HomeMy WebLinkAboutGas Piping Schematic�rlOJ�sJ'�S7VC1
FILL COPYio
2: u F-- (P
c h,
disAv
h �c►�►� �'� ,,�b,� .
Soj'70s�i
15
CL� o�Ji�31 a
C��.oV�
d7Ll
v aoo)
aqotg�D
oQS
mn
aevl!
L
L�
` T
Iqq/;?
00010h
plo
(Mh'W17 +SaI'A�'saip}�V,/I0woW
tP�S
LI o\C'
01.9
C209%,
ID
-V
110.00"
M 8965233- E
5 23I5/4 23.13
TRAA-H LME 23,38 46.66'
r 6 4-DJAAL-N 5233"
-TP F BA+* 23,
23.14
9-SWALE 2219
22.5
0 A 2310
518. 10
)ID IR *3,1 N 89052 3 w = FND51WIRC
23,z GE PALM� LB # 4632
CABAGEPALM tl 23.3 16.0.
5'm C.'t I GARAGE PAUV *22.8
CABAGEPALM
e:-. 22,7
,9 x 22 4 < 23.0
x 22.7 23.0 x
sA
LOT 18 RECEIVED
0
OCCUPIE
D Q JAN 2 3 2020
Q
_ad
79. 22A
ST. Lucie County, Permitting
7�s �lzo\ro 29.0
22.68 022,65! ,
ID -.,%k24.3' PROPOSED
22.9 1 APROPOSElJ- .4. CONCRETE x
*
J_STORY
3. R - UE
w 9-
CABAGEPA 22.6
23.2
35. PROPO
S \ED
97 PORCH 7
.8 x 22.5 22(l 21.34� 2 - WER LINE
73.8' 0PROPOSES
1 ...,
1 .2-
14 PROP SEO -23,1 90 22.8 x 22.9
15.81 POOL
AREAro
7&0'
ILL: (a
U
0 0, 23,28 PROPOSED
0
53.0'
le 22,9 WELL
EXI TING WELL
24.3 CONCRETE
170.13-
. 629.87'
0.00,
x e22A x 23,8 2.9 9 EXISTVG
HWGER 22,8X X 22.9
FFE = 25.0'
60.00' 30.00'
E)CISTIN
gt�.!CONCREM
r IRC
)ABLE 260.00ff jyl 890576 LIM FND 5/8"IRC
E UNREADABLE
< x -22-,7-
22.6
-q 5 r 11
21.6 DRAIN E PIPE 4
INV f 1. �2`
21.35 V 21.24 22.9
IN IN 21.22
GRASS TAX WAY INV
TAXIWAY TRACT 2,-3.4 23.3
22.9- 22,8
22A - WALE 22.1
a
i
i nN
lit tI
8" dome,1@441
I ��IC'TI �:`,Ni U
9
.Y
N'E'.fNl!
1 r"S P _ ]
.. Xa-•. c`4^r�11�1��[,`,�44p"P. .L G,T wY-pi7.t"y7.a',.y�i
_! WL}_VJIIM,Y- Y FVyj` 1W� iv,•ai W11 PH �e111.Pi5`}tn4!UdG,.
' y
4 a • rZm ; ch a Ax Imes '
kf+plasilc toF;yuhit
_
t{51ftr bum, hle�T�CIC �olye"sPer�Sop g p
Izecll:steeli
wperopro`s�n andedge�Pr eonJ
•
�I !Pa en pen Ing of rr�ilTla>edp�rlme. n ttopcoati
.++Duabseivice;opiiomsfdr{ab`ove;or"underground.applibaiions
r .••Opton #1 Ready to=6`ury red ok'ide durable pTgwdereoatingXWAt black
,'' • poydthyleneiQVOU dome
• dOption#2-.,AboGegro'ond�(zption%Witfisfeer8"AGUG•d'ome
`4•All'valvespbdrfloaflg-auge"s,areic'eritered.under dome ,
.diFabr�catedrto the IatestFtS MBEo'de, Secfion,Vlll 'l)ivi'sion'.1
` '�
•: Regis'te'red•wiih theiNatipnal Board;
•'MtZhquidyde�ue outage.Salveaniifice reduces,rRfu-in gterniss ons
r
•
,-
•-vacuum pre -purged to save time%;m'oney and product
.,
1I N E R S,
""�App6catil`eYfetleaall st` a'te';'or�local egurttons may.c`ontam specific.requ�remenis for
,ProfectiVe;co'gt ngs and catFiodiceprotecho`n The: pLrchaserand'in`stallerare reWonsible
�.„ 'tgr�comp6anc'-eTwith all (e_'deral, s[ateilocar�d,NFPA;iiiddstry�fegu/aiidris, Cathodic
E 4 IJ I,C4I17AMI-0
0 I
w
x
w
�
�
OUTSIDE
>
o DIAMETER
0
0
0
f-
General Specifications
Conforms to the latest edition of the ASME code for
Pressure Vessels, Section VIII, Division 1. Complies with
NFPA 58.
