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General Specifications
Conforms to the latest edition of the ASME code for
Pressure Ves€9, Secfion Vill, Division 1. Complies with,
NFPA 58.
Rated at 250 psig from -200 F. fo 125' F All tanks may be
evacuafed to a full (14.7 ps)) vacuum. '
Vessel Fmish: Coated wrih epoxy red powder. ( Tanks coated
wMthe epoxypowdermustbeburied).ForAbovegrounduse, tanks may be coated with TGIC powder. $�
$EF
UD
Applicable federal, state or local regulations may contain
specific requirements for protective coatings and cathodic
protection. The purchaserand instailerareresponsible for
compliance with all federal, state or local regulations,
VALVE
FJTTINGS LAYOUT UNDER DWE
AGUG VESSEL DIMENSIONAL INFORMATION
AD vessels dfinensionsweap ropmate
WATER
OUTSIDE
HEAD
OVERALL
OVPRAI I
LEG
LEG
WEIGHT
QUANTITY
CAPACITY
bMEfER
TYPE
LENGTH
I
HEIGHT
WIDTH
SPACING
FULL PER
LOAD STAG
120 wg.
24"
E_ llip
5 - 5 13/16"
3' - 0'
10 1/8'
3'- D°
24516s.
96 12
.54.2 L
6D9.6 mni
1671.3mm
9114 mm
267.2 mm-
914.4 mm
111.1 kg,
250w19..
31.5"
Hem[
-P-2 1/2°
3'-7 1/2"
12 3/4"
3'-6°
472lbs.
09
946.3 L
800.1 mm
2197.1 mm
1104.9 mm
323.9 mm
1066,8 mm
214.1 Pg.
320 Wg.
31.5"
Henri
8'-11 314"
3' -7 U2"
12 3/4"
4' - 0 1/4°
588 Ibs.
45 9
.1217.2 L
800.1 mm
2736.9 mm
1 V4.9 mm I
323,9 mm
1225.6 mm
266.7 kg.
500 Wg.
37.42°-
Henri
9'-10"
4'-1 7/16"
15"
5'- D"
87i Ibs
30 fi
18925 L
950.5 mm
2997.2 mm
1255.7 mm
381.0 mm
1524.0 mm
3951 kg
1000 Wg,
46.96" I
Hem! 15-10 13116"
4' - 4 5/16° 1
16 1/4"
9'- 0"
1729 Ibs,
15 5
3785.01.
i 040.4 mm'84��
-, m
1344.6 mm
412.8 mm
2?-',3,2 rrn;
34,3 k9
Rat, Jan. 27,2016
Why Tanks corrode
_-Underground steel tanks, corrode due to an electrochemical reaction
between the tank and the surrounding soil. The process a, corrosion
occurs due to small voltage differences on the steel surface that result
in the flow of DC current from one location to another. Where current
flows from the tank into the so!] corrosion occurs_ This location is called
the anode in a corrosion circuii Where current flows from the soil to the
tank, no corrosion occurs. The progress of corrosion is determined by
the amount of current flowing between the anode and the cathode and
whether the locations of the anode/ cathode remain constant overtime.
Corrosion rates are generally higher In wet soil environments since the
conductivity Of the soil promotes the flow of DC current in the corrosion
circuit.
Corrosion -generally exhibits itself an underground tanks in either a
general overall rusting or more commonly, a pitting attack Phlocations
may result from metallurgical conditions of the steel surface or soil
variations such as rocks, salts, fertilizer, moisture concentration, oxygen
concentration, eta
Preventing Corrosion
Protecting underground
tanks from corrosion Is
easflyachfeved bythe use
of two commonlyapplied
protection methods:
external coaling and
cathodic protection.
These two methods
are complementary
- - and should be used in
conjunction with the
other. An effective
extemal protective
coating insulates the steel from the soil envlronment, thus preventing
thetiow of corrosion currentfrom the anode to the cathode. An afiective
extemal coating can proteotover99% ofthetanksorfacearea However,
no coating is perfect. Damage from construction orsoll stresses create
tiny defects, which may result in accelerated corrosion atthe defect
Cathodic protection prevents corrosion at those defects by applying
DC current from an external source, forcing the tank to become
cathode. Appflcallon of sufficientDC cunerdto the tankwill preventany
corrosion from occurring. The two general types of cathodic protection
systems are sacrificial and impressed current. Sacrificial systems are
used when the amount of current required for the protection is small,
such as to underground propane tanks. Impressed current systems
are more commonly used for large structures such as large diameter
pipelines. Electrical Isolation of the tank irom metallic piping systems
arrd'electdcal grounds is critical for the cathodic protection system's
effectiveness.
