HomeMy WebLinkAboutGas Piping Schematics & Set-Up ManualsBOARD OF
COUNTY
COMMISSIONERS
GAS PIPING SCHEMATIC
JAN 0 1 ?'T7
TANK SIZE: �U� + GALS.
APPLICANCE — TYPE/SIZE
Al +eof
A2
A3
A4
A5
A6
3��Od6 BTU
' BTU
BTU
BTU
BTU
BTU
PIPING LENGTH & SIZE
L1 1� Q FT. 3/61-INCH DIA.
L2—FT. INCH DIA.
L3 FT. INCH DIA.
L4 FT. INCH DIA.
L5
FT.
L6
FT.
L7
FT.
L8
FT.
L10 FT.
L11 FT.
L12 FT.
Revised 7/22/14
INCH DIA.
INCH DIA.
INCH DIA.
INCH DIA.
INCH DIA.
INCH DIA.
INCH DIA.
INCH DIA.
PLANNING & DEVELOPMENT
SERVICES DEPARTMENT
Building and Code Regulation
Division
(PIPE SIZC�TAKEN FROM
THE 2014 F FUEL GAS CODE -
TABLE 402 (�)
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Web'site: w .stlucieco.aov
2300 Virginia Avenue - Fort Pierce, FL. 349825652
Phone (772) 462-1553 FAX (772) 462-1578
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THIS DOCUMENT PREPARED IN THE OFFICE 0FI OIAMITND ON PzVENp/i'
ELEVATION - 8.20' NAN
C.A. MITCHELL AND ASSOCIATES, INC. 4.1wtu.p..l
LAND SURVEYORS AND MAPPERS EA--
759 S.W. SOUTH MACEDO BOULEVARD Airs
PORT ST. LUCIE, FLORIDA. 34983 Ixe c
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ELEVATIONS REFLECTED ON MS ORAVANC ARE BASED UPON
NORTH AHFRICAN VERTCAL DATUM OF 1988, MORE SPECIFICALLY
ST. LUCII' COUNTY BENCIWARN "ELMS- ELEVATION - 7.08'
oESMPTl4V:(SUPPUEB UY CLIENT)
LOT II d LONE PINE SUBDIMSION', ACCORDING TO THE
PLAT THROUM"II'7S OFAISNEEP PUBLIC RRDED ECORDS OF ST. WOEPAGES
COUNTY,
RORIUA. NAG LANDS STRIATE IN ST. WOE COUNTY, RORIDA.
88'87'25"E
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FORM BOARD LOCATION ANU
ELEVATION: SEPTEMBER n. 2010
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LOT II OF "LONE PINE SUBDIMMON'• 14111 LONE PINE
FORT PIERCE• FLORIDA.
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FA MITCRE AND ASSOCIATES. INC. C
TRCATE OF AUTNGRIZAD N N0. LH427B fT
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MAY 8, 2019
MAPPER
BOUNDARY AND TOPOGRAPHIC ONE
SURVEY OF
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Pat�nt�p_ee`niimg formul'atedspnme7and�topcoati t
_ , • Dual service optidns for•above.or underground,applidationsr
• Option 41: Ready -to bury tgd ozide,durable powder coating'witH black
I • polyethylene'AGUGldome,- ,,
• Option tk2: Abovegroundoption with steel 8" AGUG dome
• All valvesiand float gauges aee,centered under dome -
'_ •°Fabricated,to the"Iatbs§Vk§,;UE Code, Section•VIII, Divisidn 1
' •Registerr"e8 withithe`IJational Board'
�.�� '• g721iquid level•outage•Valve otifise.reduces refueling emirs"ions
t
." • Vacuuni.pre=purged-Wsaveaime; money and'produdf; ,
3 , •Applicable /edeYalstate, or local regulations.may contain•speci wrequ'iremenls for
p otechve,coatings and•cathodic protection The purchaser`and intallel;are responsible
I ",..'; (or'compGance'wdh alhfedeFa/ state lo_c"al and NFPAindustry r`eg`ulations.Cathbdic.