Rated at 250 psig from -20" F. to 125" F. All tanks may be
evacuated to a full (14.7 psi) vacuum.
Vessel Finish: Coated with epoxy red powder. ( Tanks coated
with the epoxy powder must be buried). For Aboveground use,
tanks may be coated with TGIC powder.
Applicable federal, state or local regulations may contain
specific requirements for protective coatings and cathodic
protection. The purchaser and installer are responsible for
compliance with all federal, state or local regulations.
,�--� WITHDRAWAL
VALVE O110E �
FLOAT LP. ras \ ANODE
GAUGE GAUGE { CONNECTION
FILLER
1 O 1 VALVE
� A
SERVICE/
MULTIVALVE
RELIEF
VALVE
FITTINGS LAYOUT UNDER DOME
AGUG VESSEL DIMENSIONAL INFORMATION
All vessels dimensions are approximate
WATER
OUTSIDE
HEAD
OVERALL
OVERALL
LEG
LEG
WEIGHT
QUANTITY
FULL
PER
CAPACITY
DIAMETER
TYPE
I
LENGTH
HEIGHT
WIDTH
SPACING
LOAD
STACK
120 wg.
24"
Blip
5'- 5 13116"
3' - 0"
10 1/8"
3' - 0"
245 lbs.
96
12
454.2 L
609.6 mm
1671.3mm
911.4 mm
257.2 mm
914.4 mm
111.1 kg.
250 wg.
31.5"
Hem!
7' - 2 1/2"
T - 7 1 /2"
12 3/4"
3' - 6"
472 Ibs.
63
9
946.3 L
800.1 mm
2197.1 mm
1104.9 mm
323.9 mm
1066.8 mm
214.1 kg.
320 wg.
31.5"
Hem!
8' -11 3/4"
3' - 7 1/2"
12 3/4"
4' - 0 114"
588 Ibs.
45
9
1211.2 L
800.1 mm
2736.9 mm
1104.9 mm
323.9 mm
1225.6 mm
266.7 kg.
500 wg.
37A2",
Hemi
9' - 10"
4' -1 7/16"
15"
5'- 0"
871 Ibs.
30
6
1892.5 L
950.5 mm
2997.2 mm
1255.7 mm
381.0 mm
1524.0 mm
395.1 kg
1000 wg.
40.96"
Hemi
15'-10 13/16"
4'-4 5/16"
16 1/4"
9'-0"
17291bs.
15
5
3785.0 L
1040.4 mm
4846.6 mm
1344.6 mm
412.8 mm
2743.2 mm
784.3 kg
Rev: Jan. 27, 2016
Why Tanks Corrode
Underground steel tanks corrode due to an electrochemical reaction
between the tank and the surrounding soil. The process of 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 soil corrosion occurs. This location is called
the anode in a corrosion circuit. Where currentflows 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 over time.
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 on underground tanks in either a
general overall rusting or more commonly, a pitting attack. Pit locations
may result from metallurgical conditions of the steel suraface or soil
variations such as rocks, salts, fertilizer, moisture concentration, oxygen
concentration, etc.
Preventing Corrosion
Protecting underground
tanks from corrosion is
easily achieved by the use
of two commonly applied
protection methods:
external coating and
cathodic protection.
These two methods
are complementary
and should be used in
conjunction with the
other. An effective
external . protective
coating insulates the steel from the soil environment, thus preventing
the flow of corrosion current from the anode to the cathode. An effective
external coating can protect over 99% of the tank surface area. However,
no coating is perfect Damage from construction or soil stresses create
tiny defects, which may result in accelerated corrosion at the defect.
Cathodic protection prevents corrosion at those defects by applying
DC current from an external source, forcing the tank to become
cathode. Application of sufficient DC current to the tank will prevent any
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 in underground propane tanks. Impressed current systems
are more commonly used for large structures such as large diameter
pipelines. Electrical isolation of the tank from metallic piping systems
and electrical grounds is critical for the cathodic protection system's
effectiveness.
