containers are not ;satisfied. An option that may be considered is the reduction in separation
distance to 10 feet for underground and mounded containers by providing "Redundant and
Fail -Safe Product Control Measures." In this case, complete Form 9.4, below to ensure that
each requirement of "Redundant and Fail. -Safe Product Control Measures" is provided.
If there are any "No" checks in Form 6.4, then the separation distance requirements for
transfer points are not satisfied. In this case, relocate the transfer points so that the separation
distances conform to the code requirements or provide the Low Emission Transfer Equipment.
Complete Form 9.5 below and ensure that all requirements for Low Emission Transfer
Equipment are fulfilled.
A -21
Form 9.2
Analysis Summary on Exposure from and to the LP-Gas Facility
A J. B-
C
D
E
Item
Reference
Number of
CHAPTER Title
Section Title
FORM
«YES"
checked
7.1 Exposure to off. site
properties and
7.1
0
Exposure to and from Other
persons from in -plant
1
Properties
cane releases
7.2 Exposure to propane
facility from external
7.2
0
events.
If the entry number in column E "Yes Form 9.2 corresponding to Form 7.1 is greater than
zero, consider one or more of the following design alternatives.
1 Consider moving the container or the transfer point to a different location, if possible and
space exists, so that the property or the person is beyond the hazard distance.
2 Provide "Redundant and Fail -safe Product Control Measures Complete Form 9.4 to
ensure compliance.
3 Institute other technical measures such as installing gas and flame detectors (connected to
facility shut down systems), sounding alarm outside facility premises, etc.
4 Institute administrative controls such as additional training for personnel, more frequent
inspection of hoses and transfer piping, etc.
If the entry number in column E "Yes Form 9.2 corresponding to Form 7.2 is greater than
zero, consider one or more of the following design alternatives.
1 Implement procedures to monitor neighboring activity.
2 Install means in the adjacent plant to shut down the LP -Gas plant in case emergency in that
plant.
A -22
Form 9.4
Redundant and Fail -Safe Design for Containers
A
B
C D E
F
Proposed for
NFPA 58
Item
Description
Features
the facl
h',_•
section
Reference (2011
Yes
NO
Edition)
Redundant Fail -Safe equipment and
X
Container Sizes for which
Low Emission transfer lines are
1
the appurtenances are
provided for each container of
6.26.4 and 6.26.5
provided
water capacity 2,001 gal to 30,000
-gal.
Internal Valve with integral excess
X
Liquid or Vapor
flow valve or excess flow
6.26.3.1
2
Withdrawal (1 -1/4 in. or
protection_
larger)
Positive Shutoff Valve installed as
X
close as possible to the Internal
6.26.3.4
Valve
Internal Valve with integral excess
X
flow valve or excess flow
Liquid or Vapor Inlet
protection or Back Flow Check
i
6.26.3.5
3
valve
Positive Shutoff Valve installed" as
X
close as possible to the Internal
j
6.26.3.5
Valve or the back flow check valve
Flow
Emergency Shutoff Valve` installed
N/A N/A
Into or
in the transfer hose or the swivel
Out of
type piping at the tank car end.
i
6.18.2.6 (1)
Railroad
and 6.26.4.1
Railcar
tank car
4
Transfer
Flow
Emergency shutoff valve or
N/A N/A
Only
i Into
backflow check valve installed in
6.18.2.6 (2) and
railroad
the transfer hose or the swivel -type
6.26.4.1
tank car
piping at the tank car end.
5
Cargo Tank Transfer
Protection provided in accordance
N/A
6.26.4.1
with 6.24.4.1
Automatic closure of all
By fire actuation
X
6.26.4.2
6
primary valves (IV
In the event of a hose Pull-aw ay due
ESV) in an Emergency
to vehicle motion
X
6.26.4.2
Remote shutdown station within 15
ft of the point of transfer?
X
6.26.4.3 (A)
Another remote shutdown station
between 25 ft and 100 ft of the
X
6.26.4.3 (B)
transfer point?
7
Manually operated remote
Shutdown stations will shut down
shutdown of IV and ESV
electrical power supply, if any, to
the transfer equipment and primary
X
6.26.4.3
valves?
Signs complying with the
requirements of 6.24.4.3 (C) (c)
X
6.26.4.3 (C)
provided
A -23
1
4 y ote: If your facility does not have a rail terminal, write the word NA in both the "Yes" column and the "No"
column in item 4 of the form in the railroad tank car row. Similar option is also available if there is no cargo
tank vehicle transfer station.
Form 9.5
Evaluation of Low Emission Transfer Equipment
A
B
it C
D I E
F I
Proposed
NFPA 58
Item
Section
Description
Features
facility?
Reverence
(2011
Yes I No
I, Edition)
Transfer into
Delivery Nozzle Fixed Maximum
X
1
Cylinders or
j and Filer Valve- Liquid Level Gauge
L Liquid
6.26.5.1 (B)
ASME Containers
Max.
not used during
Release after
on Vehicles
transfer operations
transfer. of 4 cc.
Does not exceed 4 cc
During product 3
X
Transfer into
transfer or post (0.24 in from a hose
6.26.5.2 (A)
Stationary
of nominal size I in or
transfer uncoupling:
2
ASME Containers
smaller
of the hose, liquid
Delivery valve
Does not exceed 15 cc
product volume 3
X
and nozzle
released to the (0.91 in) from a hose
6.26.5.2 (B)
combination
of nominal size larger
atmosphere
than 1 in.
Transfer into
Do containers less than 2,001 gal (w.c.) have
N/A N/A
Stationary ASME
an overfilling prevention device or another
6.26.5.2 (F)
3
Containers
approved device.
Maximum filling
Do containers greater than 2,000 gal (w.c)
X
limit
have a float gage or other non venting
6.26.5.2 (E)
device?
Transfer into
X
Stationary ASME
Not used during routine transfer operations
4
Containers
but may be used in calibrating other non-
6.26.5.2.
Fixed Maximum
Liquid Level
venting liquid level gauges in the container
(C,D)
gauge
Note:
If the facility does not have a particular feature described in the table, write "NA"
in both the "Yes"
and "No" columns corresponding to its row in item 2.
A -24
Form 9.6
Special Protection Measures Passive Systems
A
B
C
D
E I
Special
Section
Proposed for
NFPA 58
Item
Reference
Option
the facility?
Section
Protection
Question
Reference
Option
N/A ,N/A
Yes No
(2004
NFPA 15 requirements, used for each container
6.25,6.1
Edition)
Insulation provided on each of the containers?
X
6.25.5.1
1
Container Insulation
Insulation material complies with the
6.25.6.2
6.25.5.1
Can the water spray systems be actuated
N/A N/A
requirements of section 6.235.1 of NFPA 58?
N/A N/A
and
6.25.6.2
Are the monitor nozzles located and arranged
6.25.5.2
Mounding of
Each container in the facility is mounded?
X
6.25.5.3
2
containers
1.
Mounding complies with each requirement
Can the water stream from a monitor nozzle
under section 6.23.5.3 of NFPA 58..
.X
6:25.5.3
Each container in the facility is buried?
X
6.25.5.4
3
Burying of containers
Buried containers comply with each
systems
Do fixed monitor nozzles comply with NFPA
requirement under section 16.6.6.1 of NFPA
X
6,6.6.1
15 requirements?
X
58._
6.25.5.4
Form 9.7
Special Protection Measures Active Systems
i
Special
f
Is the facility
NFPA 58
Item
compliant?
Section
Protection
Question.
Reference
Option
Yes No
(2004
Are fixed' water'spray systems; complying with
N/A ,N/A
NFPA 15 requirements, used for each container
6.25,6.1
in the facility?
1 Water spray systems
Do fire responsive devices actuate water spray
N/A N/A
system automatically?
6.25.6.2
Can the water spray systems be actuated
N/A N/A
manually also?
6.25.6.2
Are the monitor nozzles located and arranged
so that the water stream can wet the surfaces of
X
6.25.6.3
all containers exposed to a fire?
Can the water stream from a monitor nozzle
reach and wet the entire surface of, at least, one
Monitor nozzle
half of a length from one end of each of the
X
6.25.6.3
2
containers it is designed to_protect?
systems
Do fixed monitor nozzles comply with NFPA
15 requirements?
X
6.25.6.3
Do fire responsive devices actuate the monitor
X
6.25.6.3
nozzles?
Can the monitor nozzles can be actuated
X
6.25,6.3
manually..also?__..
A -25
Equivalent Protection. to a Water Su PQ for. Industrial strial and Bulk Facilities
In the case where water supply is not available in or near the LP -Gas facility, or it is
inadequate or is prohibitively expensive to connect to a public or private water supply
hydrant, alternative methods for providing protection should be considered. In lieu of
providing a water supply, several alternatives are indicated in Table 9.1, which can offer an
equivalency to a water supply system.
The intent of the controls identified in Table 9.1 is to maintain the entire system as a gas tight
entity. These methods include reducing the service life of equipment, increasing the design
pressure rating of the system beyond the requirements of NFPA 58, or providing early
detection and isolation of the system to ensure product control. This list is not exhaustive and
is not ranked in an order Of nriority.
Table 9.1
Suggested Alternative Methods for industrial and Bulk Plants That Do Not Pose a
Hazard But Lack a Water Supply
item #1 Possible options to implement when adequate water supply is not available
1 Reduce the; service life of hoses:
2 Increase frequency of ea ;tupment inspection._
Establish a service life program for the maintenance of the container pressure relief
3 devices. This could include the installation of a listed multiple port valve and certifying
that the relief devices are properly set and maintained every 5 to 10 years.
4 Increase the strength of the piping and fitting systems..
5 Install emergency shutoff valves in "conjunction with container internal valves.
Install emergency shutoff valves downstream of transfer pump outlets, and upstream of
6 the vapor and ligiud valves at the bulkhead.
7 Install pneumatic tubing along the plant boundary to serve as a perimeter fir e detection
system. This would provide protection of the plant against exposure fires.
Provide optical flame detection or linear heat detection, or a gas detection system
8 connected to an isolation valve installed downstream of every liquid and vapor nozzle
on the container. This system could also be monitored to send a signal to an alarm
11 company that notifies the Fire Department of an event.
Increase the separation distances of Ini&nal plant exposures to the container. These
9 exposures would include a site dumpster, idle or waste pallets and combustibles, and
f increasing the parking distances between the bobtails and transports in relation to the
container.
Relocate overhead power lines away from all container and cylinder storage area to
to protect against ignition in the event of a line dropping due to wind or power pole
impact.
Eliminate all combustible vegetation within 30 feet of the LP -Gas container. This can
be accomplished using gravel, or paving the site- yard,
A -26
Appe ndix B
Site imp
rovement Drawings
r
Q
1
J
C]
w U
U
a ohF. d
m
J
2 o K w
Q
W
Y
w Mi 5 W
G g wN o G
d
LLI
s m
W
2
�mi'
co
ss
J
r
Q
1
J
J
W
ss
J
r
Q
1
J
Appendix C
Gas Distribution Piping Schematics
ion C4
Ul
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Appendix D
Equipment Specifications
Internal Valves
Fisher internal valves have g3tned wide field acceptOrce for use as pn( ry 5 ttitilff valves, excess flow valves atit3'it3acirctii ck
valves'. Internal valves are trtsta8ed:in,ttte.lniets end outlets (tig(id orvapor)af pressure vessels and In plPing syateits to control
the flow of LP -Gas and N$ 9 ,(arifiytlrr3US afilrr3p.Rie) T-h mot i tregtlen$:;3ppYiC3ti0h'is on bobtail and transport tntCk tanks,;but
they may also be used on large siailoner y storage tat11C5 anti or1.,En itne tr►stalletio The valves can be used: in:tzsnjuncibrI �Nilh
or without pumps and compressors.