+ ;fpLofecticoninuousandluninte[rupted,andm'ust .`
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LEG
WIDTH
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
-- D➢CE
FLOAT LP. cas ANODE
GAUGE ® X CONNECTION
FILLER
O O ' VALVE
SERVICE! NAME
MULTIVALVE PLATE
RELIEF
VALVE
FITTINGS LAYOUT UNDER DOME
AGUG VESSEL DIMENSIONAL INFORMATION
All vessels dimensions are approximate
WATER
OUTSIDE
HEAD
OVERALL
OVERALL
LEG
LEG
WEIGHT
QUANTITY
CAPACITY
DIAMETER
TYPE
LENGTH
HEIGHT
WIDTH
SPACING
FULL
PER
LOAD
STACK
120 wg.
24"
Ellip
5'- 5 13/16"
3' - 0"
10 118"
3' - 0"
245 Ibs.
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"
Hemi
7' - 2 112"
3' - 7 1/2"
12 3/4"
3' . 6"
472 lbs.
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"
Hemi
8' -11 3/4"
T - 7 1/2"
12 3/4"
4' - 0 1/4"
588 lbs.
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.
37.42"
Hemi
9' -10"
4' -1 7/16"
15"
5' _ 0"
871 lbs.
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 13116"
4' - 4 5/16"
16 1/4.'
9' - 0"mm
1729 lbs.
15
5
3785.0 L
1040.4 mm
4mm
846.E
1344.6 mm
412.8 mm
2743.2
784.3 kg
Rev. Jan. 27, 2016
X J h'.
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 bythe 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 currentfrom 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 generally very effective. The following chart
provides size and quantity recommendations for various 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 it 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.
Soil Type
FeilileSuils Clay; ,'
ice_ SzndyLda'm . r_
Sand, Gravel, Rocky
Areas
Tank Cap.
t 1id1500D ohm
r-.:..ir-_.._l:�s
& fi)
5000 to 10000 ohm -cm
(gal.)
Slier
r>... e
, Via:
cA11o�`
c .yc
Size
Oty.
Alloy
y
1209
kx';
[' 1_
t [H=ai`
9#
1
H-1
1509#�?'.7f
a
� Hr-j:;
9#
1
H-1
250
9#
2
H-1
325;9#
(_11.
E H=1r
9#
2
H-1
500
9#
2
H-1
1000
` 17�^'"'2°
r.s,t_
,`_'H 1i'
r
9#
4
H-1
1500
7515
'2'
�:lili.
9#
4
H-1
2000el'*
LH 1c
9#
6
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
c:Dd c c
O O O
c C=Da c o�
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 over to 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.
Mechanical 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 (Yz 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) at four 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 Yz 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 not allow electrode to contact oil, road salts, or other
substances that may contaminate the solution by absorption
through porous plug. Do, not allow electrode to freeze.
Distributed By:
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.
cmuir•
• Compact design can be connected to a service valve using either
a POL adapter or a RegO product pigtail.
• Large threaded 3W F.NPT bonnet vent can easily be piped -away
underground Installations without the need of glue kits or extra
adapters.
• Non Adjustable
• Large flow 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 % F.NPT 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.
iiZx`!W& 3
Body............................................................................................Zinc
Bonnet.........................................................................................Zinc
Spring........................................................................................
Steel
Seat Disc........:........................................................Resilient
Rubber
Diaphragm...........................Integrated
Fabric and Synthetic Rubber
W+u Itu'.:Jt tiu `�'� lili'hLLlLl3�4.•.�ii� }ry 5�i
YAF . 10:31 0:1
�Y .1 i
3.56•
rwweaoenxe
Part Num lj_Connebtion;
ZF"�C`��•—n1
, -•. TI
�OUet Connection
OnficeSze;'
Factory,
' ,r
Debvery I
Psu resre`-
^-------r--r
�' '
Bonnet�Nenl Posrhov,'
^-a-�-T-- -r-•
`Vapor CaPaolyiBTURv�
P,-7,opane$ ICI
®®®®
•
11 111
11
Maximum flow based on Inlet pressure 20 PSIG higher than the regulatorsefling and delivery pressure 20%lower than the n:gulalorsetting and derivery pressure 20%lower Nan the setting.
A14 Maffa. 10D Rego or. Flan. NC 2M" USA w nagoprodus .ram +1 (335) 449-7707
3�^atra
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.
IFIM)TUr S
• 90 degree right angle inlet to outer connection for meter or
standard installations.
• Large vent helps to prevent blockage and has F. NPT for vent
piping.
• With 15 PSIG inlet pressure, regulator Is designed to not pass
more 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 1W F. NPT outlet. Plug can be
removed with a 3116• hex allen wrench.