How Sacrificial Cathodic Protection Works
Sacrificial systems work by creating a galvanic connection 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 of 1 to 1.25V volts results in current
flow to the tank that overcomes the natural corrosion cells that exist on
the tank With this current available to the tank, no corrosion occurs.
Magnesium Anodes
There are a variety of anode sizes and alloys used for cathodic
protection. The two primary alloys are designed as H-1 (or AZ63) and
High Potential. The H-1 alloy is produced from recycled magnesium
and has an open circuit potential of approximately—1.55V. This alloy
is well suited for protection of underground propane tanks. The High
Potential alloy is 99% pure magnesium having an open circuit potential
up to -1.8V. This alloy should be used for soil applications over 10,000
ohm -cm resistivity.
The two most common anode sizes used for underground propane
tanks are 9lb. and 171b. The size designation relates to the metal weight
10' of #12 TW insulated wire is attached to the anodes. Anodes are
then backfilled in a mixture of gypsum, bentonite, and sodium sulfate
to lower the electrical resistance of the anode to soil. The mixture is a
low cost, nonhazardous, electrically conductive backfill. The anode and
backfill is then packaged in a cotton bag and either a cardboard box or
paper bag. Actual shipping weight of these anodes with backfill is 27
lb. and 45 lb.
Application Recommendations
Magnesium anodes can protect underground tanks in most soil
conditions. The H-1 alloy is generallyvery effective. The following chart
provides size and quantity recommendations forvadous size tanks based
on conservative design assumptions. This chart covers soil conditions
up to 10,000 ohm -centimeter resistivity. Resistivities higher than
10,000 ohm -centimeter generally represent very dry soils. Verification
of soil resistivity can be performed through soil analysis. Contact us
for design recommendations in locations where soil resistivities exceed
10,000 ohm -cm, or If there is no effective 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 line
is plastic. All underground steel pipe should be externally coated with
a corrosion resistant material. The service line should be electrically
isolated at the house with an insulating fitting or union. If service pipe
is less than 50' in length, the tank 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 electrically isolated from the tank at the fill pipe
connection. Copper and steel create a galvanic couple that will accelerate
corrosion of the steel tank when directly connected to copper piping.
Generally, copper piping does not require cathodic protection.
Sail Type
: F.ertile S6iIsClay,,
'a`amsw;_`�
Sand, Gravel, Rocky
Areas
Tank Cap.
�S�tu.5000:nhm�cm
,
5000 to 100oo ohm -cm
(gal-)
1' z
0ty` AI(oy
Size
I Oty.
I Alloy
1209#'
S7iiw:
9#
1
H-1
150
` 9 K#
pe
!-It- )l if t
" -.. 1 i�i
9#
1
H-1
250
L7f#, 'a
r. ,j �H;1�
9#
2
H-1
325
?9#,„
dT H1'
u_ ._
9d
2
H-1
500
�,t1�7#�
1'S1'; _y �H�1''�S
9#
2
H-1
1500
(=1Cf� j,
2 i j7, ff l
9#
4
H-1
`Based on 90% effective external coating, 2 ma/h2 current density, and 30-
year Anode life.
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.
1 anode 2 anodes 4 anodes
O O O
C30 c:90
4.Anodes are shipped in either cardboard boxes or multi -wall
papersacks. Remove outer containerand burythe cloth 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. Anodes work best
in locations with permanent moisture, so generally the deeper
the better.
6.After placing the anode, stretch out the anode connection wire
and extend overto a connection point on the tank fill pipe.
7.Cover the anode with approximately six inches of backfill and
pour 5 gallons of water on the anode to saturate the prepared
backfill. Water is necessary to activate the anode.
8. Connect the anode wire to the tank with a low electrical
resistance connection. Examples 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.
10.Verify performance of the anode using an appropriate test
procedure.
Mechanica-i'Connection Under Dome
Cathodic Protection Testing Procedure
Equipment Needed: Digital Voltmeter, Red Test Lead Min.12' Long
& Black Lead Min. 2' Long, Reference Electrode (Copper/Copper
Sulphate Half -Cell)
STEP 1: Using a digital voltmeter insert the 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 NOT connect to shroud).
STEP 2: Insert the black test lead into the Common jack on the meter,
and connect the opposite end of the lead to a charged reference
electrode (ys cell).
STEP 3: Remove protective cap from the porous plug at bottom end
of electrode. Place porous plug end into native soil (remove grass if
necessary) atfour locations around the tank (one 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'h 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. {Note: If any of the four readings are below (less negative)
-0.850v then the tank is not fully protected}.
Charging Reference Electrode
STEP 1: Unscrew and remove porous plug end 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.
