HomeMy WebLinkAboutTank specs AR
120-2,000 w-,!
Aboveground/Underg round Domestic
Finished with ArcClad"
Superior Aboveground Coating
S Tank Features:
• Dual service options for above or under
ground 3pplications
Option 1 Superior, ready to bury, red
1:3 oxide dL rable powder coating with black
polyeth ien dome*
Option 2, Aboveground option with
8" dome in black plastic or galvanized steel A.rcCl coating and an 8" steel
AG U G d m e
` dannc'�'116 r-��eymyyyd
�R�C4Jd�5.16
Fabricated toA.S-M.E-code,5ecdonVlli,Divis ion I All valve and float gauge are centered
Registered with the National Board under dc me
- - - . . ... .■.
For more information #Vacuum Purged - - - - - -- -- • - -- - _..
888.558.8265 ■ #72 liquid level outage valve orifice
AR
Aboveground/Underground
OVERALL.LENGTH
DOME i
[U N I II
u
I ,
o OUTSIDE II
w p ❑IAMUER E II
0 o j IT j
o I II I
LG
W I EDTH
LEG SPACING
WITHDRAWAL
r--� VALVE
GENERAL SPECIFICATIONS FLoa DYKE1�1 _ANODE
GUA E p•GAS CONNECTION
Conforms to the latest edition and addenda of the ASME code for 0 FILLER
Pressure Vessels,Section Vill,Division 1.Camp lies with NFPA 58. 0 VALVE
Rated at 250 psig from-202 F.to 125°F.Alf tanks may be
evacuated to a full(14.7 psi)vacuum,
Vessel Finish:Coated with epoxy and red powder.(Tanks coated MuiTIV VE -PLATE
P Y p �- PLATE
with the epoxy powder must be buried).For Aboveground use,
tanks will be coated with ArcClad,zinc rich epoxy primer and VALVE
super durable TGIC polyester topcoat.
"Applicable federal state,or local regulations may contain specific requirements For protective coati igs and cathodic protection.The purchaser and
installer are responsible far compliance with all federal state,local and NFPA Industry regulations.C ith ad!c protection is required and coating must be
continuous and uninterrupted and must comply with focal,state or national code,
AGUG VESSEL DIMENSIONAL INFORM
Water Outside Head Overall overall Leg Leg Quality
Capacity Diameter "type Length Height Width spacing Weight Full Per
Load Stack
120 wg. 24" Ellip 5'-513/16" 3'-3/16" io 1/6" 3'-0" 245 lbs. 96 12
454.2L 609.6 mm 1,671.6 mm 919.1 mm 257.2 mm 914.4 mm 111.1 kg.
250 wg. 31.5" Hemi T-21/2" 3'-711/16" 12 3/4- 3'-6° 472[bs. 63 9
946.3 L 8003 mm 2,197.1 mm 1,109.6 rnrn 323.9 mm 1,066.8 mm 214.1 kg-
320 wg. 31.5" Hemi 8'-11314' 3`-711/16' 12 3/4' 4'-01/4" 588 lbs. 45 9
1,211.2 L 800.1 mm 2,736.9 mm 1.109.6 mm 323.9 mm 1,225.6 mm 266.7 kg.
500 wg. 37.42' Hemi 9'-10, 4'-15/8" 151, 5'-0" 871 lbs. 30 6
1,892.5 L 950.5 mm 2,99-1.2 mm 1,260.4 mm 381.0 corn 1,524.0 mm 395.1 kg
1000 wg. 40,96" Hemi 15-1013/16' 4'_5 3/16" 16114" 9'-U, 1,729!bs 15 5
3,785.0 L 1,040.4 rnm 4,846.6 mm 1,350.9 mm 412.8 mm 2,743.2 mm 784.3 kg.
All vessels dimensions are approximate. Eng.Update: Apri]5,2016
For-more information
888.558.8265
- - - • - 1 1 1 1 1 � 1. 1 . e
Why Tanks Corrode different metals The most common anode material is magnesium,
Underground steel tanks corrode due to an electrochemical reaction which when coupled to steel results in DG current flow from the
between the tank and the surrounding soil. The process of corrosion magnesium to he steel. The open circuit potential of steel is about
occurs due to small voltage differences on the steel surface that result -0.50 volts ref i anced to a copper sulfate electrode. The open circuit
in the flaw of DC current from one location to another. Where current potential of m ac nesium is about-1.55V to -1.80V. By connecting the
flows from the tank into the sail corrosion occurs, This location is called two metals toge her,the difference of 1 to 1.25V volts results in current
the anode in a corrosion circuit. Where currentflows from the soil to the flow to the tank at overcomes the natural corrosion cells that exist an
tank, no corrosion occurs. The progress of corrosion is determined by the tank, With tf is cu rre nt available to the tank,no corrosion occurs.
the amount of current flowing between the anode and-the cathode and
whether the locations of the anode/cathode remain constant over time. Magnesium An c des
Corrosion rates are generally higher in wet soil environments since the There are a va iety of anode sizes and allays used for cathodic
conductivity of the soil promotes the flow of DO current in the corrosion protection. The wo primary alloys are designed as H-1 (or A263)and
circuit. High Potential. he H-1 allay is produced from recycled magnesium
and has an open circuit potential of approximately--1.55V. This alloy
Corrosion generally exhibits itself on underground tanks in either a is well suited for protection of underground propane tanks. The High
general overall rusting fir more commonly,a pitting attack Pit locations Potential alloy is 9%pure magnesium having an Open circuit potential
may result from metallurgical conditions of the steel surface or soil up to-1.8V. This alloy should be used for soil applications over 10,000
variations such as rocks,salts,fertilizer,moisture concentration,oxygen ohm-cm resisthfily.
concentration,etc,
The two most c mmon anode sizes used for underground propane
Preventing Corrosion tanks are 91b.an c 171b. The size designation relates to the metal weight.