• Select Brown Finish
W�9i$AMITISR'sGiS&P-19M
Can mount directly to vapor meter. It is also suitable for mounting
directly to the house piping. It will retrofit into existing installations that
are currently using a 90 degree, right angle regulator.
Body........................................................................... Die Cast Zinc
Bonnet........................................................................ Die Cast Zinc
NozzleOrifice......................................................................... Brass
Spring...................................................................................... Steel
Valve Seat Disc ..................................................... Resilient Rubber
Diaphragm ......................... Integrated Fabric and Synthetic Rubber
Grdaidmg T?m ffka—mTu^�-m
w/Mounting8racket
t t n t t1 r rt t •ta � r r
..,t t.!• �t 1u ��(1 ut
1
Outlets
Onhce
,�51zeA
i£aetoryDehvery
Adlasanentr
I
Bonnet Ven[ Vapu ,Capauty`$TIl%tv`d
1��ry¢ gin
rP,arDNmnber
IolefCbnne�noni t
(Connecbon'
•tP[ sv�e
Ranj;e]x
Pbsid3n
111 111
•�®®®®®®
Maximum finds based on 10 PSIG INet and 9•w.t. deliverypressure.
•• Mounting Bracket Intruded. r�y�
100 Rego Dr. Elon, NC 27244 USA w ..repopmductecom +1 (336) 449.77a7 GI7"10.
0
ES-D-GAGGenerac InstallSmart
Job Name _
Job Location
Engineer
Approval
Generaco(l Pi",' S 11"Illlln T, O'
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 150OF (-40°C to 55.60C)
• Operating Pressure
MAX 0.5psi (3.45 kPa)
• Hydrostatic Burst Pressure
MIN 250psi (1726 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, Antimicroblal,
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 vibratlon 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
International Fuel Gas Code (IFGC) Section 411.1
B149.1 — Natural Gas and 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
UL2200-2016: Stationary Engine Generator Assemblies Section
66B Vibration Test.
Dormant pruductspecificetlons In D.S. customary units and metric are appmxMate and= panidedforrefsence only. rorpredse D rmont®
measurements, please contact DornontTechNrzl Service. DonDat reserves the right to change or moddy product design, construcfion,
specifications, or materials whhout prior notice and wftut focusing any obligation to make such changes and maMcetions on Dornoht
products previously or subsequenby sold. Raferto the owner's mamral forwarmnty irdormafom A WATTS Brand
Minimum Flow Capacity at Specified Pressure Drop
Straight Length BTU/hr. NATURAL GAS, 0.64 SG, 1000 BTU/cu,ft.
6enemC
Part Number
CONFIGURATION,.,.
Dmarff
Pad Number
SERIES
Nominal l0
in
Nominal Lenght
in
0.50In
0.75In
1.00 in
(INCHES WATER
1.25 in
COLUMN)
1.50 in
1.75 in
2.00 in
IDOODOD9793
CAN414141-24GEN
1 41
1 '/4
24
290.900
356.278
1 411.395
1 459.953
1 503.854
1 544,224
5111,800
10000009776
CAN41-4141-48GEN
41
%4
48
217,000
265,770
1 306.884
343.107
1 375,855
1 405,970
1 434.000
10000009717
CAN41-4141-72GEN
41
'/
72
173,90D
212,983
254,932
247,960
301,204
325,337
347,800
1000DO0D498
CAN51-5151-24GEN
51
1
24
581,600
712,557
822,789
919,907
1,007,707
1,088,448
1,163.600
1000DOOD499
CAN51-5151-48GEN
51
1
48
442,700
542.195
626,072
699,970
766,719
828,216
885,400
10000000500
CAN51-5151-72GEN
51
1
72
347,800
425,966
491,863
549,920
602,407
650,674
695,600
Straight Length BTU/hr. LP GAS, 1.65 SG, 2500 BTU/cu.lL
.,. (INCHES WATER
COLUMN)
6eneW
Part Number
Dam omr
Part Number
5FRE5
NamNal ID
in
Nominht
In al Leng
0.50 to
1 0.75In
1.00In
1251n
1.5013
1.751n
2.00In
10000009793
CM41-4141-24GEN
41
1 V
1 24
1 465.400
1 569.996
1 658,175
1 735,862
1 8D6,096
1 870.684
1 930,800
1DODOOD9776
CAN41-4141.48GEN
41
%
48
1 344,00
1 421.312
1 486.489
1 543.912
1 595.825
1 643,565
1 688,000
10000009777
CAN41-4141-72GEN
41
D'4
72
278,241
340,773
393,491
439.936
481.926
520,539
556,480
100000OD498
GAN51-5151-24GEN
51
1
24
930,880
1.140,091
1,316.463
1,471,851
1.512,331
1,741,517
1.861,760
100000OD499
CAN51-5151.48GEN
51
1
48
708,320
867,511
1,001,716
1,119,952
1,226,846
1,325,145
1,416,640
100DOOD050D
C4N51.5151-72GEN
51
1
72
556,480
681,546
788999
879,879
963,852
1,041,079 1
1,112,960
Generac part number 10000000498 (Dormont part number CAN51-5151-24GEN)
can supply a minimum of 581,800 BTU/hr.of natural gas ® 0.50 in. water column
pressure drop to the generator.