STEP 2: Replace porous plug end of electrode and place in an upright
position so that the porous plug end is facing in the down position
and let stand for 1 hour before use. This will allow the porous plug
to become completely saturated before use.
Caution: Do notallow electrode to contact oil, road salts, orother
substances that may contaminate the solution by absorption
through porous plug. Do not allow electrode to freeze.
Distributed By:
knou—mNlami
Ideal for use as a first stage regulator on any domestic size ASME or
DOT container In propane gas Installations requiring up to 1,500,000 LISTED
BTU's per hour. The regulator is factory set to reduce container
pressure to an Intermediate pressure of approximately 10 PSIG.
rm
• Compact design can be connected to a service valve using either
a POL adapter or a RegO product pigtail.
• Large threaded Ye" F.NPT bonnet vent can easily be piped -away
underground installations without the need of glue kits or extra
adapters.
• Non Adjustable
• Large Bow orifice resists freeze ups due to water concentration in
LPG vapor.
• Design provides for good flow regulation at both high and low
container pressures.
• Built in relief valve and travel stop comply with NFPA 58 over
pressure requirements.
• Incorporates W RNPT downstream pressure tap for an easy
Inline check of the regulator's delivery pressure.
• Molded diaphragm provides an o-ring type seal between the
body and bonnet !.
• Body and bonnet are assembled in the USA using the unique,
patented RegUlok seal system.
• Fully painted In brilliant red for complete corrosion protection.
• Mounting bracket available as an accessory: part number 2302-31.
FEWesrq&VAry
Bonnet.........................................................................................Zinc
Spring........................................................................................
Steel
SeatDisc.................................................................
Resilient Rubber
Diaphragm...........................Integrated
Fabric and Synthetic Rubber
LV3403TR
�1Jf
3.56•
F WPRDPPHe
�
+Factory
Delve
--^_
Va ofG as iBT !tn
p
PartWuinb'e`r
Intel Connee6oni.
"OlStlder,Connee�dn,
rOnHEe Srz@j'
+Pressure+
IBom`nye[Ven_IlPosth$n.
•.. -�
Propan'e,
II 111
®®®®
• 11
• Maximum flow based on inlet pressure 20 PSIG higher than the regulator setting and delivery pressure 20%lower than the regulatorselting and delivery pressure 20%lover than the setting.
A14 MAX—W. 100 Re00 Dr. Elan. NC 27244 USA wvraregoproduais.com H (336) 449-7707
Designed to reduce first stage pressure of 5 to 20 PSIG down to
burner pressure, normally 11" w.c. Ideal for medium commercial
Installations, vapor meter Installations and normal domestic loads.
Wenb4'irfea
• 90 degree right angle inlet to outer connection for meter or
standard installations.
• Large vent helps to prevent blockage and has a/P F. NPT for vent
piping.
• With 15 PSIG inlet pressure, regulator Is designed to not pass
mote than 2 PSIG with the seat disc removed.
• Replaceable valve orifice and valve seat.
• Straight line valve closure reduces wear on seat disc
• Unique bonnet vent profile minimizes vent freeze over when
properly Installed.
• Large molded diaphragm is extra sensitive to pressure changes.
• Built in pressure tap has plugged % F. NPT outlet. Plug can be
removed with a 3/16• hex allen wrench.
• Select Brown Finish
Can mount directly to vapor meter. It is also suitable for mounting
directly to the house piping. It will retrofit into existing Installations that
are currently using a 90 degree, right angle regulator.
Body...........................................................................
Die Cast Zinc
Bonnet........................................................................
Die Cast Zinc
Nozzle Orifice.........................................................................
Brass
Spring......................................................................................
Steel
Valve Seat Disc .....................................................
Resilient Rubber
Diaphragm .........................
Integrated Fabric and Synthetic Rubber
IclrrR�farr5�m� i{161Sx:�rn.�11,+,5ilenmt
n
w/MomtinsBracket
:1 'RA
�„1
1
Bf1143: 250,000 500,000 750.000 1,000,000 1,250,000
'P,art�Nulnben
_ TNe[Conne'c-tionl
Outleh—�
r6`on`necGon +
Onhce•,—i
S1se J
1FacloryDelivery -
Presure
rEdjustrn o� ,
Ranger`
Bome[Ue'nU
Portion
Vapor CaPauty.'BTU{h, I
rna-amne' _1
111 111
®®®®®®
• Maximum flow Is based on 10 PSIG inlet and W w.c. deliverypressure.
•• Mounang Bracket Included. �y�"a..