How Sacrificial Cathodic Protection Works -
Sacrificial systems work by creating a galvanic cc 'Hon between two
different metals. The most common anode material is magnesium,
which when coupled to steel results In DC current flow from the
magnesium to the steel. The open circuit potential of steel -is about-
-0.50 volts referenced to a copper sulfate electrode. The open circuit
potential of magnesium Is about -1.55V to-1.80V, By connecting the
two metals together, the difference oft to 1.25Vvelts results in current
flow to the fankthat overcomes the natural corrosion cells that exist on
thetank. With this current available to the tank, no corrosion occurs.
Ndag;resiurn Anodes
There are a variety of anode sizes and alloys used for cathodic
protection. The two primary alloys are designed as H-1 (orAZ63) and
High Potential. The H-1 alloy is produced from recycled magnesium
and has an open circuit potential of approximately -1.M. This alloy
is well suited for protection of underground propane tanks. The High
Potential alldyls 99% pure magnesium having an open circuit potential
Lip to-1.8V. This alloy should be used for soil applications over 10,000
ohm -cm resistivity.
Tha two most common anode saes used for underground propane
tanks are 9lb. and 1716. The size designation relatasto the metal weight,
10' of #12 TW insulated wire is attached to the anodes. Anodes are
then backlifed in a mbdure of gypsum, bentorute, and sodium sulfate
to lower the electrical resistance of the anode to soil. The mbdure is a
low Cost, nonhazardous, electrically conductive backflll. The anode and
backnll is then packaged in a cotton bag and effhera cardboard box or
paper bag. Actual shipping weight of these anodes with backfill is 27
lb. and 451b.
AppPoatdon Recommendations
Magnesium anodes can protect underground tanks in most soli
conditions. The H-1 alloyfs generallyveryeffective. The following chart
provides size and quardtyrecommendations forvarious size tanks based
on conservative design assumptions. This chart covers soil conditions
up to 10,000 ohm -centimeter resistivity. Resistivr'b'es higher than
I ligo ohm -centimeter generally represent very dry soils. Verification
of soil resistivity can be performed through sod analysis. Contact us
for design recommendations in locations Mere soil n:sistivities exceed
10,000 ohm -cm, or if there is no elective external coating on the tank
The propane service line from the tank to the house also must be
considered in the cathodic protection design, unless the service Jfne
is plastic. All underground steel pipe should he externally coated with
a corrosion resistant material. The service line should be electdoalty
isolated at the house with an insulating fitting or union. ff service pipe
is less than 5o' in length, the lank anodes will provide sufficient current
to protect both tank and pipe. For longer lengths of pipe, an additional
anode may be required at the house connections.
If another metallic material such as copper is used for service piping,
the pipe should be elecbfcally isolated from the tank at the fill pipe
connection. Copperandsteal create agalvanic couple thatwillaccelerate
corrosion of the steel tank when directly connected to copper piping.
Generally, copperpiping does ?aqulre cathodic protection.
wiechanical Connection Under Dame
Calhodic Protection Testing Procedure
Equipment Needed: Digital Voltmeter, Red Test Lead Min.12' Long
& Black Lead Min. 2' Long, Reference Electrode (Copper/Capper
Sulphate Half -Cell)
STEP 1: Using a digital voftmeterinsertthe red test lead Into the Volt
jack of the meter and select the 2 or 20 volt DC scale. Clip red test
lead connector to an uncoated metallic area of the tank, preferably
to the fill pipe multivalve. A good solid connection is very important.
(DO NOTconnect to shroud).
STEP 2: lnsertthe black test lead into the Common jack on the meter,
and connect the opposite end of the lead to a charged reference
electrode (14 cell).