Protecting underground 10' of#12 TVV insulated wire is attached to the anodes. Anodes are
tanks from corrosion is then hackfilled in a mixture of gypsum, bentonite, and sodium sulfate
easily achieved by the use to louver the ele ct ical resistance of the anode to soil. The mixture is a
of two commonly applied low cost,no n haza rdaus,electrically conductive backfill. The anode and
protection methods: bac4ll is then pac kaged in a cotton bag and either a cardboard box or
external coating and paper bag. Actual shipping weight of these anodes with backfill is 27
cathodic protection. lb.and 45 lb,
These two methods
are complementary Application Reco mendations
and should be used in Magnesium an s can protect underground tanks in most soil
conjunction with the conditions. The H 1 alloy is generally very effective. The following chart
other. An effective providessizeand uantttyrecommen data nsforvarious size tanksbased
external protective on conservative dE sign assumptions. This chart covers soil conditions
coaling insulates the steel from the soil environment, thus preventing up to 10,000 oh in-centimeter resistivity. Resistivities higher than
the flow of corrosion current from the anode to the cathode. An effective 10,000 ohm-centimeter generally represent very dry soils. Verification
external coating can protect over99%of the tanksurface area, However, of soil resistivity c n be performed through soil analysis. Contact us
no coating is perfect, Damaga from construcfion or soil stresses create for design recom rn andations in locations where soil res 1 stivitie s exceed
tiny defects,which may result in accelerated corrosion at the defect, 10,000 ohm-cm,o if there is no effective external coating on the tank
Cathodic protection prevents corrosion at those defects by applying The propane servi a line from the tank to the house also must be
CC current from an external source, forcing the tank to become considered in the athodic protection design, unless the service line
cathode. Application of sufficient DC current to tha tan kwiII prevent any is plastic. All underground steel pipe should be externally coated with
corrosion from occurring. The two general types of cathodic protection a corrosion resistant material. The service line should be electrically
systems are sacrificial and impressed current. Sacrificial systems are isolated at the hau e with an insulating fitting or union. If service pipe
used when the amount of current regaired far the protection is small, is less than 50'In IE ngth,the tank anodes will provide sufficient current
such as in underground propane tanks. Impressed current systems to protect both tan and pipe. For longer lengths of pipe,an additional
are more commonly used for large structures such as large diameter anode may be required at the house connections.
pipelines. Electrical isolation of the tank from metallic piping systems
--- -acid-electrical grounds is-critical for-tha cathodic protection-systems, If another-m-etaiiic aterial such as-copper-is-used-far service pining;------
effectiveness. the pipe should be electrically isolated from the tank at the fill pipe
connection. Copp r and steel create a galvanic couple thatwiII accelerate
How;Sacrificial Cathodic Protection Works corrosion of the stf el tank when directly connected to copper piping.
Sacrificial systems work by creating a galvanic ccnnactinn between two Generally,copper pi 31ng does not require cathodic protection.
Soil Type Fertile Soils,Clay, Sand, Gravel, Rocky Mechanical Connection Under Dome
Sandy Loam areas
Tank Cap. 5 to 5000 ohm-cm 5000 to 10000 ohrn-cm ]
(gal.) Size t1ty. Alloy Size Qty. Alloy
120 9# 1 H-1 9# 1 H-1
150 9# 1 H-1 9# 1 H-1 �+
250 9# 1 H-1 W 2 H-1 -
325 5# 1 H-1 9# 2 H-1
500 17# 1 H-1 9# 2 H-1
1000 17# 2 H-1 9# 4 H-1
1500 17# 2 H-1 9 4 H-1 Cathodic Protection Testing Procedure
2000 17# 3 H-1 s H-1 Equipment Needed: digital Voltmeter,Red Test Lead Min. 12' Long
`Based on 90%effective external coafing,2 malff2 current density,and 30- & Black Lead Min. 2' Long, Reference Electrode (GopperlGopper
yearAnode life. Sulphate Half-Cell)
Anode Installation STEP 1:Using a digital voltmeter insert the red test lead into the Volt
1.Determine size and quantity of anodes from application chart. jack of the metal,and select the 2 or 20 volt DG scale. Clip red test
2.When a single anode is installed, it should be located near the lead connector to an uncoated metallic area of the tank, preferably
tank center orr either side of tank. to the fill pipe m ltivalve. A good solid connection is very important.
3.When multiple anodes are installed, space them evenly around (DO NOT connect to shroud).
the tank. See examples below. STEP 2:Inserttha blacktest lead into the Common jack on the meter,
and connect the opposite end of the lead to a charged reference
7 anode 2 anodes 4 anodes electrode 4%z cell .
STEP 3: Remove protective cap from the porous plug at bottom end
of electrode. Place porous plug and into native soil(remove grass if
_� necessary)atfour locations around the tank done on each side of the
tank, and one at each and of the tank). If difficulty is encountered
obtaining readings,moisten soil with water or dig%cell deeper into
4.Anodes are shipped in either cardboard boxes or multi-wall the sail.
paper sacks, Remove outer container and bury the cloth bagged STEP 4:Record all four meter readings on an appropriate form. The
anode. If anode is supplied in plastic bag, remove plastic bag feast of all four readings should be a minimum of-0.850v or more
before installing. negative. (Note: If any of the tour readings are below(less negative)
5.Install anodes approximately two to three feet from the tank and -0.850v then the fank is not fully protected).
at feast as deep as the center line of the tank. Anodes work hest
in locations with permanent moisture, so generally the deeper C arging Reference Electrode
the better.