100 Rego Dr. Elon. NC 27244 USA w ..agopmducls.com G7 +1 (336) 449-7707 A21
ES-D-GAGGenerac InstallSmart
Job Name _
Job Location
Engineer
Approval
Generace ""Ii r t $ ��
Flexible Fuel Lines
The flexible connection between the gas supply and the gas inlet
of a Generac® Stationary Outdoor Backup/Standby Generator
Features
• Operating Temperature -40-F to 150•F (-40°C to 65.6•C)
• 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
• Flare Adapter Material
Carbon Steel with Zinc Trivalent
Chromate Plating
• PVC Dip Coating
Gray Heavy Duty, Antimicrobial,
UV Stabilizer
CSA Group Certificate of Compliance to
Product Standards
ANSI Z21.75/CSA 6.27 — Connectors for Outdoor Gas
Appliances and Manufactured Homes
Scope states "...intended for exterior use above ground for
making non -rigid connections... between the gas supply and
the gas inlet of an appliance for outdoor installation that is not
frequently moved after installation." In addition section 1.5.4
states the connector is designed for occasional movement after
installation. Repeated bending, flexing or extreme vibration must
be avoided. Normal operation of a clothes dryer, rooftop HVAC
unit or SIMILAR OUTDOOR APPLIANCE DOES NOT constitute
extreme vibration or movement.
ANSI Z21.24/CSA 6.10 — Connectors for Gas Appliances sA,
(Excluding 60/61 Series)
c us
Product Configurations
Contractor
Approval _
Contractor's P.O. No.
Representative
SKU
For use with Generac stationary outdoor backup/
standby generators.
Applicable Codes
ANSI Z223.1/NFPA 54 National Fuel Gas Code Section 9.6
Intemational Fuel Gas Code (IFGC) Section 411.1
B149.1 — Natural Gas ana Propane Installation Code (CSA
Group) Section 6.21
Uniform Mechanical Code (UMC) Section 1313.0
Uniform Plumbing Code (UPC) Section 1212.0
Additional Approvals
Commonwealth of Massachusetts Board of State Examiners of
Plumbers and Gas Fitters
Additional Testing
UL2200-2015: Stationary Engine Generator Assemblies Section
66B Vibration Test.
eoonuntproductspecficadons In U.S. customary units and metric are appmAnnate and are pmvidedfor reference ony. Ferpreem ® ��®��®
measurements, please contact emmontTedWcorm l Service. Dormant reserves the right to change ormodglanduct design,construction, \��//
spedfirations, or matedais wfthoutpdor noece and wilhout inaming arty obffgaton to make such changes and mocfficadons on Dormom
products preMusiy or subsequently sold. Refer to the owner's manual farwanantylnfouWon A WATTS Brand
Minimum Flow Capacity at Specified Pressure Drop
Straight Length BTU/hr. NATURAL GAS, 0.64 SG, 1000 BTU/cu.fL
Generac'
Pad Number
GONFIGUMANON
Donnom°
Part Number
SFAIFS
1
Nominal ID
in
Nominal Lenght
In
0.50 in
0.75 in
PRESSURE DROP
1.00 In1.251n
(INCHES WATER
COLUMN)
150In
1.751n
200 in
10000009793
CAN41-4141-24GEN
1 41
%
24
1 290,900
356,278
411,395
459,953
1 603,854
544,224
581,800
10000009nG
CM41-4141-48GEN
41
%
48
217,000
265,770
306, 884
343,107
375,855
405,970
434,000
10000009717
CAN41-4141-72GEN
41
e/a
72
173,900
212,983
254,932
247.960
301,204
325,337
347,800
1000000D498
CAN51-5151-24GEN
51
1
24
581,800
712,657
822,789
919.907
1,007.707
1,088,448
1.163.600
10000000499
CAN51-5151-4BGEN 1
51
1
48
442,700
542,195
626,072
699,970 1
766,779
828,216
885,400
10000000500
CAN61-5151-72GEN 1
51
1
72
347.809
425,966
491,963
549,920 1
602,407
650,674
695,600
Straight Length BTU/hr. LP GAS, 1.55 SG, 2500 BTU/cu.fL
GenemC
Part Number
CONFIGURATIONO'
0ermoor
Pad Number
SERIES
Nommai lD
In
Nominal Lenilm
in
0.50 In
0.75In
1.00In
(INCHES WATER
1.251n
COURAN)
1.50In
1.75In
2.00 in
10000009793
1 CAN41-4141-24GEN
1 41
1 94
1 24
1 465,400
1 569,996
658,175
735,862
806,096
870684
930,800
10000009776
CAN41-4141-48GEN
1 41
a/4
48
344.000
1 421,312
486,489
543,912
595.825
643,565
688,000
10000009M
CM41-4141-72GEN
41
V,
72
278,240
341173
393,491
439,936
481,926
520,539
556.480
10000000498
CAN51-5151-24GEN
51
1
24
930,880
1,140,091
1,316.463
1,471,851
1.612,331
1,741.617
1.861,760
100D0000499
CAN51-5151-48GEN
51
1 1
48
708,320
867,511
1,001,716
1,119,952
1,226,846
1,325,145
1,416,640
10000000500
CAN51-5151-72GEN
51
1 1
72 1
556.480
681.546
786,982
879.872
963.852
1,041.079
1.112.960
Generac pad number 10000000498 (Dormont part number CAN51-5151-24GEN)
can supply a minimum of 581,800 BTU/hr.of natural gas B 0.50 in. water column
pressure drop to the generator.