Features Benefits
Perform functions of three different units: 1. Primary Shutoff, 2. Excess Flow and 3. Back Check.
Effective leak resistance with TFE spring loaded packing.
Complies with NFPA 58 requirements.
Three closing systems: 1. Manual, 2. Cable or 3. Air.
Built -in excess flow valve offers closure when flow exceeds the valve's rated capacity or piping is sheared off at the valve.
Fusible links or plugs melt at 212 °F 220 °F (100° C 104 °C) and allow valve closure in the event of a fire at the valve.
Principle of Operation
The operational schematic below depicts
however flanged styles operate in the sa
detailed information, "refer to the instructior
with the valve.
a larger amount of product to bleed downstream than if the
operating lever were moved into the full open position.
i tds,- whenthetankandthedownstreampressure
4 .—s flow spring pushes open-.ther main poppet
j;lever is moved to the full open position to ready
Zr transfer operation. The pump or compressor
rsbgjg'°'"kt+tt the valve is fully opened,
the full closed position in View #1 and the steps repeated.
VALVE CLOSED 0, RAPID BLEED OPEN VALVE OPEN t�;, EXCESS FLOW
VALVE CLOSED
1. Because of the integral back check function of these valves, selective filling of manifold storage tanks requires the use of additional shutoff valves.,
n
Internal Valves
Fisher offers the widest variety of threaded internal valves in the
industry. While their most frequent use is in the liquid and vapor
openings of bobtail and transport trucks, the valves can also be used
in stationary storage tanks, complying with NFPA 58 requirements.
Designed as primary shutoff valves, the units are designed with
several features that help control product discharge.
Steel and stainless steel constructions are standard': with
total stainless steel construction available. The u
loaded TFE packing for an effective seat aggins
disc material is Nitrite, butTFE, Kalrez®, Viton®
are available. (Note: TFE seats are not bubble
All Fisher internal valves are suitable for LP-Gas'
Snecial construction is available for:.'
'i
C402
C400 Series (2 34nch Body Sizes) Only Fisher offers three
different body styles in 2 and 34nch threaded sizes so that the best
body style can be selected for the particular application.
Type 0427 (Straight- Through Body) The most compact and
economical unit in the series, Type 0427 has one bottom outlet. The
0427 can be used on bobtail, transport, stationary tank and in -line
Body) This unit is designed with two outlets,
The side outlet permits installing horizontal piping
wit to the tank without the need for extra pipe
inection can be used for truck filling orwithdrawal.
primarily on bobtails and .transport trucks,
This -valve has three side outlets and
Threaded Internal Valves
Connections
Type.Number
Closing plow propane
Vapor Capacity CF
Inlet x Outlet
Strai ht Bod Tee Body Strainer Body
Half Coupling
Full Coupling
25 Psig 1
100 Psig
WA
Inches
9 y Y.,
(1,72 bar) Inlet
f6;bar}tntet'
0407 -10. 03
30
9,300
G407M =10032 11
...._5600
114 MNPTx
0407-10 -05' 1
so
35 1;;
t 800
13,200
114 FNPT
C4D7M 10 OS? t
80
65
1 1,200
19
a
F
27 -16 -10 I `0421.16.10 0402- 16-10'
100
00
22,000
37,600
z a
G427M- 16-1'0. I C421M 1B 10
2 MNPT x
042746-451 1 0421- 16-15 .f? C402_f6 -15 t
150
90
32,000
54,500
2 FNPT
bA27M-16-15? C421tMi -1G-i t l
it 2Q4fi 6 25 C421 =1625 '11. 0402 16 -251
250
130
n i5*14 C421M-16 25
0427 24 -15 t C424-2445 1 G402-24-15 t
150
100
29,200
49 700
C427M -2415 42�fN-2+) 1
1 0421- 24-20 Cid02 -'19 20 L
C427-244V_
200 f
125
44,400 i.
75,400
i
3 MNPT x
1
0427 24 251- j 042144.25 Z t 0402 24-2 5
250
165
52,600
89,400
3 FNPT
C427M24 25 t C421It u-2v i
0427 24-40' 1 0421 14440' 1 0402-2440
400
235
$1,800
139,000
c427M*44t :..a
0427 24 50! "4 C421 -240 't 0402;24 50 J.
500
325
.W" 1.i,, G421W24W :I
1 Sthridard u<itti tft manual,_` lever g� TAm,.134 fusible link. For pp(itiial controls `refer to Internal Valve acceedOdssi
2,lnekidas a feetthrY tnsfHNl9d '994
Internal Valves
A FNPT
70*
SWING
C407 -1
4
lest_
APP
14
coul
E
H
1/4"
FNPT
A FNPT
F
70*
SWING
C421
I
B MNPT
APPROXTOP
OF BOSS OR
COUPLING
T
F
70
SWING
C402
C427
Threaded Valves All Dimensions A re In
I nches (no)
Type
A
B
Installation
Number
FNPT
MNPT
C
D
E
F
Clearance
Diameter
0407-10
1.25
1.25
6.90 1!1
1.86
2.88
5no
C421-16
2
2
8.93
2.25
5.66 i
2.7O
71
2:66
10.00
(227)
(57)
(129)
(70)
(PP)
(254)
C42 1-24
3
3
6m
3.26
3.26
13.38
(27
65)
-.(1B
183)
.(340)
C-402-1 6
2
2
12.29
;L25
8.4.3
2,75
5 Bi
pig),
(57)
214,
(70)
(264)
0402-24
3
3
14.69
2.56
10:31 :1 1,
-3.5d
5.66
13;38
(373)
(262)
(340)___
C-427-16
J
2
1 2
�A6
4.05
MOO
20
(61)
(103)
(254)
0427-24
3
3
9.00
2.6.0
4.57
1318
(66).
016)
r— 2,
3
1.-
Threaded Fittings Socket Weld Fittings,
1. Class 2000, 3000 and 6000 for threaded Fittings. i. Class 3t)00, 61)00 and'90t10 for socket weld
fittings.
2. Industry standardized thread forms are
assured through rigid adherence to ANSVASME
131.20.1 standards.
3. Quality threads are assured and controlled
by ANPT gauging standards. Qualified guage
calibration programs are maintained on all
inspection and test equipment.
4. Extended reinforcing bands beyond the critical
depth of threading ensure that wall thickness
dimensions are maintained.
2. Forging design and geometry ensure minimum
thickness conditions are always exceeded.
3. Concentric socket and through fares minimize
turbulence and waterway flow restrictions.
4. Extended reinforcing bands and center distance
to socket bottom dimension ensure minimum wall
thickness dimensions are exceeded.
Engineered and manufactured from materials in accordance with the relevant ASTM materials specifications.
7/$ 4" ASTM AIDS, ASME SAIOS
7/8" —Va° ASTM A182, Grade F5. FS, F11 and F22
Capitol Forged Steel fittings and Unions meet the latest revisions of ASME 016.11 and MSS SP 83 and
MSS SP 79 dimensional standards.
Permanent heat code identification and pipe size markings on fittings. and unions ensure full traceability
From raw material to finished product.
Forged steel shapes are machined from solid forgings with grain flow and strength designed to meet the
most stringent operating conditions
Extensive In- process final inspection, certification and quality assurance records are maintained for
future reference.
vbow-s'
PAss,3000
Dimension A
Dimension H
Approx Wt.
'A
31 /32
I Vst
.68
V4
52
1
.50
Class 2000
1.4'
4
Ph
1.43
-Yd
1%
I"Ar.
2.30
A^
1
2Vo
3.73
2
2
4.40
A
Ptpa Size
34
V4
V2
34
I
4
Dim :A
Dimension H
3"
1 V84
Waz
1 1 164
3 %z
1 Ya
1%
Ms
IlAc
1%
1%
1
13 V i
2Y4
2 1 h
2
3152
3
3 Vw
3% 4
4 5 2 /4
Approx Wt.
34
1-.28
.49
.70
1.03
1.63
2,04
US
6,56
10.00 '22.50
Class 3000
34
1 /4,
M
V4
1
IY4
134
2
_21t
Dimension A
1 %2
116
isVie
11x4
1%
2
2%
216
3 1 /4
3 1 /4 4V2
Dimension H
I Ved
11/64
I%o
1 V.
I 'Vie
2V&
2
3 1 /4
3SM a
4
4 3
Approx Wt.
.34
-31
.60
.91
1.43
228
2.88
4.88
5.44
10.00
17.13 29.25
Class 6000
pipe Size
15
V4'
1
1Y4
1%
2
2
3 4
Dimension A
3 i%
1 A
1%6
M
AV@
2
2%
23
3
31 4 4
Oka
Dimension H
1'/&
I-Vis
1
1
2144
2
3Vk
3
A
04
5
Approx Wt.
.25
.66
1.00
1.59
2.54
3.66
SM
7.06
MOD 21-78
36.22
Tees
Class 2000
Pipt,
'A
2
2%
.3 4
Dimension A
3%j
74/jj
2S6
'114
IS/,
lik
1
2
2%
1
4
Dimension H
Approx Wt.
1 V64
-49
1'/
.44
I1164
.34
Ma
.69
M
.96
1 ':V-4
1.35
2'!4
2.10
215
2.75
3
4.25
3%
9.06
49/, SV
1350 32.50
Ptpe$
Dimension A
!Via
adz
1 146
2
2
2
3
416-
Dimension H
1
1V64
IYu
I Va
I'V"
234
2316
315z
3946
4
4% 6
Approx Wt.
.44
.43
.94
1.23
1.85
3.00
3.63
6.63
7.00
13.75
21.00 38.DD
Class 6000
Pipe-Sae
344
V&
V4
1
1 IA
I "h
2
2%
a
Dimension A
AIA2
1%
Mc
1 1 16
IV&
2
2%
214
3%
33/4
4
Dimension H
1Y
1%-
1
1 wAs
2V4
2%
3 Ma
:VAe
4
4%
5144
Approx Wt.
.44
.92
1.38
216
3.63
4.83
7.76
9-75
1730
28-90
49.60
Crosses
ciaw'ZO00'.
U
,Y4.
Va
I
1Y4
11*
2
2
3 4
Dimension A
3 VU
31 /n
I VS2
1%
Ig/1B
1
134
2
2%
9
3% 4%&
Dimension H
I 1 /w
1?/ea
1
Me
1%
1 'Via
2
2
2
3'Vie
4Vie 6%
Approx Wt.