STEP 3: Remove protective cap from the porous plug at bottom and
of electrode. Place porous plug end into native soil (remove grass if
necessary) at four locations aroundthe tank{ona on each side of the
tank, and one at each end of the tank). If difficulty is encountered
obtaining readings, moisten soil with water or dig 111 cell deeper into
the soil.
STEP 4: Record all four meter readings on an appropriate form. The
least of all four readings should be a minimum of-0.850v or more
negative. Mots: If any of the four readings are below (loss negative)
-0.850v then the 'tank is not fully protected).
Charging deference Electrode
87EP 1: Unscrew and remove porous plug and of new reference
electrode. Add deionized or distilled water to the copper sulfate
crystals, filling electrode completely. The solution will turn blue in
color and there should always be excess crystals at the bottom of
the tube. DO NOT USE TAP WATER.
STEP2: Replace porous plug end of electrode andplace in an upright
position so that the porous plug end is facing in the down position
and let stand for i hour before use. This will allow the porous plug
to become completely saturated before use.
Caution: Danofallaruelecfrnde fo confacf e11, read salts, arafher
substances that may cauiamlaafe the solution byabsarplien
fhrcugb porous plug. Do gatafloweleefrnde to freeze.
Based an 90 effective menial ceahng, 2mv)V cunentdens&,, and 30-
yearAnadelife.
Anode installation
1. Determine size and quantity of anodes from application chart.
2 When a single anode is installed, it should be located near the
tank center on either side of tank.
3. When multiple anodes are installed, space them evenly around
the tank See examples below.
I J 7 anode a ar+ades al
Q
4.Anodes are shipped in either cardboard boxes or multi -wall
papersacks. Remove ouiercontainerandburythecloth bagged
anode. If anode is supplied in plastic bag, remove plastic bag
before installing.
5.Install anodes approximately two to three feetfrom the tank and
at least as deep as the center line of the tank Anadesworkbest
in locations with permanent moisture, so generally the deeper
the better.
6.After placing the anode, stratch out the anode connection wire
and extend overto a connection point on the tankfill pipe.
7. Cover the anode with approximately six inches of bac>sfill and
pour 5 gallons of water on the anode to saturate the prepared
badd11. Water is necessary to activate the anode.
8.Connect the anode wim to the tank with a low electrical
resistance connection. E:amplas are threaded stud on the
tank fill pipe or any accessible metallic connection point to the
tank All connections should be coated with a moisture -proof
material.
9.ideally, the tank connection is made in the area of the tank fill
pipe within the covered dome. With access to the anode wire,
subsequent testing of the tank can include measurement of
anode output and verification of performance,
1o.Vedfy performance of the anode using an appropriate test
procedure.
Loss of Pressure
Freeze-up inside the regulator.
This will prevent the regulator from regulating properly.
Regulator freeze -ups occur because there Is excessive moisture
in the gas. Freeze -ups can also occur In pigtails that are kinked or
bent where free flow of the LP -Gas is restricted. These freeze -ups
can occur when the moisture, gas flow and temperature combine to
create a hazardous condition. Freeze -ups can occur at temperatures
above 32'F.
Action Required: All LP -Gas should be checked for moisture content
prior to delivery to consumers and proper amounts of anhydrous
methanol added if the gas cannot be returned to the supplier. Any
container suspected of having excessive moisture should be treated
with the proper amount of methanol.
Customer Safety
Since regulators are often used by consumers Without previous
knowledge of the hazards of LP -Gas, and the LP -Gas dealers are the
only ones who have direct contact with the consumers,
it is the dealer's responslbllity to make sure that his
customers are properly Instructed In safety matters relating
fo theft Installation.
At the very minimum, it is desirable that these customers:
1. Know the odor of LP -Gas and what to do in case they smell
gas. Use the NPGA "Somfoli'n Sniff' leaflet
P. Are instructed to never tamper with the system.
3. Know that when protective hoods are used to enclose
regulators and/or valves, that these hoods must be closed,
but not locked.
4. Keep snow drifts from covering regulators.
5. Know the location of the cylinder or tank shutoff valve in
emergencies.
Underground Installations
Special hazards can occur if regulators are not properly installed in
underground systems. Water, dfr4 mud and insects can get into the
regulator If the bonnet cap is not tightly In place and the vent is not
protected with a proper vent tube, opening above any potential water
level.