6.After placing the anode,stretch out the anode connection wire STEP 1: Unscrev and remove porous plug end of new .reference
and extend over to a connection point on the tan kfill pipe. electrode. Add eionized or distilled water to the copper sulfate
7.Dover the anode with approximately six inches of backf ill and crystals, filling electrode completely. The solution will turn blue in
pour 5 gallons of water on the anode to saturate the prepared color and there s ould always be excess crystals at the bottom of
backfiIJ. Water is necessary to activate the anode. the tube. D❑NO USE TAP WATER.
8.Connect the anode wire to the tank with a low electrical STEP2:Replace porous plug end of electrode and place in an upright
resistance connection. Examples are threaded stud on the position so that tie porous plug end is facing in the down position
tank tit€ pipe or any accessible metallic connection point to the and let stand for 1 hour before use. This will allow the porous plug
tank. All connections should be coated with a moisture-proof to become compf tely saturated before use.
material. Caution:Do not a low electrode to contact oil,road salts, or other
9.Ideally, the tank connection is made in the area of the tank fill substances that way contaminate the solution by absorption
pipe within the covered dome. With access to the anode wire, through porous p ug. Do not allow electrode to freeze.
subsequent testing of the tank can include measurement of
anode output and verification of performance, Distributed By:
10.Verify performance of the anode using an appropriate test
procedure.
Tulsa 1 : : : 11
Houston: 1-281-445-8700
mesaproducts . com
11M11.50M
ES-D-•GAG Generator Generac
For Use with Generac Stationary Outdoor rbGenerators
Job Name Contractor
Job Location Approval
Engineer Contractor's P.O. No.
Approval Representati e
SKU
Dormant SupraSafell
Flexible Gas Appliance
Connectors i
The flexibte connection between the gas supply and the gas inlet
of a Generac®Stationary Outdoor Backup/Standby Generator.
Features For use with Generac
stationary outdoor backup/
•Operating Temperature -40°F to 150-F(-40.0 to 65.6`C) standby generators.
•Operating Pressure MAX 0.5psi(3.45 kPa)
•Hydrostatic Burst Pressure MIN 250psi(1725 kPa)
■Flexible Tube Material Annealed 304 Stainless Steel
•Flare Nut Material Carbon Steel with Zinc Trivalent
Chromate Plating Series 30,40 and 60
•Flare Adapter Material Carbon Steel with Zinc Trivalent
Chromate Plating
Applicableodes
GSA Group Certificate of Compliance to ANSI Z223.11N A 54 National Fuel Gas Code Section 9.6
Product Standards international Fue Gas Code 0FGC)Section 411.I
ANSI Z21.751CSA 6.27—Connectors for Outdoor Gas Appliances 6149.1—Natura Gas and Propane Installation Code
and Manufactured Homes (CSAGroup)Section 6.21
Scope states"...intended for exterior use above ground for making Uniform Mechan Code(UMC)Section 1313.0
non-rigid connection s...between the gas supply and the gas inlet Uniform Plumbing Cade(UPC)Section 1212.0
of an appliance for outdoor installation that is not frequently moved
after Installation."in addition section 1.5.4 states the connector is Additional Approvals
designed for occasional movement after installation.Repeated bend- Pp
ing,flexing.or extreme vibration must be avoided.Normal opera- Commonwealth of Massachusetts Board of State Examiners
tion of a clothes dryer, rooftop HVAC unit or SIMILAR OUTDOOR of Plumbers and 3as Fitters
APPLIANCE DOES NOT constitute extreme vibration or movement.
ANSI Z21.241CSA 6.10—Connectors for Gas Appllances Additional Testing
(Excluding 60/61 Series) UL 2200-2015:Stationary Engine Generator Assemblies
IP` Section 66B Vibration Test.
c us
Product Configurations
DDRRIONIT PART WhIBER SERIES NOIRIPAL ,
OR
OL4835A CAN30-3131-146L 30 '/q % '/2 14
QL4&36A CAN404141-14GL 40 '/ 1 '/ 14
OL4836C CAN50-6161-15G1 60
"CM"prefix indimtes productsupplied WM bath EngG9 aad French instrudons for Canada
�1l;7'llllT,fi
All installations must completely comply with all Dormont manufacturing company warnings
and instructions,national,state and local codes and all applicable ansi standards.
. . .
--- . O- - - prod- - --fi- -- n OS.customary un is and metr c are approximate and are praus. .for reference copy.For precise rhea re- - - - -D6-rmont*- - -
ments,picric contact QonnontTechnical Service,Qormont reserves the dghl to change or modify product design,construction,specVLO ins,
or materials wiihoutt prior notice and without incurring any oblgadon to make such changes and modns on Qormont products prewir aly
or subsequently sold_Refer to the mane8 manual farvinnanty ir>analim A MMM Brand
Minimum Flow Capacity at Specified Pressure Drop
(Straight Length BTU/hr.NATURAL GAS,0.64 SG, 1 DOD BTUku.ft.)
CONFIGURATION PRESSURE,.U.JINCHES WATER COLUMN]
Wen rac Pail Number Dormant Fart Number 11'i ES No1711,7 D N0..n2l Length
in rn 050r7 a75ri7 1.00in 1.25in ?.50in L75if 2wm
OL4835A CAN30-3131-146L 30 / 14 174,500 213,50 246,500 275,500 1302,000 326.000 349,000
OL4836A CAN40 4141-14GL 40 %, 14 338,500 414,500 478,500 565,000 1 586,000 633,ODQ 677,000
OL4836C CAN60-6161-15CzL 60 1'/ 15 1,171,5001 1,434,500 1,656,500 1,852.0001 2,029,000 2,191,000 2,343,000
{Straight Length BTU/hr.LP GAS,1.55 SG,2500 BTU/cu.it.j
,.,• COLUMN]
fienerac Part Number Dormont Part Wrn bar SERlE5 Nominai 10 Nominal Length
5i2 in in in1.00 ir n 00 in
OL4635A CAN37 3131-14GL 30 z 14 172779,20073417600394,400 080Q 8,400 OL4836A CAN40-4141-14GL 40 % 14 541,E00 663,200 765,600 856,000 937,600 1,012,800 11,083,200
OL4836C CAN60-6161-15GL 60 1 Y 15 1,874,400 2,295,200 2,650,400 2,963,200 3,246,400 3,605.600 3.748.900
Dormont part number CAN30-3131-146L can supply a minimum of 349,000 BTU/hr.
of natural gas 0 2.00 in.water column pressure drop to the generator.