.75
68
.4b
zo
i-ob
us
2.35
3.28
5.00
17-20
22.10 32.70
C18-515 GODO
Pipe Size 1 /8 Vd 1 h V4 I
birviihsibn A IY6 I i/b Is/is 1 1 2
Dimension H 1 Me VA I'-Aa 2 rAa
Approx Wt. .50 1.12 1.55 2.59 4.21 5.64
1 2 2% 3 4
235 MA 31%4 3 4
2 2 'h2 3%s 4 43/4 6
8.13 8-31 16.96 20.75 34.13
1 1'A 2 2 3
2 234 3 3 AV,@
2 3%s 4 4Y4 SY4
9.58 11.39 21.37 28.32 55.88
)Vu MIWKN A"9 MiSM Altv- I*b ru P11 F*zz
PAss,3000
Dimension A
Dimension H
Approx Wt.
'A
31 /32
I Vst
.68
V4
52
1
.50
14
IIA
Me
96
1.4'
4
Ph
1.43
-Yd
1%
I"Ar.
2.30
A^
1
2Vo
3.73
2
2
4.40
C18-515 GODO
Pipe Size 1 /8 Vd 1 h V4 I
birviihsibn A IY6 I i/b Is/is 1 1 2
Dimension H 1 Me VA I'-Aa 2 rAa
Approx Wt. .50 1.12 1.55 2.59 4.21 5.64
1 2 2% 3 4
235 MA 31%4 3 4
2 2 'h2 3%s 4 43/4 6
8.13 8-31 16.96 20.75 34.13
1 1'A 2 2 3
2 234 3 3 AV,@
2 3%s 4 4Y4 SY4
9.58 11.39 21.37 28.32 55.88
)Vu MIWKN A"9 MiSM Altv- I*b ru P11 F*zz
l ow
4;
,Class 2000
Y. "A -Y. 1 t 1 Yk 2 h
:V- 2 A I I 'A 1%& 17e VVIa 2Vis
Dimension H 1%4 1%4 1 1% 1 2 2 3 4
Appmx Wt. .32 .23 .45 .59 -90 1.40 1.65 2.63 7.63
Class 30M
4 1 1 1 V2 2 2N
Dimension A V-4: V'r 1 1- 1'!A 1 21k
Dimension .H 1111 11 A4 1 1'h I a/, s 2Y. 2 3 Ilk Nse 4
Approx Wt. .34 .32 54 .76 1.18 2J03 2.13 4.05 4.25 7.63
Class 6000
2 'h
Dimension A Vt 'A 1' IMe '14 lfib v ili 2A '2vla
Dimension H I%- M6 1 A 1 "/w 2;4 2 31& Weis 4 4
Approx WL .25 .59 .85 1.34 2.25 2.59 4.66 5.75 9.63 15.46
Elbows
4
214 3
4% 6%
12.00
3 4
2 3'/z
4 SY4
12.00 19-75
3 4
3%
31.21
Plass-3000 Not 61.6.11 Street Obo'w'"
W IVA
Pipe Size 1 Y4 1 1 /2 2 2% '3 4
Dimension LIM) 11.
2% 2 /a 2 3 i
Dimension A A 1% 1A 1-% 1 2 2% 2
Dimension H I I'Vis 1% 1% 2 2 2- 3Y%
App Wt. -25 .36 .53 .85 1.38 2.25 2.81 5.09
L (tatJ
Class 3000 -_VVej to.
ujljj J00iiii C Reducer
t I Vi: 1 1 4 2 M '3 A
'Dim VV I 'A 13A 1% 1 2 2 2i4 3% 3% 2% 4"A 4-74
Dimension D
VA V4 3 A 1 3'4 2V4 214 3 3% 414 6 Ya
Approx. Wt. m .10 .13 .28 .42 .8 1.50 2.19 3.02 456 6.79 12.00
Class AQ99 WO1101t kref"s to Full 40uponm4ft1v
Pipe Size y Y,
A .'A I
2 3 4
Dimension W 1 1% 1 'A VA 2; 23fa '2W' 3% 3% t*' 4
Dimension 0 Ph 1 1 Yk 1'A 1 9 /4 2Y4 2 3 3% 4 5 OVA
Approx. Wt. N .18 .14 .40 -69 .90 1.88 2.31 4-00 7.50 9.25 13.44 22.13 U 4
.Mqle: 'W" requirements to meet 815.11
sdfiiO JonqAL.s _vt0y;.
Q1a*s 3000 H41f 061A ng
1p4P Si ze I/ I/,
31, 1 1A 1i/i 2 Ui,- 1 4
Mi
imension W/2 s/. 'VIG 3 /4 1 5 /is 1 lVir, 1 9 /m s I 1 1 /15 TA 4 2
Dimension D L
3 14 V4 Il I Vs I VA 2 2 I/a 3 3 4VA 51/1
Approx. WL .06 .05 .06 .21 .43 .75 1.09 1.67 2.28 3.40 6.00
Jtlasswo-
-4
Pipe Size i V4
TV& 1 Va 2 2VI 3 4
Dime nsion W/2 9 /e Y16 3 /4 TIVI .1 1VIS 1 1 Vt a I'Vis 1% 2'A4 2
Dimension D 1 /6 1 1Y4 1 1 /3 1 3 /4 2%4 2 11 /a 3 3% 4A 5 6VA
Approx. Wt .09 .07 .20 .35 .45 .94 1.15 200 3.75 4.62 65.72 11.06
kt-.-. "AhIMr fa:- t- DIC 1 1 1 --f- than rltmon¢ inn¢ ehnwn..
Pipe Fittings
{NC
Forged Steel Fittings Pipe Tape
F or g ed St Fitti
Forged Steel 45° Elbows 2000 Lb. Reducing Couplings 3000 Lb. Forged Steel Bushings 2000 Lb.
Pert L t Part Part
no. i+ Sfze; Price 1. no. Size �Ltst Price'; no Size Price?
11106 114 ".J._51282.,I 111901112°x114'1 $7.98 ;i 11135C(1f4':x
8.1
31w] $12:82 I J':1191 J3(4" x..1 f2 -:$9AQ i 11350 {3/8' x 114 $2:28
1111661 112 i1.$t232 1' 1192 1 1 x 314" l $11.06 113611/2 x 7/0.1.$2,30
1107 314` $13.76, 1193117.' $21.94 1136A111/2"x3/81 $2:30
1108 „1 1 1 $16.1.8,. 111 93A 1 Y: x V 1,' $21,94 1137 .1314 x 114 1 $2.84
.E �..1194� 11 Ye° x.3/4'1:. ,$?2.14 i 1379 13 x 318 $2.64 :l
t1i01 1'fi 1.$2928,1 11194A1`t "h•x1 "1 $22.14 113783/4 °x112'1$2.90.:-
2 •1 "$q6 (16 )1194917 Ya° x 1 Y $2214. I i :60
`719 1138 1 1' x 114 $5
x1"
11179. 2rla 1311066 f 11951 2.X 1 b $28 80 113891 9, _X318 1 $5 60
I�= 95A} 2^x1/,"1 $29,60 1713881 i x1/2 1 $560
Forged Steel 90° Elbows 2000 Lb,
1196AI 2'k" x 2' 1 $108.54 .113801.1' x 314 1' $5.32 '1
1197 3 x 1 %i• 1 $140,92.. v• 1139 11 vi x 1/4 $8.92
Part no SIzA 1197AI 3' 1 $140.92 11399 �1'/.' x 112 J $8.92
;f 1 �t 197 3 x 2?/,° 1 $140.92 1113901 $8,92
10999' 1/4 .:$8.10
17390 J 1 x 1 1 $8.92 1
:10998.;1 $9.42
Square Head Plugs 2000 Lb.
1101 1314" 1 °x1 /4 +1 ,$9.101'
if00 1 112 1 1..SoA.u4,', Pert no Slze Llst Pric®:i t Y' I140AJih'_x 112'x' $0,24.•,,1.
,1: $9.76
,1 -_?1 1/4';1 $2,54 1'. K 1 74os11u x3140 $9.24 1
1102` I 1129 {3 /Hr.'j $2.04 1i,140C1,1hx1 1_$9.24
1 11091 711. 1$23 a F 8 1.,: 1.130 112 Ir $2.60 i. 11400 IA" x $924
1104 17Ya $31.20 1131 1314 :1' $324- _1141'12 421,
1� 1 026 i 1132 J 1
$4.60,, 1 1 1141Al2°x3�4 1$17,421
$6.76
82191 1133 1 l i 11478 2 .x 1 1$17.42
r s 1134 14z ;1 $9.82 1:7410 1 2 x 1 /e 1$17.42 J
Forged Steel Tees 2000 Lb. F
Size. 113 1 1
56 3 $6670 k 114 %F'J $&3073
Pert Ltst 1.1141H13 x7JA J$76308.
no Prtce Forged Steel Unions 2000 Lb 1:.11411 1 3 x 2 1 57s.DS'
1111Q 1/4 $9:54
List
1117 :3l6 $10.48 �Part no Size i) Price
1112 112' 1 $926 119969 114,. $14.(18,:
1 1113.:314 14.98 1.798 1 3/8'
7114 7 $20:40 1142 1 112" f,$18.10
fw Mft 1143..'1 3 /4• 1 $2254 1•
1116 14h ',839 `1144 .1- .:.1y.
l�`5 -1?bs
11117 2'h' $114.98
'1:148 1'1a
1 p
Couplings 3000 Lb Zii4T&� 2'b' ($1 52,49
1Part no. Slze 1List Price,
1117c 114 1' S4. Forged Steel Handlebar Unions Pasco Pipe Wrap Tape
11170 3/e• $4 1D_ 2000 Lb,. PVC plastic tape with special high tack
1 11 is I dhesi
ves formulated to resist corro-
a
1179 '1 314 I $540 Part no size ust 91o
PfiCO
1120 :`1 1M 1: $932 1.-$7,0.381
just
Pert no. SIze1MU Pecel
X1 51302 :1 1658 1 Y 16 109
',99 t, ano
p n
1122 1 i' $1526 71t35G 1 it/,' 1$t 16.081 an l
Ou ttry
11123 r $3730 u
1165D.4 2 1$1 33.39 9051 1 ,1°_x 100 8./10 1 48 J $8.10
1124 2 5j r2 '1165E I 2W ($252,91 J 9061 1 1' x 100 $120 ae
J, $13.68
1165E
ill 9052 1 2 x 100 R;jTO 1 24 $14.65
1 {2540 a s 3" 5365.53 8062 i', 2" x 100 R `1. 24 1. $28.2Q; :1
Prices sub)act to change'v.Ilhoul notice. Some Items may not be In stack F12 Rev. 4(2005
„al all warehouses or may be spoclal order. Please check ith w TEECO,
Order Online: www.tescaproducts.com Sacramento, CA Rapid City, SD Auburn, WA
e -mail: info @teecoproducts.com (800) 225 -6621 (800) 849 -8660 (800) 426 -9456
ASTM A 106
Seamless Pressure Pipe
Submittal Data Grades A B
Scope
Covers seamless carbon steel Grades A B pipe
for high pressure and high temperature service.
Pipe is suitable for bending, flanging, and similar
forming operations and for welding. Applications
include: Refineries, Power Plants, Boilers, Ship
Building, and other specialized applications.
Heat Treatment
Hot finished pipe need not be heat treated. Cold
drawn pipe shall be heat. treated after the final
cold draw pass at a temperature of 1200 °F or
higher.