Most problems occur because the waterproof dome on the buried
storage tank does not extend above the ground level sugiciently to
keep out water and mud. Refer to NPGA No. 401.
Rcyup:oradjus =Tdvsum
vpmustbe A.ht I e.a,
led above Iha hrghasi
waterlevd.
orslcmdIng
61Kh�=ft m /
(tarnch zminunumif
subjectto veNailar troGd.
Note: Water mark left In housing dome at level
above regulator vent, or end of vent tube requires
replacement of regulator. Then correct installation.
General Warning
All RegO Products are mechanical devices thatwill eventually
become inoperative due to wear, contaminants, corrosion
and aging of components made of materials such as metal
and rubber. As a general recommendation,Regulators should
be replaced in accordance with all of the recommendations
outlined in this safety yarning. The recommended service
life of a regulator is one of many factorsAhat must be
considered in determining when to replace a regulator.
The environment and canarnons or use will uetuil"I". um auc
service life of these products. Periodic inspection and maintenance
are essential.
Because RegO Products have a long and proven record of quality
and service. LP -Gas healers may forget the hazards that can occur
because a regulator is bsed beyond its Seib service fife. Life of a
regulator Is determined by the environmerd in which it'lives.' The
LP -Gas dealer knows better than anyone what this environment Is.
NOTE: There is a developing trend in slate legislation and
in proposed national legislation to make the owners of products
responsible for replacing products before they reach the end of their
safe useful life. LP -Gas dealers should be aware of legislation which
could affect them.
M
_ rf� • 100 RnO Dr. Eton. NO 2725 _ xvnere9"pmdu4seom +t (336) 4494707
First Stage Regulator
-- - with Relief Valve and
Second Stage
tar
rge Vent and
a Tap
ice regulator is truly the head of an 1P-Gas installation. It must
=rni ensate for variations in tank pressure from as low as 8 PSIC`s
'M PSIG — and still deliver a steady flow of LP -Gas at 11' We.
.s consuming appliances. The regulator must deliverthis prewura
:.E;�p.;a a variable load from intermittent use of the appliances.
=wh a single -stage system may perform adequately In many
-_-t�'Oons, the use of a tWo-stage system offers the ultimate in pin-
p:zt regulation. Two -siege regulation can result in a more profdabla
;f%zs operation for the dealer resulting from less maintenance and
e,T=r Installation callbacks — and there is no better time than now for
`stalling Rei Regulators in two-sthge systems.
tf larm Appliance Pressure
The tnstallatlon of a two -stage system — one high pressure regulator
a me container to compensate for varied inlet pressures, and one
sv pressure regulator at the building to supply a constant delivery
g assure to the appliances — helps ensure maximum efficiency
a d trouble -free operation year-round. It Is important to note that
w5iae pressure at the appliances can vary up to 4" w.c, using single-
-stage systems, to -stage systems keep pressure variations within
1= w.c. New high -efficiency appliances require this closer pressure
Control far proper Ignition and stable, efficient operation- In fact, one
,,4or manufacturer requires the use of two -stage systems with their
aaplances.
Reduced Freeze-ups/Service Calls
Regulator freeze-up occurs when moisture in the gas condenses and
_ezes on cold surfaces of the regulator nozzle. The nozzle becomes
chilled when high pressure gas expands across It into the regulator
body. This chilling action is more severe In single -stage systems as
eas expands from tank pressure to 114 w.c. through a single regulator
nozzle.
Size The System Correctly
Prior to installing your two -stage system, be sure the system pipe
and tubing Is property sized. Proper sizing will help ensure constant
delivery pressure to the appliances during fluctuating loads at all
times. Just as important be sure the Rego Regulator's you choose
are capable of handling ilia desired load. This is another advantage
of two -stage systems — they are capable of handling much
more BTU's/hn than single -stage systems. The Rego 'LP -Gas
Servivenlan's 141rnraN providua =1n iu Ir a3?n rn pip' sizing
and proper regulator selection.
/ r—To Applianaes/Fumzce
Two -stage systems can greatly reduce the possibility of freeze -ups
and mulling service Gals as the expansion of gas from tank pressure
to v w.c. is divided into two steps, with less chilling effect at each
regulator. In addition, after the gas exits the fist -stage regulator and
enters the first -stage transmission One, it Picts up heat from the line,
further reducing the possibility of second -stage freeze-up.