-D6fM0nt`- - - - - - - - - - -- - - - - -- - - - -- -- -- - -- -
A, WAM Brand USA:Tel; 800)367-%M o FaxF(724)733-4808 e l crmorrt.com
Canada:I al:P05)332-Q90•Fax(905)332-7068 a Dormam.caa
Lain America:Tel:(52)81 1001-8600 o Fax 152)61-80DD-7091 -Dormont.00m
ES-D-GAG_Generator_Generac 1651 Q 2016 Dormant
r ■ r f
Ideal for use as a first stage regulator on any domestic size ASMF or
DOT container in propane gas installations requiring rap to 1,500 000
BTU's per hour. The regulator fs factory set to reduce container
pressure to an intermedcate pressure of approximately I 0 PSIG.
eNIMI
LV8403TR aVEr Duff t
LV3403TRV9 'r��FNPT %"F.NPT 7/aa" 10 PSIG 1,500.000
9:pp
"Maximum flow based on Net pressure 20 PSIG higher than the reaalatorsettrng and delivery pressure 20%Iowerthan
the regulator setting and delivery pressure 201A lower than the setting.
LVM03TE
qz7:3l;TTTFTMnF
r + 1
Provides accurate first stage regulation in two-stage bulk tank 6e5
systems.Reduce tank pressure to an intermediate pressure of 5 to 10 F,
PSIG.Also used to supply high pressure burners for applications like L
industrial furnaces or boilers.Also incorporated in multiple cylinder >
installations.
OutletInlet
connection Connectioll Size PM5-5� Range*ftr'v SW .
i L1r44033Ft4 �s F 5 'l_g
s I.V4403TR4 NPT ,
LV4403SR9 NPT 5 1.5
LV4403TR9 /' q0 t 5_,10 Yes 2,500,000
LV4403SR96 F. POL 5 1-5
LV4403TR96 F NPT 10 5-10
*When used for fnal stage pressure control,must either incorporate integral relief valve or sepambe rellei'velve should be ecifiied in accordance
with NFPA Pamphlet 58.
Maximum flow based an inlet pressure 20 PSIG hlgher than the regulator smiting and delivery pressure 20%lower than thE set5ng- MM03 Series
r ■ ■ ■ r r
Designed to reduce first stage pressure of 5 to 20 PSIG down to o�+
burner pressure, normalcy 11"w.c. Ideal for medium commercial .,
installations, multiple cylinder installations and normal domestic
loads.
.. _ _.ELL- _�--
Factory Houmel
■
—i
LV440384 �a
LV4403946 %"F.-NPT
#2B "W.C.. .at 9't t 3"LV4403S46R` 90 PS[G Over Inlet 9353000
LV4$El3H65
F. NPT Drill Inlet W-C.
LV4403S69R' s/a"F.N PT
16���03t�s�eee
=aackmauat design Maximum ftow based on 10 PSIG inlet and 9"w.c.delivery pressure.
_
100 Rego Or.Elop.Nr-27244 USA www.;egopioducts.com+1(336)449-7707 t ��
TECHNICAL DATA
112'c75 .625 7.0 0.090
314'IPS 1.050 11.0
Q.095
V.CT5 1.125 11.5
0.099
1"IPS 1.315 11,10
1 1-114"IPS 1.660 T 0.0 0,166
FF-24 End i-112'I IPS 1.900 13.0
0.173
-- ----- --32- 2"IPS 2.375 11.0 0.216
Normal Pipe Size crud SIR must be used to match fi dings and IPS PE pipe.
Nominal Pipe Size and Min.Wall must be used to match Mfings and TS PE pipe.
All pipe shall be ASTM Q2513.
Visit www.performancepipe.com for more information,
_ 1 1:1 1 •1 r�uor�
WfffYpLSEAL
ETRNIER
•1y�
I
CCHAMFER TH-E
Be OF P1I
e F +
F
~�'E.0'IFHSXvoT
Parlent 4s 13W260,5,692,785&5,853,272
Gastite Division o 1116 Vaughn Parkway Portland,TN 37148
ASSEMBLY INSTRUCTIONS: I.D.
E
O _
■
P�
Verify the polyethylene Clark the stab depth by
- pw� (RE.) pipe being inserting the pipe info
assembled is the the chamfer too!and
correct size. marking the pipe of the
entrance as shown,
r a Cut pipe ends square. If using chamfer fool
Wit h ID gauge, check
for proper chamfer by
inserting pipe over
gauge.
- - STEP ZTi;P
Clean Piping thorou hl g Y�. Stub pipe completely fa assure there is no w j ....__. .. Info fitting entrance.
dirt grease or oil in
assembly area.
STEP 4
Chamfer end of pipe . Stab pipe completely
using Continentals > '` `2. into fitling so that the
chamfering tool with l.13, mark on the pipe is
gauge, within 7/8"from the
PT777 fitting entrance.
11E,P
7MF
Repleect steps T though 4 for all Can-Stab joints.
101
[Cr
To assure prop r assernbly and tocomply with 49
E r: CFR 3 92 5ubp rt J-Test requirements, the joint shall
� be leak tested.
- - -- - - - - - - . . ..