Hydrostatic Nondestructive Electric
Testing
Hydrostatic inspection test pressure is 2500 psi
for sizes NPS 2 and under. Test pressure shall
be maintained for a minimum of 5 seconds.
Chemical Requirements Composition, Max
Carbon Manganese Phosphorus Sulfur
.25 0.27/0.93 .035 .035
Silicon Copper Nickel Chromium"
0.10 Min .40 .40 .15
Molybdenum Vanadium
.15 .08
"For each reduction of 0.01 below the
specked carbon maxim an increase of 0.06%
manganese above the specified maximum will be
permitted up to a maximum of 135%
a The combination of these five elements shall
not exceed 1.00%
When specified by the purchaser, pipe may be
tested by the nondestructive electric test in lieu
of the hydrostatic test.
End Finish
Plain End:
NPS 1 -1/2 and smaller shall be either plain end
square cut or plain and beveled at the option of
the manufacturer. NPS 2 ends shall be beveled
to angle 30 +5 with a root face of 1 /I6"
1/32
Threaded Pipe:
Threads comply with ANSI Standard B 1.20.1
Couplings:
Couplings comply with ASTM Standard A 865
Available Coatings
ASTM A 106 seamless pipe is available in four
different coatings:
Exclusive Blue Diamond Coating
Hot Dipped Galvanized
Pickled and Oiled
Bare
Tensile Requirements
Yield Strength, min 35,000 psi
Tensile Strength, min 60,000 psi
Elongation in 2" 35% Minimum
Bending Test (Cold) For NPS 2 and under
Degree Diameter of Mandrel
Of Bend
Standard 90 12 X pipe O.D.
Close Coiling 180° 8 X pipe O.D.
Frequency of Tests
Tensile tests and flattening tests are required on
one length of pipe from each lot of 400 lengths
or fraction thereof for each size.
Dimensions and Weights
The dimensions and weights furnished under this
specification are in agreement with the
standardized dimensions and weights specified
in ANSI B 36.10.
ASTM A 106 Seamless Pressure Pipe is sold by the following John Maneely companies:
Sharon Tube Company Wheatland Tube Company
134 Mill Street Sharon, PA 16146 1 Council Avenue P.O. Boa 608
Phone: 1-800-245-8115 x Wheatland, PA 16161 -0608
Fax: (724) 993-1031 Phone: I -800-257-8192
Fax: (724) -346 -7260
Container
Part
Start to
Discharge
Container
no.
Type
Setting
Connection
(PSIG)
M NPT
9545A1< I _DOT.
Pressure Relief Valves
and Relief Valve Manifolds. RegO
Flow Capacity .1 'It
CF Air"*
(ECIi Rated at List Price
480 PSIG)_
$11.00
R!
UL
1 Accessories (Order
i
Separately) Part na. Last Price 754 14 7545 -12
go.
Proteouv 'to i.(Includedl. L 7.545 -40 ,I. $210 ;I 8545AK Adapter Adapter
Deflectors* 46 Elbow 7545 -14*
90° Elbow: 7545 -12 $4.00
Classified by I.I.L. in accordance with Compressed Gas Association Pamphlet S -1.1 Pressure Demos Standards for Cylinders. Meets requirements for use on DOT containers with 262
pounds:or less weight of water or 109 pounds or less of LP- Sao. Flow rates are shown 4or bars relief valves. Adapters and pipeaways will reduce flow. Order protective cap #8545 -41
or 7545 -40.
e i r' Pressure Relief Va lves f or A SME C
Designed for use as a primary relief valve on ASME containers such as 250, 500
and 1,000 gallon tanks. Underwriters' Laboratories lists containers systems on asea
which these types of valves are mounted outside the hood without additional pro- series
tection, if mounted near the hood and fitted with a protective cap.
Start to Height Flow ,Capacity SCFM /Air Suiffible for
Container Overall
Part no i ,i)Seharge' Connection Height Above wrench Hex UL (at 120% of ASME (at 120% Tanks with Protective Cap .List Price
Setting M. NPT (,pprox.) CoaPltng Section Set pressure} of Set Pressure) Surface qre$ .(induded) i
a �rrox1. 1 ,to.
7503E 3l4' f8 3%16" U 17116 1. 7;980 I me 1 80;SQ. FL ?583-0OX I $34 70
8884E 250 1° 9 8 I.1 9116 1 718" 2;020 i, 2,565 113 Sq._FL 8684-40 I $3770
tat 5p 7 y� i
I. I li s' L 1.,.11116" i" 9 VII :a
4.385 i i 4 212 ft Fi 7585�OX i $56.60
Per NFPA Pamphlet #58, Appendix 0. Area chown Is for UL or ASME flow rating whichever is larger.
P:
"P R f Co ntainers
Destgne esptaolalty far is a as s pfi reAef rr lve 2° limovs ,3001 Y storage,
contailt8rs tht a #Owr pyv to relief Ye3
a tf gerieiali�r rriiaarrte i Ira half couplings:
t
HowevBr thEy 8fe deb gtied so:;hat le °.tti #et pats leaf the k> ottacn Of tali bu
piing 17,s gaSClreS that relief valve1,ioutd.,�siWays be ":espabie of,rr+axintum °flow
U nder ers$rgency ondit€ttns s3a2b
Accessories 75
Start'to Suitable for' 75348
Container Flow Capacity, $CFM 1 Air* rt 34G
Part no Tanks w!
setting Connection r" Ust Price
PSIG M. NPT Se[ Pressure) T Se! Pres sure). o1 Surface rea�P C tive� Adapter .i'..
1 5 6025 318 Sq. Pt. 75U 0 7534 -20
753dt3 *a
$477.20
f
<.rA 15675 �;.T
71 Po� 'Xfl$ 5 tS r $27.00 $97.50
Row rates are shbrin for tiare relief valves. Adapters and pipsaways will reduce flew. —Per NFPA Pamphlet #56, Appendix 0. Area shown is for UL or ASME Clow
rating--whichsver is larger, 3 F.NPT outlet connection.
Prices subject to change without notice. Some hems may not be in stock Al S Rev. 4/2005
at all war¢hogsea or maybe special order. Please check whh TEECD.
Order Online: www.teecaproducts.com Sacramento, CA Rapid City 5D Auburn, WA
e-mail: IrltaL@teeceproducts.com (800) 225.6621 (800) 843 -8660 (800) 426 -9456
Pressure Relief Valves
and Relief Valve Manifolds- RegO
Part no.
start to Container Height
Valve Wrench ne Pr�ptive lust Price
G °n
Material M i4
Setting (PSIG)
(app x)
tl
SS8001G
114'
11116"
i $22,40
Stainle
S580216
Steel 114W'
I[;
11!18"
114_N1
33670
250 112
318° NPT Thrds.
I $64.40
.3127,G
1/4"
7/�
3129G
i/2"
219!32
i 1/8'
3129.10"
$30.50
319711
1Y4
l; 1.311a2
718•
,j `$1640
312911
275
219/32" S
i i/8"
3129-10"
$30.50
7545.40
$5.60
31279
Brass 114"
i,31m
$2,10
$16.50
3129P
300
�r I/V
219132 '1
11/8"
3 -1
$30.50
3127)
1 /4"
131132" tl,
718
31 29)
1 /2"
219132"
1 1(8"
3129 -10
$30.50
SSBOQiJ
350
7/8
11/18"
i
$22 100_
$SBW2J,
Stainless 1/2"
I
1
718"
$47.00
1 SS8021J
Steel 114"
11/16
114'NPSM'Thrds,
;aj t*
SSep22J
1
13/8'
310 NPTThrds.
$64.40
3127K
114"
131/32 1
31/32"
718"
375
jfi j
754540
J
3129 -1D'
3129K
1/2
1 219132' 1
11/8
Y $2.10
$30.50
3125E t
1 9(16 .._.._:5/8,
Included
Brass:
1!4"
7 0
T
31271
131132
7/8
$1650
3129E
i /2"
2 i9/32
1 118'
312940P
3128 -10•
$30.50
400
SS80011
11118"
SSl.
Stainless 1/2
718
7!8
$4700
SS8021L I
Steel 1j¢r%
".F1/16"
1NWNPSMThrds.
1 318"
315...
r
7/8
Brass
754540
3129U
112
19/32°
1
1 1/8
$2.10
r $30.50
s�
450 I
718"
$2'100 .y
Stainless
716"
OQ:.
Steal x 1 W'! r
11(16°
y y
v
$58022U
r
112
1 318
NPT Thrds,
11fA0
12' F. NPi outlet
connection,
notice. Some Items may not be In stock AZi
,1.1 ...d.. G, .....a. D ..m°. xcen
3125L
SS8022G
Rev. 4/2005
f
Order Online: tluww.teecoproducts °com Sacramento, CA Rapid City, SD Auburn, WA
e -mail: info @teecoproducts.cam (800) 225 -6621 (800) 843 -8660 (800) 426 -9456
Designed especially for the protection of piping and shut -off valves where there is a possibility of
trapping liquid LP -Gas or anhydrous ammonia. They may be installed in pipelines and hoses lo-
cated between shut -off valves or in the side boss of RegO® shut -off valves.
rM M M11 M. M M. M W to. I zo M I LE M ".1 1 M 1 1 M :59101MMI E M. Wit
S bolffi� d" 1 "quire po��ff S,
bi k4t
Y
"a"Oe 0
nia P n the high gttaiity corsstructlor send wide Vaf BtS/ Of t3iztgB' A751 SAP A751
ei
Al
A7
A750SAP
A751SAP
Teflon seat discs on vatm t2ulft to order.
300# ANSI RX. Flange.
To obtain appr9;tImato Dow at other than I PS 10 pressure drop, multiply Pow in chart by square root of proanum drop.
taimplo: 7514FP @.9 PSIG 133 x square root of 9 389 GPIAlpropane. For NHS flow, multiply propane now by .90.
Prices subject to change without notice. Some Items may not be in stock
all,warehDussrs or may be special order. Please check with TEECO. A24 Rev. 4/2,005
Order Online: www.teecoproducts.com Sacramento, CA ;Rap City, SO Auburn, WA
e-mail: infog8rteecoproducts.com (800) 225-6621 (BT 843-8860 (800) 426-9456
Pan no-l"i-List Price
Flow at i PSIG
Moes6offes.1 Ust Price
Inlet and
Part
lFressure Drop (Cv)
Buna IN
Scat Discs
Teflon Seat Di scs*
Outlet
Dia
(CIPM/Propartelo-
Hydrostatic Vent Valve
01abo'
I MW 0 1
Globe
A6910
Connection
Globe. I Angle ;Relief
Valve
TA7034P
TA7034LP
1/2 NPT
i
10.0
1 14.8
$16150
$17050
3/4-
A7505AP
A750AP t
TA!sow
TA7506AP
3/4" F. NPT
12J0
17.7
$170M
A7507AP
A750BAP
TA7507AP
1" F. NPT
f
17.8 22.0
$145.90
$171.50
np
Atislosip
TA7509BP
TA7510BP
I
i
I F. NPT
1
36.5
54-0
$241 OD
U411.00 4
"12.111
$317.10
A751 1AFY
AmMp
TA7511AP
I'& F. NPT
43.0
55.6
$397.00
$443.0D
ssaoolu TSS31 69
A7511FP
i $22.0D $'15.60
Fla
1% ngs*
I
46.0
3.80
A751W
TA75i3AP
$352.60
$35t
$409.90
75.0 88.5
A7513FP
A7514FP
TA7513FP
.2" Flange"
79.0
133.0
_$1,21M.30
111
111
AtsvAp
J TESS F -:7
TA7517AP
$1.148.50
I f
$1,289.,10
3 11w
197.0 303z
AM7FP
A75i8FP
TA75ntm
3° Flange
J
$1,941,50
$1.841.50.