All installations must completely comply with all DOrlimnte manufacturing company warnings
and instructions, national, state and local codes and all applicable ANSI standards.
u&monto
A WATTS Brand USA: T. (800) 367-6668 • R (724) 733-48DB • Donnont.com
Canada: T. (905) 332-4090 • R (905) 332-7068 • Dormont.ca
Latin America: T: (52) 81-1001-8600 • F. (52) 81-8000-7091 • Donnont.com
ES-D-GAQGenerac_InstallSmart 1703 0 2016 Donnont
1
Maximum Capacity of PE Pipe in Thousands of BTU per Hour of Liquefied Petroleum Gas
with a Gas Pressure of 11.0 In. WC and a Pressure Drop of 0.5 in. VIC
20
18
15
13
12
- 11
10
9
• 9
8
8
8
7
7
113
102
86
76
68
63
58
64
51
48
46
44
42
40
147
132
112
99
89
81
76
70
66
63
60
57
54
52
209
188
160
140
126
116
107
100
94
89
85
81
78
75
376
338
287
252
227
208
192
180
169
160
152
146
140 .
734
569
516
441
391
354
326
303
285
269
255
244
233
224
216
1061
956
810
712
642
587
544
608
478
453
431
411
394
379
2516BTUh=ICFH
Maximum
Capacity of PE Pipe In Thousands
of BTU per Hour of Liquefied Petroleum Gas
with a Gas Pressure of 2.0 psi and
a Pressure Drop of
1.0 psi
11800 7586 6008• 5092 4479 4033 3478 3007 2707 2478 2295 2144
74652 9835 7790 6602 6807 5229 4432 3898 3510 3213 2975 2780
20877 74014 77100 9408 8275 7451 6316 5555 5002 4578 4239 3962
37514 26188 19946 76905 14869 13389 71348 9982 8988 8226 7618 7119
43429 29848 23969 20516 18182 16474 74700 72496 11322 10477 9691 9092
105963 71131 66339 47750 42000 37820 32054. 28194 25388 23234 21517 20108
zdo
2U7
187 Ib8 139 125 775 IDb 99 93
88
84
80
77
74
7995
1192
1073 910 800 720 659 611 577 537
508
484
462
443
425
7767
1545
1391 1179 1037 934 855 792 740 696
659
627
599
574
551
2503
2202
1983 1680 1478 1331 1218 1128 1054 992
939
893
853
81B
786
4498
3956
3563 3019 2656 2397 2189 2027 1894 1783
1688
1605
1533
7469
1412
- 6903
5232
4740 4057 3596 3258 2997 2788 2616 2471
2347
2239
2744
2060
1985
12705
11175
10063 8529 7502 6755 6182 5725 5350 5036
4767
4535
4331
4150
3988
25T6BTUh=1CFH
Maximum Capacity of PE Plpe In Thousands of BTU per Hour of Liquefed Petroleum Gas
with a Gas Pressure of 10.0 psi and a Pressure Drop of 1.0 psi
(based on a 1.62 specifia gravity Bps)
14234
9555
7668
6414
5642
5080
4306
3757
34TO
3727
2890
2707
2542
2236
18455
72388
9812
8316
7375
6587
5583
4910
4422
4947
3747
3502
3296
2899
26296
17652
13981
11849
10423
9385
7954
6997
6300
5766
5340
4990
4697
4137
47252
31720
25723
27293
18729
16865
14294
12572
17321
10367
9595
8967
8440
7423
53960
37087
29782
25489
22591
20469
17679
15527
74068
72943
12041
71297
10671
9458
733476
89601
70967
60148
52905
47640
40376
36614
37980
29267
27104
25329
23840
20970
Ph: 1.800.662.0208 o Fax: 615.325.9407 ^ Web: www.gastite.com
N
-----------------------------------------
O
O
O
O
O
O
O
O
O
a
b
C
m
N
O
I'
m
h
m
T
lIF
V
t0�1
N
N-
--
0\
U\
ao
l�
b
b
YI
V1
'd'
-IF
-If
N
O
O\
I�
b
Ym1
V
tN+l
N
O
Q
w
b
Y�1
VOi
V
m
?