- _- -- - - - - -
P�fenr s 5.3fi6,260,5,fi42,385 a 5,853,272 - - -
Ph: 1,800,662.0208 0 Fox:615.325.9407 � Web-www.gasti,e,corn
NATURAL GAS SIZING TABLES FOR PE PIPE
Maximum Capacity of PE Pipe in Cubib F7Dropof
with a Gras Pressure of 6.0 in.WC and a Pressuren.WC
(#used on a 0.60 specific gravity ga
1
110 74 59 50 44 39 33 29 26 4 22 21 20 17 16
635 426 338 286 252 227 192 169 152 1 9 129 120 113 100 90
823 553 438 371 326 294 249 219 197 1 0 167 156 147 129 116
1173 787 624 529 465 419 355 312 291 2 7 238 223 209 184 166
2108 1415 1121 950 835 752 638 561 505 2 428 400 376 331 298
2765 1900 1526 1306 1158 1349 898 796 721 6 3 617 579 547 485 439
5954 3997 3166 2683 2360 2125 1801 1584 1426 1 05 1209 1130 1063 935 842
1 iTubing Length
it 1 le �/1 1 .1 IF 2/1 4 11/ le D 1! 1. 11
13 12 10 9 8 7 6 6 6 5 5 5 4 4
76 67 60 51 45 40 37 34 32 3 29 27 26 25 24
99 87 78 66 58 52 48 44 42 3 37 35 34 32 31
141 124 111 94 83 75 68 63 59 5 53 50 48 46 44
253 222 200 170 149 134 123 114 106 1 0 95 90 86 83 79
376 333 302 258 229 207 191 178 167 1 7 T49 143 137 131 126
714 628 565 479 421 380 347 322 301 283 268 255 243 233 224
10WBTUh=1CFH
Maximum Capacity of PE Pipe in Cubic Fe t per Hour
with to Gas Pressure of 6.0 to 7.0 in.WC (t 14 psig) ans� a P essure Drop of 1,0 in.WC
(based on a 0.60 specific gravity gas)
y 1 � 1 1 .F a el •! 11 1
165 111 88 74 65 59 50 44 39 36 33 31 29 26 23
947 636 503 427 375 338 286 252 227 20 192 180 169 149 134
1228 824 653 553 487 438 371 327 294 26 249 233 219 193 174
1749 1174 930 788 693 624 529 465 419 38 355 332 312 275 247
3143 2110 1671 1416 1246 1122 951 836 753 689 638 596 567 494 445
4023 2765 2221 1900 1684 T526 1306 1158 1049 965 898 842 796 705 639
8878 5960 4720 4007 3519 3169 2686 2362 2127 194 1803 1685 1586 1395 1256
1Tubing
1. F a r!1 el 1
20 17 16 13 12 10 10 9 8 8 7 7 7 6 6
114 100 90 76 67 60 55 51 48 45 43 41 39 37 36
747 129 117 99 87 78 72 66 62 58 56 53 50 48 46
210 184 166 141 124 112 102 95 88 83 79 75 71 69 66
377 331 298 253 223 200 183 170 159 149 141 135 128 123 T18
547 485 439 376 333 302 278 258 242 229 217 207 199 191 184
1065 936 843 715 629 566 518 480 448 422 399 380 363 348 334
-- - - - - --- - - - - T000sTUh=1GFH
4 Gastile Division a 1116,Vaug}m Parkway e Portland,IN 37148
1
NATURAL GAS Willi';
Nlaxllmum Capacity of PE Pipe in Crab c Feet per Hour I �
with a Gas Pressure of 8.0 in.WC and a Pres ure Drop of 3.0 in.WC I
(based on a 0.60 specific gravi gas) ' 1
308 210 166 141 124 ill 94 83 75 68 63 59 56 49 44
1773 1205 955 809 712 641 543 478 430 394 365 341 321 282 254
2298 1561 1236 1048 921 830 703 619 557 510 472 441 415 365 329
3275 2198 1741 1476 1298 1169 991 871 785 718 665 621 585 514 463
5885 4002 3170 2686 2363 2128 1803 1586 1428 1307 1211 1131 1065 937 843
7290 50TO 4023 3443 3052 2765 2367 2097 1900 1748 162-7 1526 1442 1278 1158
16623 10940 8665 7344 64W 5816 4930 4336 3904 3673 3309 3093 2911 2560 2305
Tubing Length (0)
250 it ee •rr e� r rrr e re er
37 33 30 25 22 20 18 17 16 15 14 13 13 12 12
215 189 171 145 127 113 11]3 96 90 84 80 76 72 69 67
279 245 221 187 165 147 134 124 116 109 103 98 94 90 87
393 345 371 264 232 209 191 177 165 156 147 140 134 128 123
715 629 566 480 422 375 343 318 297 280 265 252 241 230 222
991 878 796 681 604 547 503 468 439 415 394 376 360 346 333
1954 17T9 1548 1312 1154 1060 970 898 839 790 748 711 679 651 626
TO003TUh=1 CFN
Maximum Capacity of PE Pipe in Cubic eet per i-iour
with a Gas Pressure of 12.0 to 14 in.WC(1/2 psig or less) nab(a Pressure Drop of 6.0 in.WC
(basest on a 0.60 speclfiC gravity g s)
Tubinq Leng1h
462 310 246 208 183 165 140 123 111 101 94 88 83 73 65
2657 1784 1413 7197 1053 946 804 707 637 583 540 504 475 417 376
3445 2313 1832 1553 1366 1230 1042 917 825 765 700 654 615 541 487
4909 3295 2610 2212 1946 1752 1485 1306 1176 1076 997 932 877 771 694
8821 5922 4690 3975 3496 3148 2668 2347 2114 934 1791 1674 1576 1386 1248
10606 729{) 5854 5010 4440 4023 3443 3052 2765 544 2367 222T 2097 1859 1684
24918 16727 13249 11229 9877 8894 7638 6630 5970 64 5R60 4729 4451 3915 3525
w
rr a !1 ,ee IE .l ea :rr •r f �e of YI r
55 49 44 37 33 29 27 25 23 2 21 20 19 18 17
319 280 252 214 185 169 155 144 134 26 120 114 109 104 100
413 363 327 277 244 220 201 186 174 64 155 147 141 135 130