Service calls for pilot outrages and electronic ignition system failures
are also reduced as a result of more uniform appliance pressure from
two -stage systems.
Economy of Installation
In a single -stage system, transmission line piping between the
container and the appliances must be large enough to accommodate
the required volume of gas at 11" w.c. In contrast, the line between
the first and second stage regulators in Mao -stage systems can be
much smaller as it delivers gas at 10 PSIG to the second -stage
regulator. Often the savings in piping cost will pay for the second
regulator.
As an additional benefit, single -stage systems can be easily
converted to two -sage systems using existing supply lines when they
prove Inadequate to meet added loads. This is the least expensive
and best method of correcting the problem.
Allowance for Future Appliances
A high degree of flexibility is orered in new installations of twc -
stage systems. Appliances can be added later to the present load —
provided the high pressure regulator can handle the Increase — by the
addition of a second low pressure regulator. Since appliances can be
regulated independently, demands from other parts of the installation
will not affect their individual performances.
Replace Pigtails
If you are replacing an old regulator, remember to replace the
copper pigtail The old pigtail may contain corrosion which can
restrict flow. In addition, corrosion may flake off and wedge
between the regulator orifice and seat diso — preventing proper
lock -up.
.Mi°➢9 �>Stc43ll�lL�e� tr�l l�yS�NS'S`ZS�t' 2C6SatSL�-.l VmyS�
First stage Regulator
vrlthRelief Valve and second Stage
Pressure 1 Tap Regulator with Large Vent
and Pressure Tap
To Appllancas/Fumace
FirstSthgs Piping) ----
With no first stage relief valve,
propane liquid may form here... 70° F. 120 PSIG 40' F. 72 PSIG
Resulting in sudden pressure surge due to flashing into vapor herel 80' F 140 PSIG 50° F. - 86 PSIG
First stage relief can prevent liquid from forming in first stage piping gal F. 165 PSIG so' F. 102 PSIG
during periods with no gas damandl I I
Pressure at which liquid can form
at various temperatures,
Vapor Pressures of LP -Gases
W
a
m
m
m
m
Q.
Temperature OF.
The Problem
Many modem LP-Ges appliances are egpippedwdh plotless Ignition
systems. Water heaters and older appliances use plot lights, but it
has become a common practice for energy conscious homeowners to
shut-off the pilot when leaving home for extended periods of time. In
each instance, there Is no gas demand at all for extended periods.
The Consequences
If the first stage regulator falls to lodt-up fight usually as a result
or worry seat disc or foreign material lodged between nozzle and
seat disc, pressure will buildup In Ina first stage piping — possibly
to a level that approaches lank pressure. Combining this with warm
ambient temperahrres and cool ground, propane liquid may form to
the first stage piping_
When gas demand resumes, this liquid may, pass through the second
stag6 mqulator into the appliances and filmaes. NOTE —the second
stage regulator will not relieve the pressure in firststage piping.
The rapid vaporization of the liquid may cause a rapid pressure surge
that could seriously damage critical components of the appliance and
furnace controls.
Afire or explosion could occur as a consequence.
The Solution
RegO LV4403 Series First Stage Regulators with Built -III Relief
Valves reduce the possibility of this serious hazard In two stage
applications. The built-in refer valve is designed to vent as needed
and reduce the possibility of first stage piping pressure from
becoming high enough to forth liquid.
t
MM . 100 Regn Dr. acq — 144 USA wvnv.2goFmduGs. am +1 (396)4497707.
Ideal for use asafirst stage regulator onany do, nes5cstzeASMEor
• DOTwrdatner In propane gas installations requiring up to 1,50%oilb
BTU's par hour. The regulator is factory set to reduce container
pressure to an Intermediate pressure of approximately 10 PSIG.
Mmdnmm Ow.V and
on NW preessu 20 % IGhrghenn theharzgnlaWrselSrg antl dmiveuypresnue 20Y.lwrutllzn
the regu�crs-1Gng and delinry pmssur 20X Imrrlhn Ihesel6ng.