M
M
C1
nl
m
Hf
„;
m
N
N
N
14
f`(
N
CI
m
y
O O
O
O
O
b
O
O
o
Y OB
O
O
O
O
O
O
O
N
O
b
Om
O
V1
O
O
O
O
O
O
O
O
O
O
O
O
N
O
O�
t+f
O
O
N
b
N
W
h
o0
V
O
r
m
sY
r
b
O
m
D\
o
D\
M
O
m
O
M
O
m
O
O
M
O
O
O
o
0
0
Ol
,y
O.
ro
ri
b
b
vi
N
V
sf
V
m
m
m
N
ofN
N
„may
CI
O
Of
O
ON.
php
h
N
h
m
N_
.y
.-i
...i
4
.-i
.-i
14Vi
6
---------------------
a
m
Q\
M
m
16
N
Cf
N
N
R
N
�_0
9
b
0
0
0
0
0
0
0
0
0
0
0
0
0
0
y
N
N
d
b
b
V
n
m
N
l+1
m
v
N
KNi
N
N
N
O
N
g
n
vL
m
ti
O
=
CI
.y
�„�
O\
S
m
m
C`
n
n
b
b
b
�D
vQf
V�1
vbf
VMl
v01
V
V
V
V
a
V
6
L
m
O
�
N
T
N
I?
W
h
V
T
b
V
M
N
19
1
O
C
C
y
N
c
WtU0
(hn
b
C
N
a------------------
m
eO�I
O
V�
C
N
_a
a
a
N
m
m
b
h
V1
'y
N
n
h
h
V1
O�
O
r•
a0
y
W
n
O
�
r-�
N
V
W
Z
U
OCl
N
m
M
V
Vl
Vhl
b
b�
n
m
W�
Q
O
O
N
M
V
Vl
b
h
m
D\
O
z
eArlmm. EnptllyafTxW nfauma541YY 653AT:mmeanlelUMr Nmma WvpxaEu
-IAtn:4 Fi-el'a-iuie. : {1 r .
j6uq en a Is spc5v EnXyl ID0 RJ w aMc tml EY)
a• a >1 59 u Ia w v m m IT a
a z1 a v n m u n 11 !
a
e
e
e
Zur .... 1 ui:�
;:
- ..
wfp!
W
x1B ]m3nia
�gl
]atIi�/YI1G,'
; '� 9 :,li
SAu9
Y ,ctm!cYRIvs9
ImIT]�
x
,�IfwmsiZ]i).
r
..i.szITaaRzs
.mu}yvvTaa.r
11
.e
9r
w:1
�-7rj
- -'.
-�
++.•
b Td
t LL59my
hoIiu65�9fla.
:ataYmw91s]ix»9 Ws
m:'1:t1imm
!i
lveam
W,.S
]
:� ;-
4.i2mfuw4s
��weus,Jtsm]1ISa!l
....a3vatig�.2 ,•:'.
.4a.3s1.amN2
.se11]T%te9h
mviL
vG
F!w
s.aitmnslie9
tv
.
Tad
C!y-alifs]]0u
a�go $,eC"a•..
•�eY.�•
� 3iKs �z1 v
ms;e; m.Rt ir1xzma u.
:}ta_ema"gm.m,.1
.::S
:Hvs TtlsabwxYWYm (v 4vmCNra YtlaW b9ebeL9Y iuenAb9b.m:4naq[Nav'W
ep9aNLYmamlb PambeYebribtl504vbmabbbvmwne
(n
ID
TEbIE P-1A Prepane LmvPressure
I I
maemav GV+W NT:Wwrvm45vtxe G4TA]rve+wetxmlmlbuaa WUP'^m Ev
l9ando 1 nrlry/L']�p E1v(mtEu)
m .v1" r s l l i l iSi Tl e^F:1 61 1
1 i! iti.. ia. P I xs ti-•'l u l n y*�
..� .,�
`� L....
t 1 M
ip +v 1w m T m u a w 1
w m yx v u m a_ 3 a vi 1 16 1 n
J�a]m
n n
v� u
e B
15. h W rm m
Y•.: w.�
_...]�>
-
..A
% tiatl
3EJ }69�1+ R
;�.