589 518 466 395 348 313 286 265 248 33 221 210 201 192 185
1058 930 838 710 625 562 515 477 445 19 397 377 361 345 332
1442 1278 1158 991 878 796 732 681 639 573 547 524 503 485
2988 2628 2366 2006 7764 7589 1454 1346 1258 1 84 7121 7066 1018 976 938
10OOBTUh=1 CFH
Ph: 7,800,662.0208 a Fax:615.325,9407 Web:www.gasiife.com 5
I1
1
1
NATURAL GAS SIZING TABLES FOR PE PIPE - ELEVATED PRESSURE
Maximum Capacity of PE Pipe in Cubic Peet per Hour with ra Gas Pressure of 2.O psi and a Pressure Drop of 1.0 psi
(b a sad an a 0.56 speciHe grovi3y gas)
NMI1 P •1 a .1 :1 1 t8JIM
1
1167 783 621 526 463 417 353 311 280 56 237 221 208 183 165
6710 4504 3568 3024 2660 2395 2030 1786 1608 1471 1363 1273 1198 1054 949
8687 5832 4619 3915 3443 3101 2628 2311 2081 1 05 1764 1649 1552 1355 1229
12396 8321 6591 5586 4913 4424 3750 3298 2970 2 18 2517 2352 2214 1947 1754
22276 14953 11844 10038 8829 7950 6738 5927 5337 4 84 4623 4227 3979 MOO 3151
25532 17548 14092 12061 10689 9685 8289 7347 6657 6 24 5697 5345 5049 4475 4055
62923 42239 33455 28355 24940 22458 19034 16742 15076 1 97 12777 11941 11239 9885 8902
1Tubiqg Length (ft�
6
1 ° t1 •It / ,/° tl :t/ 'li 1 p° I ido 12061 11 /
140 123 111 94 83 74 68 63 59 5 53 50 48 46 44
805 708 637 540 475 428 391 363 339 3 9 302 287 274 263 253
1042 916 825 699 615 554 507 469 439 4 3 391 372 355 340 327
1486 1307 1177 998 878 790 723 670 626 5 9 558 53D 507 485 467
2671 2349 2TT5 1793 7577 1420 1300 1204 1125 1 9 1002 953 910 872 838
3470 3076 2787 2385 2114 1915 1762 1639 1538 14 3 1380 1316 7261 1211 1167
7544 6636 5975 5064 4455 4011 3671 3400 3177 2 2831 2693 2572 2464 2368
10008TUW CFH
M aAmLim Capacity of PE Pipe in Cubic Feet per Hour with a Gas Pressure o 5.0 psi and a Pressure Drop of 35 psi
(fried on a 0.60 specific gravity gas)
9 ! 'T—f�116bjnq Length Of)
t e 1 .e •e It t
2544 1708 1353 1147 1008 9aS 770 677 610 55 517 483 454 400 369
74628 98T9 7777 6592 5798 5227 4425 3892 3505 32 7 2970 2776 2613 2298 2069
18966 12731 10084 8546 7577 6769 5737 5046 4544 41 3851 3599 3387 2980 2683
27024 18141 14368 12178 10711 9645 8175 7190 6475 59 5488 5128 4827 4246 3823
48561 32598 25819 2T883 19248 17332 14689 12927 11635 106 8 9861 9215 8673 7629 6870
53153 36532 29336 25108 22253 20163 17257 15294 13856 127 9 11860 17128 10512 9316 8441
137172 92082 72933 61813 54370 48959 41494 36498 32865 300 8 27855 26031 24500 2T550 19405
1 / ■
r722.
1tl It tt .°/ °° :tt ^tt °t 11 1268 242 205 180 162 148 137 128 121 114109104 100 96
1543 1389 1177 1036 932 853 790 739 695658 626 598 573 551
2000 18DI 1526 1343 1209 1106 1025 958 901 $53812 775 743 714
2850 2566 2175 1913 1723 1577 1460 1364 128 1216 1156 1104 IU58 1017
5121 4612 3908 U38 3096 2833 2624 2452 23Q 2785 2078 1985 1902 1828
6403 5802 4965 4401 3987 3668 3413 3202 302 2873 2741 2624 2521 2429
14466 13027 11041 9711 8745 8003 7411 6926 65]9 6171 5870 5606 5372 5163
10008TUh=1 CFH
Maximum Capacity of PE Pipe in Cubic Peet per Hour with a'Gars Pressure of I .0 psi and a Pressure Drop of 5.0 psi
(used on a 0.60 specific grovity gas)
■ W. K�
° / 1 3529 2369 1877 7590 7399 1260 1068 939 846 774 717 670 630 554 499
20291 13621 10789 9144 8043 7242 6738 5399 4862 4449 412D 3851 3624 3188 2871
26309 17661 13988 11856 10428 9390 7958 7000 6303 5769 5342 4993 4699 4133 3722
37487 25164 19931 16893 14858 13380 11340 9974 8982 3220 7612 7114 6696 5889 5303
67362 45220 35816 30355 26700 24043 20377 17923 16139 14770 13679 12783 12032 10583 9530
72320 49705 39915 34162 30277 27433 23479 20809 18855 17346 76137 15141 14302 12676 11485
19C283 127734 301171 85746 75421 67915 57560 50629 45590 41723 36639 36109 33987 29894 26919
11 t 1! li e ° tt :°° t/ 111 ► tt le 1 a/
423 372 335 284 250 225 206 791 178 168 1 159 151 144 138 133
2433 2140 1927 1633 1437 1294 1184 1096 1025 964 973 am 829 795 764
3164 2775 2498 2118 1863 1677 1535 1421 1325 1250 1184 1126 1075 1030 990
4495 3953 3560 3017 2654 2390 2787 2025 7893 1782 1686 1604 1532 1468 1411
8Q77 7104 6397 5422 4769 4294 3930 3640 3401 3201 3031_ __2883. .2753 ...2638,_v25.36___ _
f -9830 ' 8712 7694 07 6 '8988 5425 4991 4643 4357 4115 390-8 3729 3571 3480 3305
22815 20067 18070 15315 13471 12130 11101 10281 9608 9043 8561 8143 7777 7452 7162
i 000STUh=1 CFH