Provides accurate first stage regulation In hvo-stage bulk tank wrte
systems. Reduce tank pressure to an inlemlediale pressure of 5 fo 10
PSIG. Mso used to supply high pressure burners for applications like
Industrial furnaces or boilers. Also Incorporated in multiple cylinder
Installations.
�fiiPr�E.TiR.^i� r�S'aC+QZ•f°v�'�rv�
LY4403SR4 ,W F.
5 .1-5
LY4403TR4 NPT W F. 10 540
LY4403SR9 NPT 5 1-5 Yea2,500,000
W44030i9 V.
10 5-10 ,
LY4403SRS6 F. POL >„ 5 .1-5
LV4403IMS F.NPT 10 5.10
• YMen used rwimal stage presswe w:feul, must eMerinrnrpo; teinle32r refiefi^.Ne wserruate reGert�Jveshauld be Spz�edNaan+darxs
with NFPAP=pMet 59.
^ Maxianan ll wbasedon rnletpre=are 20 PSIG hfeherthanthe ,,umarseltha and derwwy pr'-aure 20% lawwfhan the segfng.
Designed to reduce first stage pressure of 5 to 20 PSIG down to
burner pressure, normally 11' w.c. Ideal for medium commercial
Installations, multiple cylinder installations and normal domestic
loads.
Lv44me4 . 34'
LY440aR96 % F NPi 11' w.o. at
LY4403B48R° #2B 10 PSIG 9'vta 93" Over Inlet
LY4403H66 '/•° F. NPi Dd0 Inlet
LY44U3B66R' '/< F NPT
'6adannwtd�ign
^ nnmlanun fwwtrseP on t0 PSIG inlet and e'w.m Cererypressme
i
935,OD0
Mdv"AR
&94403sedes
&944a SM-J �
Job Name
Job Location
Engineer
Approval
Raidble Gas Appli.2nce
The flexible connection between the gas supply and the gas inlet
Of a Ganelace Stationary OutdoorBackup/Slandby Generator.
Features
o Operating Temperature-9°Fto 150°F (-40°C to 65,6°C)
• Operating Pressure MAX Q6psi (3.45 kPa)
e Hydmalatic Burst Pressure MIN 26opst ('1725 id'a)
• Rodble Tube Matedal Annealed 804 Slainiess Steel
• Flare Nut Material Carbon Steel With ZNc Tdvalent
Chromate Plating
e Rare Adapter Material Carbon Steel with Zinc Trivalent
Chromate platingi
GSA Group Certificate of Compliance to
Product Standards
ANSI Z21.75/CSA'6.27— Connectors for Outdoor Gas Appliances
and Manufactured Homes
Scrape states °... intended for exterior use above ground formaidng
non -rigid connections ... betWeen the gas supply and the gas inlet
Of an epp➢ante for outdoor Installation that Is not frequently moved
aBertnsta➢ation.' in addition section 1.6.4 states the connector is
designed for occasional movement after tnstal etion. Repeated bend-
ing, flexing or extreme vibration must be avoided. Normal opera-
tion of clothes dryer, roer7op HVAC unit or SIMILAR OUTDOOR
APPLIANCE DOES NOT const1hute extreme vibra5on or movement.
ANSI Z21.24/CSA 6.10— Connectors for Gas Applfancas
(Excluding B0161 Swiss)
All Mida tans mustcompiatelymmpy ra'ih a➢Demmnt memrfactudog Company vrmnings
andiosbudong national, dada End iocalcodes and a➢2011cable awl standards
ES-D-GAC GerleratoL Ganerac
Contractor
Approval
Contractor's P.O. No.
Representative _
SKU
r „{ V' J
ll(
T
For use with Generso
stationary outdoor backup)
standby generators.