$2.51&60
Teflon seat discs on vatm t2ulft to order.
300# ANSI RX. Flange.
To obtain appr9;tImato Dow at other than I PS 10 pressure drop, multiply Pow in chart by square root of proanum drop.
taimplo: 7514FP @.9 PSIG 133 x square root of 9 389 GPIAlpropane. For NHS flow, multiply propane now by .90.
Prices subject to change without notice. Some Items may not be in stock
all,warehDussrs or may be special order. Please check with TEECO. A24 Rev. 4/2,005
Order Online: www.teecoproducts.com Sacramento, CA ;Rap City, SO Auburn, WA
e-mail: infog8rteecoproducts.com (800) 225-6621 (BT 843-8860 (800) 426-9456
Adapters, Connectors
Jed Tvoe Hose Counlinas for Vanar and Linuir,
as and
&ME
InI
Wam
IF Iw
threads are machined on a rugged steel insert which is i
permanently n
the aluminum handle, providing for durability under repeated use.
Part no.
Type Of
Hose
Connection M.
Coupling
Approximate
List Price
'Amm,
Service
NPT
Connection F
Length
Style A
Style 8 for
Style C
ACME
A75751_2*
liquid
2"
$122.8
A7575[ 3
fill
equalizing.
-470.80:
317S
Liquid quid
3171
3191
A757 .11,41
Series
$56.00
A767-51_6"
Style (I Hose connection :Coupling Connection tailpiece Bore Hose End to Nutt
I 'Al.
Li st Price
711
$118.30
A7571LA T
Length
31758
_$44,20
A7571LB I
Vapo
SW
1 "/4
Brass
$150A0
Inoludes 71M,33 adapter, shipped loose.
Includes A75 adapter, shipped loose
1 -J
A7571 A7675
Series Series
Short Type Hose
Couplings for Vapor
and Liquid Service
'Amm,
Style A
Style 8 for
Style C
Style 0
for liquid
liquid
for Vapor
for vapor
filling.
fill
equalizing.
equalizing.
317S
A31a5
3171
3191
Series
Series
Series
Part no. Material
Style (I Hose connection :Coupling Connection tailpiece Bore Hose End to Nutt
oviirair.
Li st Price
'Wrom 11
(F. ACME)
Length
31758
416.46
Brass
A 414'
1 YV
3/4
0
2 7/8'
S1.6.90
3175A
V 1.
516.90
1 Ve
2ye 13/16 1
2 1j18
$90-50
Brass NLrt'&
32 a^
7 m
AN 0 $123.90
Steel Nipple
iR
A.3fJF5- I
A 3'
1'/i"
71w
A3175A'_
ij
I S
Steel
$4M30
A31 65
B
2/" 1
217s"
A V1010F
A 3195
'A" 1 1311V
2 118'
3- 5/8�
1
3171,
317A
31W
I A 13/32' '1 1
7132"
13/16"
2 7/If
S13
3io J: Brass
314 C
4'
3181 A
7,18"
3 118
649.90
";Z 4
Prices subject to change without notice. Some items m no t b In stock
A42
flev. 4/2005
at�iil!veaT,boyses.or may. boppedal Bider.
Please check with TEECO.
Order Online: www.teecoproducts.com
Sacramento, CA
Rapid City,
SD
Auburn W I A
e-mail: infoCWteecoproducts.com
(800) 225-6621
(800) 843-8660
(800) 426-9456
Adapters,
PRODUCTS, INC.
Connectors Fittings
!RegO
ACME x Female NPT
A
BE
Spare Gasket
Part no.. Material
M. ACME
F. NPT
Hex
Diameter
Part No. List Ust Price'
5764Ai
1.' I
114
price
j
57648
30
$9.70
576.4C
1'1."
1' /x" 9.
A2697 20R
js $9.70
5764D
1/4"
1
314"
?0
_$9.70
$11.10
57648 Brass
1
$12.40urita*soun
apsi
5766E
j
2Y:`
1 J
2
25/16
1318
II
A31e4 -BR
I $66.30
ACME.Female NPT
5766E
I
I
1
$38.60
I $63:60
5768G
7'h"
3 W
3 5!8"
2 1/8
A3184 8R
$100:80
5768H
j`
$33.20
0050
A5764D i
1 j
3(4'
1 9
2 3116" I
314'
A2697 -20R
$40.50
A5764E 'I
I
1..
$7.70-
..j. $29.80
Steel
1194 -SR
A5768H
3' /a"
2"
3 Y<'
3
1 13116"
$10D.70
i
$33.20
ACME x Male NPT
A
B
C
JE
Spare Gasket;
Part no.
Material
D
Part No. Ust Ust Price
M. ACME;
M. NPT
Hex
Diameter
price,.
i 2TM 20R
5763D
1' /0
314"
1' /1
E 1Il
7118°
$7.70
$19.50
57650
3/4' ,J
17/8" I 11h6
$13.60
A2697 -20R
57655 J
74
1
13:°
2118"
3/4'
$7.70
$13.6b
6765F
j,
1 +I<• C
$13.80...
S7oir Brass
1' /a'.'
1 3116
S53 10
1 a
2
1 2
2 a/:'
2 5116 r
1 3/8
A318"Fi
5y 08.80
5767M,..
i
2318,
'i: 27/16 1, 25/6*
1 $73.00
5769H
2"... f
3 318"
i 2 718 11 17
x $33
$65.60
3
1
3
3 518' :1
0.
j, .$164:60
fimishaci uA h adapted
A5765C
17(32 i
$43.10
ACN�xMateNPT
A 5765D
314"
11116 f
A2697.20R
$35.20
1
y */a
23/16
7/8'
�i
$8.50
$24.20
A5765E_.
1 :I
I
y5116
$39.40...
Steel
2 /d'r$rc
1 R, 6
$75.6D
t7lv't
A5769F1
r €t'
R
4 +d t )r A
$144.30
A5769K
$181.90.
AL_
Prices "act to change wIftut notice, Some items may not be In stock A45 Rev. 4/2005
at all v2rehouses or may be epeclal oroer. Please check wllh TEECD.
Order Online: www.teecoproducts.com Sacramento, CA ;Rapid City, SD Auburn, WA
e -mail: InfoOteeeoproducts.com (800) 225 -6621 (800) 843 -8660 (800) 426 -9456
M Equipment
Including notagauges and ESV's RegO
dohWhor 'CO'n W, 1 '71"hily" rrt6it n n a standard 1°
0 'h
6416 MW" ef
;;�;4h ri., 'r b
opene Ih# 4,1p, AM, r WOV-ftmylzilrom
F3otogages�, the vent valve is rile ctzritainer vapor space
to th 6 116 J Id
I, rea Vat 690
of d '�i' eve K"
.'th o her.
P.O
Rotogage@ Dials A9091.18L
Oft Part-jno. _11, -Service 1, Container Size I List Price
Y A9091-18L LP-Gas Al(Nies
91 1 -1 LX Over 1,200 US
8 LP-Gas
Ago $22.20
Gallons
A9091-18N i. NH, Alf Sizes
Rotoaaae@ Orderinfa Information
4L
Part no. .1, List Price
or,doniafner Inside Diameter
i
For Use,with.LP-410s. For Use With NH, W Heads
For Mobile or Stationary, For Stationary For Mobile or For Stationary
Containers Containers Only Stationary Containers, Contalners Onl
Side Mounted End Mounted (Side Mounted End Mounted
Agogi-M60*
$M69—
Agogi
$66.60
A9091 -M60
80-99
I TW-W, 111.11 v__
So'-99
BW_99"
L r
supported Design, NOTE: The dip tube must be Cut to the required length.(W of container inside diameter minus 5 V4').
13/4" Rotogages(E� for Small Stationary and Mobile LP-Gas Conta ers
RotogagesO are designed to provide accurate determination of LP Gas container contents. They rnaybe end or side mounted
in a standard W NPT coupling on stationary or mobile containers. To guarantee ac-
curate measurement, they should not be used on stationary containers that exceed
60 1, I.D. or on mobile containers, subject to vibration, with an I.D. of more than 24'. 207000
'Parf
Bo. ,List Pric For Containers With Tank I Vawd seat
Rotogage DIP Tube I Inside lWarnater I _Cgnn
pqt onji, Orifice
"207000 2071125.7 $22.00 i Up to 40" .1
3/4" M NFIT No. 54 bat
690 ')0 up to ear J
NOTE: The dip tube must be cut to the required length (14 of container Inside diameter minus W),
Prices subiect to change without notre. Some Items may not be In stock A49
at ahwarehouses or may be special order. Please check with TEECO.
Order Online: www.teecoproducts.corn
e-mail: intooteecoproducts.com
acramento, CA Rapid City, SD Auburn, WA
(800) 225-6621 (800) 843-8660 (800) 426-9456
Rev. 4/2005
Miscellaneous Equipment
including Rotogauges and ESYs RegO
Si Fl ow Indicators for P lants
Designed to promote maximum pump efficiency, these indicators enable bulk plant operators to visually inspect liquid flow
conditions. With glass on both sides of the indicator, flow can be observed from either side, even under some poor light condi-
tions. The integral swing check also serves as a back =check valve to prevent reverse flow and product loss if the hose fails in a
loading. operation.
By installing an indicator on the upstream side of the plant pump, suction conditions III
can be observed and the pump speed adjusted to obtain the maximum possible flow
rate without cavitation.
Addi otlally,, fran fndldattor ls, lnstallle it) ,the,: piping at the loading rack, just ahead of
the l 60We tits doOtator carh<maintillm,a constant check on pump conditions.
Both Jinstaltatiotts 10 alltNgrfior observation to provide maximum pump effl-
+ciettay nd asspce safe. "IBM pump operation:
In compressor operations a sight flow indicator installed in the liquid line will give a vi-
sual indication when the tank car or transport is emptied. Compressor operation can
then be immediately reversed to start recovery of the vapor.
J inlet 1 outlet 1, 1
Part no. length List Price
Connectfons.. 1,
A7784 1 2 F. NPT f" 5'A" l $674:50
s r µ_>A,'7795- :':r' A �-'*.F. l mac"
E LI Away Valdes for T ransfer Operations
WAS
,y' s
A2141A10
Prices subject to change without nottoe. Some Items may not be In stock A50 R ev. 4/2005
at all Warehouses or may be speclal order. Please check with TEECO.
Order Online: www.teecoproducts.com Sacramento, CA Rapid City, SO Auburn, WA
e -mail info@teecoproducts.com (800) 225-6621 (800) 843 -8660 (800) 426.9456
Inlet/Outlet
Disconnect
Reconnect
Length of
g
t.P -Gies Glquid Flow Capacity at Various
Part no Connections F
Force A rox.
pp
Force
Valve
otfterentlal pressures:.(GPINy'..