Gastito Division e 1116 ughn Parkway � Portland,TN 37148
Gostk Division
1116 Vaughn arkway
Portland, N 37148
Toff free: 1.800, 62.0203
fax:615.325.9407
Web: www.gas ite.corn
i~-r�'��iL• gc�s;ite@gas ite,ccarn
Rev.6/2016
LP
S SUING
[ TABLES ■ i @ 1
1
11.1
Maximum Capcicity of PE Pipe in Thousands of BTU per H ur of liquefied Pefroieurn Gas
With a G:'s Pressure of 71.0 ir-s,l^JG and a Pressur Rrap of(1.5 1n.WC
(based on ra 1,52 spec#fic grav�ify gas
/ r
• ■
187 125 99 84 74 67 56 50 45 41 38 35 33 29 26
1073 720 571 484 425 383 325 286 257 235 218 204 192 169 752
I'cis 1391 934 740 627 551 > 497 421 370 333 305 283 264 249 219 197
1983 1331 1054 893 786 708 600 528 475 435 403 376 354 311 280
3563 2391 1894 1605 1412 1272 1078 948 864 781 723 676 636 560 504
4724 3247 2608 2232 1978 1792 1534 1359 1232 1133 1054 989 934 828 750
LP
.../. -
10063 6755 5351 4535 3989 3592 3044 2678 241T 2207 2044 1910 7797 7587 1424
-
F 1 !1 tT tt .!1 !! ilt • / !t [1 It 1[ ; f
22 20 18 15 13 12 11 70 9 9 8 8 8 7 7
124 113 102 86 76 68 63 58 54 51 48 46 44 42 40
167 147 132 112 99 89 87 75 70 66 63 60 57 54 52
238 209 786 160 140 126 116 107 100 94 89 85 81 78 75
427 376 338 287 252 227 208 192 T80 169 160 152 146 140 134
642 569 516 441 391 354 326 303 285 269 255 244 233 224 216
1207 1061 966 810 712 642 587 544 508 478 453 431 411 394 379
Maximum Capacity of PE Pipe In Thousands of BTU per i-tou of Liquefied Petroleums Gas 51681U1�=1CFH
with a Gras Pressure of 2,0 psi and a Pressure rap of 1.0 psi
(rased❑n a 1.52 speciBC gravity gas)
1 /
:-
7966 1319 T045 886 779 702 695 523 471 43] 399 373 351 309 278-
11300 7586 6008 5092 4479 4033 3478 3007 2707 247$ 2295 2744 20T8 1775 1599
14652 9835 7790 6602 5807 5229 4432 3898 3510 32T3 2975 2780 2677 2302 2073
20877 14014 1T100 9408 8275 7451 6315 5555 5002 578 4239 3962 3729 3280 2953
37514 25163 19946 16905 14869 13389 11348 9982 8988 226 7618 7119 6700 5894 5307
43429 29848 23969 20515 18182 76474 14100 12496 11322 0417 9691 9092 85891 7612 6897
105963 7T131 56339 47750 42000 37820 32054 28194 25388 3234 21517 20108 18926 76647 14990
Mk �I tl •It i} •tI 11 :FI 'll 1!1 it t! 1
236 207 787 la139 125 175 106 99 93 88 84 80 77x 74+
1355 1192 1073 910 800 720 659 611 571 37 508 484 462 443 425
1757 1545 T391 7179 1037 934 855 792 740 96 659 627 599 574 551
2503 2202 1983 1680 1478 1331 1218 1128 1054 2 939 893 853 818 786 4498 3956 3563 3019 2656 2391 2189 2027 1894 1783 1688 1606 1533 1469 1412
5903 5232 4740 40�57 3596 3258 2997 2788 2616 71 2347 2239 2144 2060 1985
12705 11175 10063 8529 7502 6755 6182 5725 5350 5 D36 4767 4535 4331 4150 3988
Maximum Capacity of PC pipe in Thousands of BTU per Hour of Liquefred Pefroleurn Ga2516BT!lh-1 CFFI
with a Gas Pressure of 10.0 psi and a Pressure Pr p of 1,[i psi
-- (based on a 1.52 spec;i5c gravity gas)
1 P
■ •
t 1
2476 7662 7316 1116 981 884 749 b59 593 t 7 tt
14 5234 9555 7568 6414 5642 5080 4306 3787 3410 3121 2890 2707 2542 2236 2014
18455 72388 9812 8316 7315 6587 5583 4970 4422 4 7 3747 3502 3296 2899 26296 17652 13981 11849 10423 9385 7954 6997 6300 57 6 5340 4990 4697 2611
4131 2611
3720
47252 31720 25123 21293 1872-9 16865 14294 12572 17321 10 6I 9595 8967 8440 7423 6685
53960 37087 29782 25489 22591 20469 17519 15527 14W 12 43 T2041 11297 10671 9458 8569
T33476 89601 70967 60T48 52905 47640 40376 35514 31980 29 67 27104 25329 23840 20970 18882
r -
• ■ r
It 1 t! Tt !t .!t 11 !1 •1! 1 t 1
297 261 235 799 175 158 144 134 T25 11 171 106 101 97 93
1707 1501 1352 1146 }008 907 830 769 719 67 640 609 582 557 536 2213 1946 1753 1485 7306 1176 1077 997 932 87 830 790 754 723 695
3153 2773 2497 2116 1862 7676 1534 1421 1328 12 0 1i83 1]25 1075 T030 990
5665 4983 4487 3805 3345 3p72_ 2757 2553- .2386-..-22 _ . 2726 2022 •1931---1851-- •1779
7334 65�t] 5890 5041 4468 4048 3724 3465 3251 3071 2976 2782 2664 2564 2466
I6004 14077 12675 10743 9449 8509 7787 7212 6739 634 6005 5712 5455 5227 5024
25168TUh-1CFH
Ph: 1.800.662.0208 - Fax:615.325.9407 e Web:www.gastite.com
GAS PIPING INSTALLATIONIS
Gas Undiluted Propane
TABLE 402.4(25) inlet Pressure 10.0 psi
SCHEDULE 40 METALLIC PIPE Pressure Drop1.0 psi
Specific Gravity,1.50
11VT hiI]E0 ti8JR Pipesizirzg between first stage(high-pressure regulator}and second stage(low-pressure regulator).