,
Series 30, 40 and 60
Applicable Codes
ANSI Z223.'VNFRA 64 National Fuel Gas Code Section 9.6
Intemetioral Fuel Gas Code (IFGC) Section 411.1
13149.1 — Natural Gas and Propane Installation Code
(OSA Group) Section 6.21
UnWorm Mechanical Coda (UMC) Section 1313.0
Unfform Plumbing Code (UPC) Section 1212.0
Additional Approvals
commonwealth of Massachusetts Board of State Examiners
of Plumber; and Gas Fitters
Additional Testing
1.11-2200-2016: SIntionary Engine GeneratorAssembFes
Section 66B Vibration Test.
tE� �1f�^1-�=;j�•:ll �", ems'
A WXAM, Brand
n
f.7O7xo arum Capaai;y cf PZ Pips Jr.
wlin a Gam, Pre5:l ire of I
1073
720
571
484
425
1391
934
740
627
551
7983
1331
1054
893
786
-3563
2397
1894 -
1605
1412
4724
3247
2608
2232
1978
70063
6765
5351
4635
3989
P/ta4mum capoclh/ cf PE Plpe In The
wlth a Gas Pressure of;
(posed on
scfBTU.erHOufofUr, uefi9dPst-,19L!n Ges
and a Pressure drop 6f 0:5 in. WC
58 54 51 48
46
44
42
40
75 70 66 63
60
57
54
52
107 100 94 89
85
. 81
78
75
192 780 169 160
752
146
140
134
303 285 269 255
244
233
224
216
549' " 508-" 476 ' 453
431
411
394
379
2516B711h=1CFH
s of 8TU per Hour of Uquetled Pet(leum Gas
and a Pressure DTbp of 1.0 psi
1966
1319
1045
886
779
702
595
b23
4/1
461
3w
j/o
001
auy
Zia
11300
7686
6008
- 5092
4479
4033
3418
30D7
2707
2478
2295
2144
207E
1776
1592
T4652
9835
7790
6602
• 5807
5229
4432
3698
3510
3213
2975
2780
26T7
2302
2073
20877
14D14
1T100
94DB
8275
7451
6375
5555
5002
4578
4239
3962
3729
3280
2953
37514
25183
19946
769D5
14869
13389
17348
9982
89BB
8226
7618
7119
6700
5894
53D7
43429
2934E
23969
20515
18182
16474
14100.
12496
11322
70477
9697
9092
85B9
7612
6897
105963
71131
56339
47750
42000
37820
32D54
28194
25388
23234
21517
20108
IBM
16647
14990
1355 1192 1075 910 BCD 720 659 611 577 537 508 484 462 443 425
7757 1545 13121 1779 1037 934 855 792 740 696 659 627 599 574 551
2503 2202 1983 16BO 1478 1331 1218 1128 1054 792 939 893 • 80 818 786
4498 3956 6563 3019 2656 2397 2189 - 2027 1894 1783 7688 1605 7533 1469. 1412
6903 5232 4740 4D57 3596 3253 2997 2788 2676 2471 2347 2239 2744 2060 1985
12705 11175 10063 8529 7502 67M 6182 5726 5350 5036 4767 4535 4331 4150 398B
2516BTVWCFH
Maximum CappacOy of PEPTpa in Thousands of 67U per Hour of Uquelled Petroleum Gas
with a Gas Pressure of T0.0 psi and a Pressure Drop of 1.0 psi
2476
-1662
1316
7176
981
684
749
659
593
543-
603
410
442
389
35u
14234
9555
7568
6474
56V
5080
4306
3787
3470
3721
2890
2701
2542
2236
2074
78455
12388
9812
8316
7315
6587
55M
4910
4422
4047
3747
3502
3296
2899
2611
26296
77652
78981
11849
10423
9385
7954
6997
6300
5766
5340
4990
4697
4737
3720
472M
31720
25723
21293
18729
16865
14294
12572
11321
70361
9595
8967
8440
7423
6685
53960
37087
29782
25489
22597
2D469
17579
115527
14068
12943
72041
11297
1D671
9458
8569
33476
89601
70967
60148
52905
47640
40376
35514
31980
29267
27104
25329
23840
20970
78882-
1707 IJim 1352 1146 1008 907 830 769 719
2213 7946 1753 1485 1306 1176 1077 997 932
3153 2773 2497 2116 1862 7676 75M 1421 7328
-5665 4983 4487 8803 3345 3012 2757 2553 23B6
7334 6500 6890 5041 4460 4048 3724 3465 3257
16MM 74077 12676 10743. 9449 8509 7787 7212 6739
676
640
609
582
557
586
877
830
790
754
723
695
1250
T183
1125
1075
1030
990
2246
2126
2022
1931
7857
7779
3071
2916
2782
2664
2560
2466
6343
6005
5712
5465
5227
5024
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