List Price
NPT.
Ibs
Approx. lbs.
5 PSIG ll t 10 PSIG 25 Pella. I so Pella
A2141 A8
14140
A2141A6L 'L-
130
60
3 716
i 1 16 25 36
F..'
$147 40
i:.A2141A8L
1'
75
50
4 9116
21 30 7
$26650
A2141A10 ;1
1 ve l
160
25
,5 t/Br
52 t 75 1 .....120 1 170 1
$624.30
A2141A16
2"
30o I
50 1
14 6116"
.1 250 3tP 1 .550 1 750 1`
$2;486.70_
To determine NH Itquid flow capacity, muWply by .90.
Prices subject to change without nottoe. Some Items may not be In stock A50 R ev. 4/2005
at all Warehouses or may be speclal order. Please check with TEECO.
Order Online: www.teecoproducts.com Sacramento, CA Rapid City, SO Auburn, WA
e -mail info@teecoproducts.com (800) 225-6621 (800) 843 -8660 (800) 426.9456
Miscellaneous Equipment
Including Rotogauges and ESV's Rego
Especially designed for installation in liquid transfer lines at
LP -Gas or anhydrous ammonia bulk plants to provide for quick
shut-off of liquid or vapor flow in the event of an accidental
pull-away, line break or hose rupture.
Part no For Use Inlet and Liquid Flow dapacitil
with, Outlet at 10 PSIG Pressure' List Price
o n l y- Connections Drop (GPM)
WOMW V �RPV W 1
427 NN.
Ambis-1
Replaces 76058 and A7W58,
Must be actuated pneurnaticallyJ0*0 by cable or by cable connection to pall -awa val
r
L)r LP•Gla-; Sulk P
(R
Especially designed for Installation In vapor transfer lines at LP-Gas bulk
plants to provide for quick shut-off of vapor or liquid flow in the event of an
accidental pull-away or hose rupture, both of which can cause a fire.
For Use Inlet
Part no., with: Connection
M.NPT
A7781AFI LP-Gas 1,1 1 1/4"
A ESV Remote Cable Controls
ow Capacity
Outlet
Cc nnection.
Vapor at 100 PSIG
i. and 10 PSIG Liquid at 10 List Price
F. MPT
Pressure Drop PSIG Pressure
7609-50 Attaches to ESV and Bose for
Drop GPM
SCFH
AW
mdoo f.. 55 f_.$466.70
A ESV Remote Cable Controls
Controls
Part no. Description,
I List Price
Transfer cable release kit.
7609-50 Attaches to ESV and Bose for
$107.20
automatic closing as hose
7781AFPN-1
sketches.
$318,90
Remote manual cable release
pneurnexaAhutdo".
7606HM kit. Permits manual closing of $227.90
one or more ESVs from rem
ote
location.
Cylinder assembly M to
Remote thermal cable release
7605APN-1
kit. Provides high temperature
$234.60
76DSRT closing of ESV. Required 0
$116.1or
ESV Is more. than 6 last from
t)eareat end of hose.
1
:76061`1711 -1 100' roll of extra cable.
190.40
1 1601-c-m-n! 16.1bie link for
A3218 34
7605PN-50
7606RT.
$14,70
76058-20 Replacement fuse latch
assembly for 76058,
�107.70
11 AF
ESV Pneumatic
Controls
Cylinder assembly kit to
7781AFPN-1
convert 7781AF ESVz to
$318,90
pneurnexaAhutdo".
Cylinder assembly M to
7605APN-1
convatt 76058 ESVs to
$234.60
Pneumatic shutdown.
Pneumatic remote shutdown
system kit complete with 100'
7605PN-50
of tubing, fittings, 1 charging
$540.50
valve assembly and 1 remote
shutdown valve assembly..
7605AW8A
Extra shutdown valve
$248.50
assembly.
7605A-8T
EAM shutdown vave
assembly.
7605AP=I8
l 1141,tubf,ria t", w/nuts. j
$27.50 j
7605AP-15
iArNPTx 114" tubing, straights
$11.50
co nnector.
.1
Prices subject to change without notice. some items may not be In stook
at all warehouses or maybe speci order. Please check with TEECO A61
1
Order Online: Www.teecoproducts.com
e-mail; lnfb@teeooproducts.com
Rev. 4/2005
Sacramento, CA Rapid City, SP Auburn, WA
(8()0) 225-6621 (800) 843-8660 (800) 426-9456
121, Swing Chek ESV's for Bulk Plants
Miscellaneous Equipment
Including Rotogauges and ESV's Rego
0 4!ion an bulk storage containers, this valve combines a pressure gauge
f pr4insw!i.
fig1 1 Ahdlp
rV 061on for a fixed tube liquid level gauge. The shut-off valve prevents the
71 -A
re,:gaugwfdrn%!,befng subjected to constant pressure, thereby prolonging its life and ac-
c uracy. Ttfe valve'miiy be closed, and the vent valve opened to vent pressure from the gauge
to permit replacement. For fixed liquid level gauging, the valve can be mounted at the maxi-
mum permitted filling level. When equipped With a dip tube threaded 1/8" M. NPT, it can be In-
stalled at any convenient level.
Liould LeV61 List Price
Part no
Container ervice Cortnectioll v ent
Connection
Knuilddl $107.40
ra,
Has 11W R NPr opening for Installing separate dlp tube.
Designed especially f& JJS6 q _UId rNA fuel lines to trap foreign ma
1. 11 1 1 1 I
terial,which atherwisii'l'"'aly-darn ectiOn
age p r components in the LP=Gas
carburetion system. 'TheAp"'flWit'll' r Yet integral sintered metal
r;C0 PO. 0, an in eg
filter element in a straight through design.
t outletc6nnection I 1ist Price I
"1N61 1/4 F. NPT i/4"M. NPT _mflb
A280
Gauges
Especially designed in a variety of sizes and construction for the LP-Gas and anhydrous ammonia industry. All Reg0@ pres-
sure gauges have a 1/4 M. NPT connection unless otherwise noted.
P art no.
Service 'I
lmaterlaVl
case ill
maArnurn
Pressure
Case
Size
increment Division
List Price
J2434-2
Steel
oz.
2 'A"
1"w.r. and 1 oz.
$190.70
322SA-3
$16.80
30 PSIG
112 PSI
2411
Y;
B
5575
L -G
P
I
so PSIG
I PSI
t647
an lyas
Steel 4
100 PSIG
2 PSI
1286
$17.70
_$04.10
9486
3 0 0 PSIG
2 1;
5 PSI
$14.60
A8060
60 PSIG
ii
t69.60
A056
NH,
LP-Gaa
Steel
150PSIG
5 lb. j
75 60
AWO
400 PSIG
1
sa ba
114' Hose Connection
11V M. NPT Connection
5575
Prices Subject to change wtthout notice, Some fternr may not he In stock ASS Rev. 4/2005
at all warehouses or may be special order. Please chock Win TEEGO.
Order Online: no: www.teecaproducts.com Sacramento, CA Rapid City, SD Auburn, WA
e-mail; infoCuReecoproducts.com (800) 225-6621 (800) 843-8660 (800) 426-9456
Plant Equipment
IN Strainers
iron Strainers
Feature tough, weldable ASTM A395
type 60-40 .i0 annealed, nodular (duc-
tile) iron bodies. Stainless steel .027"
screens have a tapered, self-Migning
WA seat. Gasketed blow-off connections
wit h straight threads standard. 400 psi
W.0,G.
Description Ust Pricei
1je*rtyp gfrajhg�jron J, snqxo 1
-314! type stralner,4ron 1 $111.00
*,TY-V I I V46.60
$163.00
163-S
"J#60 I,. o.."Y!jype strainer; iron $279.50
Brags Strainers
Bronze body with steel plug. Blow-down
outlet for easy cleaning. 400 psi. W.O.G.
With 100 mesh stainless steel screen.
0 escri ption .11.1stprice
B110-ss i/2""Y"type strainer, brass 1 $41-18
8180 5 �'Il I aA"Y,'tybe.Etrainir,...brziss
BIM's 'Lir'Y" type strainer, brass .65
B162•13; j tvh,,!Y we sh brass 1, $131.42
Y t ie, strainer, brass j: $1151
B169-S.1- 2"Y"' t y .1 pe stralner, bta§s,. 1._ $206,38
Smith Precision Strainers
Designed for high pressure LP-Gas ser-
vice. Ductile Iron body, working pres-
sure 600 psi W.O.G. Less -resistance to
.flow, with readily removable screen.
)Part nci.1',. Deect [List price
NP
lt� NPT intii.xi14 ,T
1* NPT lnIef.xi*' NPT oUUdl" S29061
176-8 .1 TA' NPT)nlet x.9147 NPT outlet..... -)_$295.76
178.5 1 'A NPT inlet x V NPT outlet 1.1421108
.17S-3
.J 184-S j_2'..NFr, inlet x1VV NPT ouVet 1 $49"5
,I 186L.9 1::9 Inlet l(,2 NPT_ outlet 1 $42548
486,.9 fAl, 2'W.j NPT 1nIatxR NPT outlet 5565.02
LIEk j
_7_,L
ia wown,'r aass.m
Style 20
Single swivel for full 360' rotation in one
plane. 1000 lb. low pressure steel, for
LPG service.
low pres-
sure steel, for LPG service.
'Part DeSpilipt.1-d.n..
I U st.,pricd)
rice
I
2M75 1 3/4' swivel joint
1 T:t424"xj:
$4115.00
f
20-1-00:,1 VsWlVel joint
$460:0
0.00
i 20-114 1 1 Ile swivel Joint
1 1 $445.06
f 2CI-1561 1W'iWIVifi6I6t,
c
20-200 1 2' swivel Joint
$580.00.
Style 30
Single swivel with elbow to
permit
swinging at 90 angle. 1000 lb,
low pres-
sure steel, for LPG service.
Description
.11.1stwicel
34076 1 314'swivel joint, elbow
1 T:t424"xj:
30100.1 1 1 swiveljoint, Albow
f
30-114 t I'le swivel 16IM' 011DOW
$460:0
30160 ,j_1'W swivaLloint elbow
_1
30-200 2' swivel Joint, elbow
j ,srmob
Swivel Joint Accessories
Part no, Description
Ltst
price
#tChillsangreastil2lb-can-
'I W.00
#.7-f3filksan-girsase, tube
i i) $23.00
20308 i 114'sWel bails for '3/4" 1'
1: steel joints (42)
$8.00
W stsel bills for 1Y i W
2036C
$7.50
steel Joints (54)
2030D! 316" steel balls for 2' Joints 148). $13-10
Ff pale kit lot 26 �30 We
fH1ZK7j 1141 I IR joints
1 $34.50.
L131 K7> Repair kit for 20 a 30 style
314 -V" Joints_
L231IC71 Repair kit for 20 30 style 2'
joints
1'1,� $1 1 3S 6 C
Prices sub)ed to change without nallea. Some Items may rvol be In slack D8 Rev. 4/2005
at as warehousdi; or may be spacial order, Please chad( Will TEEGO.
Order Online: vriNwAdecoproducts.corn Sacramento, CA Rapid City, SD Auburn, WA
e-mail: infbCaUecoproducts.corn (800) 225-6621 (800) 843-8660 (800) 426-6456
PRODUCTS, INC.