PIPE SIZZE(inch)
Naminal Iz 314 1 1'J4 1% 2yZ 3 4
Actual10 0.622 0.824 1.049 i.380 1.610 2.037 2.469 3A&8 4.026
Length(ft) Capacity in Thousands of Btu per Hour
10 3,320 6,950 13,100 26,900 40,300 77,600 124,000 219,000 446,000
7A 2,280 4,780 9,000 19,500 27,700 53, i] 85,000 150,000 306,00[]
30 I,830 3,840 7,220 14,800 22,200 42,8 68,200 121,0♦}0 246,000
40 I,570 3,280 6,180 12,700 19,000 36,6)0 5S,400 103,000 21I,000
50 1,390 2,910 5,480 11,300 16,900 32,5)0 51,700 91,500 187,000
60 1,260 2,640 4,970 va'200 15,300 29, 0 46,900 82,900 169,000
70 1,160 2,430 4,570 9,38p 14,104 27,110 43,100 76,300 156,000
80 1,080 2,260 4,25U 8,730 13,100 25 0 40,100 70,900 145,000
9Q 1,010 2120 3,990 8,190 12,300 23;540 1 37,700 66,600 14000
100 956 2,000 3,770 7,730 11,600 22,3 0 35,600 62,900 128,000
125 848 I,770 3,340 6,950 10,300 19,8(0 31,500 55,700 114,000
150 768 1,610 3,020 6,210 9,300 17.9(0 28,600 50,500 103,000
175 706 1,430 2,780 5,710 8,560 I6 26„300 46,500 94,700
200 657 1,370 2,590 5,320 7,960 15,3 24,400 43,200 SS,100
250 582 I,220 2,290 4,710 7,060 13,60 21,700 38,300 78,100
300 528 1,100 2,080 4.270 6,400 12,30 19,600 34,700 70,800
350 486 I,Om 1,910 3,930 5,g80 11p3m 18,I00 31,900 65,100
400 452 945 1,780 3,650 5,470 10,50 16,800 29,700 60,600
450 424 886 L670 3,430 5,140 9P890 15,800 27,900 56,800 ��1
500 400 837 1,580 3,240 4,950 9,340 14,900 26,300 53,700
550 380 795 1,500 3,070 4,610 81870 14,100 25,000 51,000
600 30 759 1,430 2.930 4,400 9,460 13,50Q 23,900 48,60D
650 347 726 1,370 2,810 4,210 81110 12,900 22,900 45;600
700 334 699 L310 2,700 4,040 7,790 12.400 21,900 44,800
750 321 672 1,270 2,600 3,900 7,500 12,000 21,100 43,1Q0
900 310 649 1,220 2,510 3,760 7,240 11,50Q"20,40041p,6010,600850 300 628 1,180 2,430 3,640 7,010 11200 ,300900 291 609 1,150 2,360 3,530 6,800 I0,800100950 283 592 1,I10 2,290 3,430 6,600 10,5009001,000 275 575 1,080 2,230 3,330 6,420 10,2001,100 261 546 I,030 2,110 3,170 6,100 9,720000
1,200 249 521 982 2,020 3,020 5,820 9,270 16,400 33,400
1,300 239 499 940 1,930 2,890 5570 8,880 15,700 32,000
L400 229 480 903 1,850 2,780 5,350 8,530 15,100 30,80p
1,500 221 462 370 1,790 2,680 5,160 8,220 14,500 29,600
1,600 213 446 840 1,730 2,590 4,980 7.940 14,000H26,100
,600
1,700 206 432 813 1,670 2,500 4,320 7,690 13,600 ,700
1,800 200 419 789 1,620 2,430 4,670 7,450 13,200 900
I,900 i94 407 766 1,570 260 4,540 7,230 12,800
2,000 189 395 745 1,530 2,290 4,4I0 7,030 12,400 ,400
For S'1: I inch=25A mm,I foot=304.8 ram,I pound per square inch=6.895 kPa,1-inch water column=0.24-88 kPa,
I British thermal unit per hour=0.2931 W,1 cubic foot per hour=0,0293 ni'/h,I degree=0.0 1741 rad.
114nte:A U tableeentries have been rounded La three sigoifj cant•digits.. . . _. _. . - . . . . _... _ . - _ _ _ • __ . . . .
J
50 FLO131DA BUILDING CODE FUEL GAS,6th EDITION(2017)