I �N- 2T Ilm IW 13f9 11 IPO W m a9
j��„*ie. � mj• e
file 64 ®2 SYx 6fi> SOI 1& f i61 Z9 m) 359 a1 31]
m] 1m
@ 11
168 1f'I
1H 11p
26!: ?xs t ye; iisl
,ems 31--
to
3 z
= :aF
r w mR 6ue 5a1 Ieu 1 am ]xm a!a
R. •"":- i'^ x'i..R: r� f iv. .,.[�� .3 ✓a
zwo 3 1 age mm tms uT lax zm
� .a„. F.] 1 We eV ]R
x l
6a 03
691
6W 511
Yel¢ FNOIFMEMaMyYWbflemeb!/ ACaueYd YYwIiMMRa W hpnWNwMgr`ntltlubWa.
Ilb MlapwlYr/tlalmeawe iNaNmlvbumebmnmrt64MuyvbYpbempNrenlnsMMa.
ae,eGwma./mur6:9.a�:�nii.ia.�ev.nnm�.ieyvidx<no.eim.n.nma.mmniemea°ea, e�.!.s """•� ••••••��_:••w:.::::�:e.:.:o.o.w �,ea.,,d o..o®w•. w`..N�m9
Nnlmm. EapiAfWTmFpYCwnWreC6 CESibTe.�aHmYwbnuaa WWm�Eaa
119as1m�1 pWa4mibx3ROBNw�N�An[Eul
Nnlmm. EapiAfWTmFpYCwnWreC6 CESibTe.�aHmYwbnuaa WWm�Eaa
119as1m�1 pWa4mibx3ROBNw�N�An[Eul
Yatlmvv C.IvlolTr IbwMMb Bfm TvmWaat6Nwllmvaq^Y:e•S+as
(EaaNwal!]spatlPe ErarXy l34u llYpnmdeSv+l Onl
3n
1
ISr
ip
a
i6
ip.l
i5
jl
t]311
i W
Im5
ae
5 p
T
1 E..11
1
PI
1
fSOY:
[fl�0)
,•OV
•R`
-•X
.,fit•
'JA
W
HY
]T11
ax
10
131
11j11
Im
L,.1
n
61.
m
me
n
3a
a
a
la'
n
13
fe
161
Y
/
61 r19I'.
/9L
3A
'ID]1'124,
ae
3E9{:Y
�.
l�
fM
rt�?
10�i13f
J]1lFiati
Nllnr
�im
}N...
4BI
.y
'.i53.
r161
]Y lE'�+fT11�f1?vi6.
'�a].'F
f05-R'.-]d'.
�:�9.
�Tl
r]a:
9�ciy l'.
]p%
a
1193
SY
6m
mf
f93
w]
m!
!R
ID
]m
'A1
ZT
1
IP
181
1w
1T
116
fm
1m
T
]B
T
—1 -.
Lisfr
1�1•
+ixs
_Fw.
�9m?
4!1W
ea.:.mi:.iln'
r69Q
✓
S�a'za
,,m.:
ip:.5?e
rix
'
eisi:
•zli
lym
1BI'
tm
tm`"1T
118
r.i< 1
tm
- - 3
'Ya
Ei
+ff
jss
1'tl-
1111'
]Te
31f]
'QSS
99f9
1xM
lm9
1 9]
13w
f113
1m8
f0a
B91
4V
168
ne
ml
sei
E
wx
%p
a6
=1
ax
Ea
-1
31x
i1lYaS ix:.
mT
aSm
m6t
]In
3eM
iSN.IDa
tm]
iBll.
IER
teID
yf>{.
Swd
iwe
faf.
1fls
.6W
869-
M9
,69I
ea.
$m
��
w1
3Q
w9
:
`a9'-]N-
�]9
r 6]
la
IG]
x._
M55
.:: �..'..
]a9
SSV
r^it";�t
59iE
�..;.N-'"'
S1T
!
ww
]9A
]e]B
]IBI
aJ0
als
,..a•,i..,
mH9
ID
tr
IDm
s"
.
155E
1
f
IMB
-.
1N9
YE:
I1m
11
IM
9T
9 f
91
06f
E.W
IN�n.ir.•iew.amnwilrme,viibaam�bu:r.mti. �nr.ace�.imi,�.�ew. r°