Apollo Bronze Ball Valves
Bronze body, TFE seats and
seals. Rated at 600 WOG.
UL Listed.
1. 'Part size
ILISt prical
Lever Handle
$160-28
Part no.'..l Description_
List Price
80-101 114 bronze bag valve
$22.74'
80-1 02-6111 3je bronze cafi vgIve
$2214
1/2 ball valve
-JA
74
0 bronze ball valve
1 $3
ball valve
.']List Price
4 !Closed
f.1 $71,26
Wbronza,ball.valve
1 $86.82
I $CALL
112
60.1 09.011 AW.bronze ball valve-
1 $443.68
82i63W1110M NO j�,YNP1r_1j0VDC
.Z82.24
Apollo 3-Way Bronze Valves
SCALL
Bronze body. Chromium plated
ball, Reinforced TFE seats and
T,,IIQV,DC
stuffing obox ring. Large ports.
832 00 1 82-12VAC -i'3Way.1 NPT;12VAC
400 WOG rated. 90* operation.
0 NPTj2VDC
100% tested air under water.
fk&920r3182-110VAC,1 3-Way,1jWNPT,1l10VAC_1;'
Threaded.
Lever Handle
Normally Open
1. 'Part size
ILISt prical
1, 70-603-01 112
$160-28
70,504-01 314'
1 .$50.40
70-605-01
I 6722.33
Low Pressure Valves
5807EGTB I Aepalrklt. 1 for E790 valve, Buna-N
$219.50
ASCO Solenoid Valves
$242.00
1 Part n
.']List Price
4 !Closed
`1 82105(1 12VA6
2-0ay, 1 NPr 12VAC
[2Wav1
I $CALL
112
NPT
$CALL
82i63W1110M NO j�,YNP1r_1j0VDC
$258
1,'.a2isa3o ZmWiWNP`� 12VAC
SCALL
j B21503WINAC NW. V4- WFT, 11 it
-OVA
rsx4'60:1
T,,IIQV,DC
I $CALL
832 00 1 82-12VAC -i'3Way.1 NPT;12VAC
4"$CAU
0 NPTj2VDC
1 $240.00
fk&920r3182-110VAC,1 3-Way,1jWNPT,1l10VAC_1;'
09621
$CALL.
Normally Open
'02D(2119242VAC j _34vay_9' NPT.'12V AC
1 t:b*W.12VDC
_$r ALL
240.00
J�
10-210 J. l.(or As
$CALL
I
Plant Equipment
Valves Controls
VM W
Double union carbon steel ball
valve with 316 stainless steel
ball and stem. 100% full port
3000 WOG 150 WSP. UL
listed for liquid propane. Re-
versible 304 Stainless Steel
handle.
Part no. Deau rT Obn
100 -897 (.1 4 VV
T9 :DoU eunlon.bafl-vatva
$330.00
101-997 1 1 'A' Double union bill So cket Weld end I _$330M
100 -598_, I 2'.Double union ball.vatva $450.00
101 -998 f 2' Double union ball valve., backot wakLend $4.00_
Mar•ac Steel Double Union Ball Valves
Forged carbon steel
body. Rated to 2500 psi.
UL Listed. Available with
TFE or Buna-N seals and
seats.
Lever Handle
Part lid.
TFE SeaW/Seata IBuna-M S013 ISIS a'atal Description ILISt Pric
CS-M0.MLIA25 I CS- E790-TBU-125 $666.60
C$-E794-TT1.17150 I CS-E790-TBU-150 11 IM? steel ball valve 1'$748.54
Cs-127904TU-200 I CS-E790jPW 250 1 T.-PW.01ball valve I $822.52 11
Repair Kits For E790 and 8790
Part no
List Price
6807EFFT l Repair kit 1114", for E790 valve, TFE
$160-28
5807EG1T.1 Re pair kF(J for 5190
$201.66"
5807EKrT '1. Repair.kk 9", for E790 valve, TFE
I 6722.33
5807EPT8 L 1`46pilr_K 1 UVAbi E760 valve8una.N.
5807EGTB I Aepalrklt. 1 for E790 valve, Buna-N
$219.50
58071EHM ]Ribdle kit. 2'. for E790 ve Suha-N
$242.00
5807FrT Repair kit. 1W, for 8790 valve, TFE
1, $174 48
'680107 I Repair kit I Va'. for 6190 vsJve, TFE
59071,M J Repalr Idt. 2", for 8790 valve, TFE
S258.90
5607F113 )Repair kd 1Y' far 8790 valve, Buna N
1 '$174.48
5807078 I Repair. kit_1%%,1dr,B790:valve, Buna-N
J S219.50
j 5807HT6 1, Repair W i'13790valy I e, lhi I it 7 W
...to
IMMM1111
$258
212* F. fusible link for KCC8
Internal valves.
1, Part-no. J, Description-,
List PrIceL
.2001-FL Fusible link
$64.00
Prices subject to change Without nofte. same Items may not be in s tock
at an worehWOOR Of may be Special order- Please check wtM TEE00- DIG Rev. 4/2005
1
Order Online: www.teecoproducts.com Sacramento, CA Rapid City, SD Auburn, WA
e-mall.* lnfoC&teecoproducts.com (800) 225-6621 (800) 843m-8660 (800) 426-9456
PRODUCTS, INC.
Hose
Hose
High Pressure Hose
High Pressure LPG Hose
350 psi maximum working pressure. UL Listed. 7132- 25354E -350 sized for shipment by UPS,
Pa P a id W1./100 Reel Standard Lest
Par( no. 6lze LD She O.D 5 Ira! /Bra' N
Price /foot
e
7132 45354, 1/4 _1 7/B4" .R spirals i4.ibs.. j.. 700 $1.52
i 7132 25354E -350 t 1/4" 1 7164° ,J 4 spirals 1: 14 11211, j 3617 i _$1.36
i 7i3248754 I WT.., I 314" 4 4.splrais 22 lbs. l 550'. is $2.82
:.-7132 50354 j 1/2' 15/16" l 450' i $3.92
44 SpIlWa 30lbs
i
71 75354 1 3 r li 1 h a spirals 42 Ibs, j 300
32
71321DD354 11 1.1 1 J: 4 spirals ,1 82 ibs I` R!50 t ffi876.
R ,f�txl3.1 1 1 2tirattls.: 98112 300' I $1510
1 2?hs' I, 3 braids ',I 114 Ibs, 150° (i $21,10
72321503..:.. 16 1
-;1.42 Ibs 150
High Pressure LPG Hose Stainless Steel Reinforced
Rubber_coyer 350 psi maximum w0rking pil"sl re. UL Listed, Cut lengths -bulk lots 300' to 400':..
Part no. Size LD
Size O.D. 8rald aNelght/100 ft Standard flat
Resisize l� Price /toot.
7233 -31.1 318 l ,.43/64' 1 19 Ibs. 500' i $3,46'
7231-751' i 3/4° 1 ,1 f Y.', i 1 59 1tts. 700' L- .$21.08
7231 10t)1.._ 1 1.h' 1 75 Ibs ,l too' $27.86
7231.1251 l I W i 1 31i 1 1 92 ibs,
1 DQ'_ $36.96
7231 ?1501K ,i .:._.I 1 h" l 2° 1' l l 113 Ibs.
i 151Y j $51.90
7231 -2002K 11. 2' 1 R'laa" ,1, 2 1 __:1671bs. 1 150' I, $79A0
High Pressure LPG Carburetion Hose Stainless Steel Reinforced
Textile braid cover. 350 psi maximum working pressure, UL Listed. Cut
lengths -bulk lots 300' to 400'.
Part no.. I. Size 1-0. i Size 0A 1 Welght/100 ft° {'list Price /foot
e
FC321 -04 i1 'I/4' i 33!64 1: 1.11 a i.: $4.94
J_ _:FC321 08...._ J 112- j 49/64" i 21fbs $5.68'.
33 FC321 12.... 3/4, l: 1'Jba" 37 Ibs- ffi13,46
Lo P ressure
Low Pressure General Purpose Hose Red
LP- Gas.vapor -only service. Recommended *HNatft Buie 125 .psL.Rubber coated.
i 1
Part no Spirals Size I.D.
Size 0.0 WeIgM/i00 ft Standard List
Reel Size Price /foot'
712262_._..... 1 2 3/8"
21/32" i 14.9 Ibs. 650` 1 $1.96
LPG Vapor /Water Heater Hose,
Standard
Part no.. Size I D Places List Price /toot
i Package
VHB l 516 3 1. $8.84
YLi34 f 3/4 "30 J" 5 i $sale,
YH 78 7/8" I 3f1. ......._._.l` 3..::,:. $6.00
30'
VH 100
1 30' j 3 $9,60 1
VH 112 1........ 1Yi
'Vacuum Hose
1 Part. no. bbacdption: l List Price /foot
340-VH J, Vacuum hose, 3/1'6 1.0. a:, .97_
341 VH 71, Vacuum hosa,.11.4' L0. 1i $1.29
i
342 -VH Vacuum hose, 318° I.D. SCALL
Prices subject to change without notice. Some Items may not be in stock E1
Rev. 4=05'
at all warehouses or may be special order. Please,dreek with TEECO
Order Online: www.teecoproducts.com Sacramento, CA Rapid City, SD
Auburn, WA
e -mall: info@teecoproducts.com (800) 225 -6621 (800) 843 -8660
(800) 426 -9456
Flexible Stainless Steel Connectors
Stainless steel corrugated metal hose with a stainless steel braided jacket and heat shrink cover. 350 psi working, 1750 psi
burst pros
01ftings size C List Price Part no. I Fittings Size t .lJ st Price. .1
k; F50 -S10
F50 -S24 1
F75 -S18
F10041
F100:824
#1 25-924' 1
17150-SIB
Ground Joint
Union x MPT
1`20"11.8
F200-824
F250,518
`17250 -k4
MW4.
Other sizes available upon request.
!Inv
Hi•h Pressure Hose Fittings
High pressure fittings are for hoses which have a 350 psi working pressure and 400 lb. pull test.
lamp Type Couplings
F50
1/2' x 18'
1 $78.04
1/2" x 24' J
$88.14
r
112' x20
$88.14
_314 i 1 13'
$88.1,4
3/4' x I IT'
J $68.14
11 314" x 24
XDBN-1 112!'
05,82:48
We x 24"
F $66.32
_SW J
$109.92
I
V x IT
T p :4r,.
I x W 1
$13290 1:
1 FIMSM
!'.x 24
$125.68
'$GA
F126wSI85
1114' x I a,
1 $119.16
A Y 24
V
$176.52
1`1254248
x 24°
is
$160.54
MPT MPT
1.. F150SY8S
lth"x 19"
l $134.16
I I W,'. x 14! 1
$197.74
F150-S243
117$155.52
f 2' i(18
3241.34
Z Is'
1 $110.66
-TX24'
5900.S24S
2 k Ir I
sms.9z.
Ve x 18'
1 $286.54
2 x 04". J:
t
I400.96 I
W)i f4',
$3 15.22,
M A4
473
RMISS-
3' x 18
I $351,94
.1 fr 7 7t' ,$5 4 2.46
MW624S
�T i1 4'
$4 00
!Inv
Hi•h Pressure Hose Fittings
High pressure fittings are for hoses which have a 350 psi working pressure and 400 lb. pull test.
lamp Type Couplings
AtAlle!"'or malleable iron clamps with
steel stems. Reusable.
Part no. I Hose I.D.
Iii4imtIn q
List Price
3/W MPT
XDBN-1 112!'
TM
=1 O
_SW J
__...3/41
I
1. '1
T p :4r,.
tPALL v
R26*120 JI Y y 1'/' 1"'
$CALL
K24N-124.__- .1 W
'$GA
1(32N-132. I 1-';_
't
ACALL
K32-
.1. �1 'i I
Steel Hose Couplings
,Swivel w1hex nut for stainless steel wire reinforced Ime
Price
'r n End Angle
H
Pitting
318 1 1/4' PT 44.83
318 I 318' MPT
2082014_4 _�144
3/6
2080-8-8 1/2"F.
$12.20
30061 Flare 45'
$14.86
27920-4-4 1510.16
90' $14.60
27920-8-8 I
7/2" Flare i
4W
Prices subject to change without notice, Some Items may not be In Stook E3 Rev. 4/2005
at aft warehouses or may be spedal order. Piewa chankMth TEECO.
Order Onflne: www.teecoproducts.com Sacramento, CA Rapid City, SD Auburn, WA
e-mail: info(pteecaproducts.com (800) 225-6621 (800) 843-8660 (800) 426-9456
Pressure Gauge Adaptor Test Block
The J595 adaptor is installed in the outlet of a Flrst -Stage regulator to
indicate the outlet pressure use with J500 Series gauges.
Type J600 test block connects to the container valve to check for
leaks in the downstream system.
Type J595 -1/2" MNPT x1/2" FNPT, adaptor only.
Type J600 Male POL x Female POL, test block with 0 -300 psig gauge.
M
Test Gauge Assemblies
The Type 50 Series is used to check appliance line pressure
after the regulator has been installed.
inlet
T Manifold
,j ype of a
Piping
bor
Connection
Hose
Plastic
Inches
Inches
Inches
1/4 MN PT
Nc
Female POL
Yes
Yes
Female Hose
Yes
I No
Tee. Block
Pigtail at
T Manifold
,j ype of a
Piping
Regulator
Tee Block
Tee
Connection
Connection
Without
Inches
Inches
check)
Check
Female POL
Female POL
Male PO,L
P400
_114 MNPT'....
P413
1 /4lnverted
1/4 MNPT
P414
Flare
Bottom Back
Co nn ection Connection
Pressure Gauges
Fisheroffers pressure gauges with either a bottom or back connection
for LP -Gas service. The back connection makes a more compact
assembly on installations where space is limited. All gauges have a
2-inch diameter face /steel case.
PRESSOR. E GAUGE F FtANGE, PSIG
Connection 4 Inches 0-151,
0 -30 't. 0 80 0 -16tl 0 300 -400
F 1 iii 111111
Bo tom ril4 J500 J501 J502 J504 J55' J542'
Back J510 J511'f 512 1 J514
i. For LP-Gas or ,*#t service.
22
Emer Sh
Snappy Joe® Emergency Shutoff Valves for
Bulk Plants
Snappy Joee Type N550 Emergency Shutoff Valves (ESVs) are
designed for in -line installations, usually near a bulkhead. The
valves provide a means of shutting off gas in the event of a hose
rupture or piping break at the transfer area to avoid a large scale
loss of LP-Gas or NH,.
The valves can be manually opened and closed at the installed
location or closed remotely by either cable or.,'
operating actuator Is also available.
High Flow Capacity -The main poppet moves
the flow stream for extremely low restsietian
Operational _Ease Moving the,ct .Y'
across a bulkhead. All sizes look similar and z'
same, an important point in an emergency situation.
Fusible Element The fusible element is located at the hub of
the operating lever and stub shaft When exposed to fire, the
element melts allowing the stub shaft to turn. The poppet then
moves to the closed position, even if the operating lever has been
wired open.
Rugged [isttuotitirf Heaujr .dut+Cpn3huct(ofnmakesStB�py
Joe® ESVa suitable for u ad:a shutcfl'valve'torftie:,
transfer aria,. evell;.vitde7 Snegue�+t :use.. Thr3 )ritensaf °dosing
spring rs protered freuri the eleittertts and tartsering All semis
and seals rise meLi',taeck�tlA. seals for`axtehtlet <t5re t�esfstarictr:
The valves are rated 400 WOG.
Ease l tr 'wSol' m 6 removal from the pipeline.
Parts (hat lr ina eidb iat4t d ;can be changed out in a matter
of minutes: Thte packing can't)e r#iahaed with the valve In -line.
Type Number
N550 w/ P327C
Cable Release Standard valves are fitted with a release
mechanism for cable attachment. A cable connected to the wire
loop allows closure from a safe remote location, such as the bulk
plant entrance.
While the ordinary cable can be used, the Type P164B release
bty is available. This "assembly uses 50 -feet (15 meters)
Stttg...which does not require elaborate guiding like
Remote pneumatic closure is available
etease. Depending upon valve inlet pressure,
pressure of 30 to 70 psig (2,07 to 4,83 bar) on
to be latched In the open,position with
Upon loss of pressure, the valve closes, assisted by the spring
in the pneumatic cylinder. All necessary installation hardware for
the P327C is furnished.
Fisher makes available a small 3 -way control valve (T1139599012)
for pneumatic E8V Installation, This control valve can be used as
primary control (open or close the ESV) or an auxiliary remote
release (close only).
Placing the valve's button in the upward position permits pressure
to the cylinder. Pushing the button down exhausts pressure to
close all valves connected to the system.
Accessories
P164B bible Release
P327D Pneumatic Release
P327C Air Cylinder
T1139599012 Control Valve
W
Emergency Shutoff Valves
Body Size
Flow In GPM Propane
Inches
1 P$117 2 PSID
1 -114 FNPT
s0
2 FNPT
75 115
3 FNPT
100 275
Accessories
P164B bible Release
P327D Pneumatic Release
P327C Air Cylinder
T1139599012 Control Valve
W
raw F L OPe M AX L
+lade in 1ne
Dry Break Transfer System
Ti.'F n• 4
AAEBb6 t6 `y v Patent
f
n Pending
ME868 �6 snbevarve
Nct Ir tided
Aml i cation: For ruse with LP gas transfer systems.. This revolutionary system provides a safe, ergonomic and efficient solution
to LP Gas transfer applications while increasing productivity and dramatically' reducing fugitive product emissions. for use with
bobtail, transport, :railcar, and bulk plant- applications.
Features:
Minimum $350 $avings per 1,1100 fills (See reverse for payback chart)
Reduces product emissions 99.6% over standard valves
100% ,corn,patible with all existing Acme transfer connections
Heavy duty spring loaded safety latch prevents accidental opening of valve
Cam operated vapor equalization feature for smooth valve operation
Hardened steel bearing race Wth stainless steel ball bearings for maximum product life
All stainless steel internal components C' D Listed
Factory installed =,hydrostatic relief valve
Gonvenient carrying ,'handles and custom fit dust plug with lanyard
f
Low Emission Transfer Valve
Pan No. Desc19p8on f D ivletenal
lNE$06 1.6:
RpWxVE low Emissioh Trans r Valve °2" 1 NPT x 3174 F. Aome SWvel Connection l 09 CC DuctflelBrass
haw £missien Acme Adapters
pan T40. Descoplioa Nleffi�ial
Ater
M E 8 6 6 Eir�H7nx].F Low Emission Acrrae 1 WMP7 x 1 -814 M Acme 16 CC Brass
ME8S6A_$
E Lowrrnssinn 71eme.Atyapter 1 ivINPTx 9 =314 1N. Acme vmth Witter Screen tfi CC Brass E
'l0 Iq
F1 7cLE row l mission Aare ltaapter 9 11d M13P1 x 1 31� U. Acme 1 a 6 CC Bra
i�llEBb$A;�D
Love Emission flcme.Adapter 9 �a4 MNPTx 1-374" U. Acme with Fitter Screen 16 CC
1 Brass
ME8S? 1: FZ,o3r]�t E 114 tv1T7Pixz-lxU.A Am- 9.86_CC I SrQSS
ME867A -i 1Ft ariiE- LowEmissonAcrneAda
pter1- MNPTx2' Ii r4 "M191:>0.crnewrTFi Fitter Screen y 1.96 C C Brass f,
FLoNlaxi E .Low Em "fission Aflme Le WIN x 3 114" 4u1. Acme 3.91 CC Brass
1 f io-TIAxLELOW'E m> ssionAameAdapter. Z' MNPTx3- 1J4"- M.Acme- WjIhFilterScreen 3.t'rCC'I Hrass
lV1,E8E$ 24 r.tn3rlaxt Lowl:miss.onAcm Adapter3 "MNPTx`3IX' i 311 CC Brass
flA E 13`6 B A 2 3:. �ntplFixL t Lnw Emission A Acme.' da- t 3" M"W" T x 3 -174" TvL Acme with Filter Screen t 3.11 GC 'j Brass
Ascesoayes
Pan!Nn
1 M.E`8_S$Y71116.. 1 Brake Intelock Reim Fit MA for ME86&16 8 24
11A E P i ID8 i Heck Check Test Adapter `Brass for IVIEB6i3 i S ME868 24
a aced• onIndependentNattona l Board -Labort desTestirig
For Your Local lljlarshall ExceJstor Distributor Call 289 789 -67 00,
Fax 26'9 81 -8340 or:E -maj]: sales @marshallexcelsior.com
`Q www.marshallexcelsior.com
W4
4.-
Ns-
1'
Model
FP4 -750
Station Monitor
4" ASA 150# raised face flange with full flow 2-1/2" waterway
Built with standard long radius weld fittings with 2 -1/2" NH stainless steel discharge thread and red epoxy
finish inside and out
Capable of flows up to 750 GPM
Available with optional 2 -1/2, 3 ,4 N.P.T. female or male base
Height 22 (plus 14" tiller bas handle) width 13 weight 45 lbs.
Please visit www.fi!e p romonitors.com for most curre spe cificdtion s.
FIRE PRO NOZZLES AND MONITORS
17451 HURLEY STREET CITY OF INDUSTRY, CA 91744 USA
877 -917 -5800 626 -937 -4723 FAX 626- 937 -4707 E -MAIL info @p fire romonitors.com s•�„ o+: t�475o:
ooe: 9/1 /OB'
Fire Pro is a member of Acorn Engineering's Family of Companies
w
Model
FPw500B
Master Stream
Nozzle
500 GPM aluminum master stream nozzle with Delrin seat for shut -off feature and 180° full fog
capability.
Can also be preset at 300 GPM.
"As cast," bead blasted finish.
Please visit www.firepromonitors.com for most current specifications.
FIRE PRO NOZZLES AMD MONITORS
17451 HURLEY STREET CITY OF INDUSTRY, CA 91744 USA
877 -917 -5800 626 937 -4723 FAX 626- 937 -4707 E -MAIL info @firepromonitors.com submi D 9 B:
Fire Pro is o member of Acorn Engineering's Family of Companies