All Installations must completely comply with all Dormant® manufacturing company warnings
and Instructions, national, state and local codes and all applicable ANSI standards.
l�
r
A WAM Brand USA: T: (800) 367-6668 • F: (724) 733-4808 • Donnont.com
Canada: T. (905) 332-4090 • F. (905) 332-7068 • Donnont.ca
Latin America: T: (52) 81-10DI-8600 • F. (52) 81-8000-7091 • Donnont.com
ES-D-GAC Generac InstaliSmart 1703 (D 2016 Donnont
Maximum Capacity of PE Pipe In Thousands of BTU per Hour of Liquefied Petroleum Gas
wish a Gas Pressure or 11.0 in. WC and a Pressure Drop o 0.6 in. WC
(basetl on a 1.52 spoclffc gravivgas)
zu
lb
lb
IS
12
11
1u
9
9
8
8
8
7
7
113
702
86
76
68
63
58
54
51
48
46
44
42
40
147
132
172
99
89
81
75
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
760
752
146
140 .
734
569
516
441
391
354
326
303
285
269
265
244
233
224
216
7067
956
810
712
642
587
544
508
478
453
431
411
394
379
25768TUh=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
7.0 psi
17300 7586 60D8• 5092 4479 4033 3418 3007 2707 2478 2295 2144
14652 9835 7790 6602 6807 5229 4432. 3898 3510 3213 2975 2780
20877 14D14 11100 9408 8275 7451 6315' 5555 5002 4678 4239 3962
37514 25783 19946 169D5 14869 13389 11348 9982 8988 8226 7618 7719
43429 29848 23969 20515 18782 16474 14100 12496 11322 70417 9691 9092
105963 77131 56339 47750 42000 37820 32054 28194 2538E 23234 21517 20708
1 �z
iuro riu auu au WY 611 bdi 637 508
484
462
443
425
1545
7391 1179 1037 934 865 792 740 696 659
627
599
574
551
2202
1983 1680 1478 1331 1218 1128 1054 992 939
893
• 853
BIB
786
3956
35633019 2656 2391 2189 2027 1894 1783 1688
1605
1533
1469.
1412
5232
4740 4057 3596 3258 2997 2788 2616 2471 2347
2239
2144
2060
1985
11775
10063 B529 7502 6755 6182 5725 5350 5036 4767
4536
4331
4150
3988
2516BiUh=iCFH
Maximum
Cappacity of PE Pipe In Thousands of BTU per Hour of Liquefied Petroleum Gas
Nth a Gas Pressure of 10.0 psi and a Pressure Drop of 7.0 psi
(based on a 1.52 specific gravity gas)
1 14234
9555
7568
6414
5642
5080
4306
3787
34M
3127
2890
2701
2542
aer
2236
oau
2014
18455
1238E
9812
8316
7315
6587
5583
4910
4422
4047
3747
3502
3296
2899
2611
26296
17652
13981
17849
10423
9385
7954
6997
630D
5766
5340
4990
4697
4131
3720
47252
37720
25123
21293
18729
16866
14294
12572
11321
10361
9595
8967
8440
7423
6685
5396D
37087
29782
25489
22591
20469
77519
t15527
14068
12943
12041
71297
10671
945E
8569
133476
89601
70967
60148
52905
47640
40376
35514
31980
29267
27104
28329
23840
20970
18882
7707
2213
3153
5665
7334
16004
Ph: 1,800,662.0208 ^ Fax: 615,325.9407 o Web: www.gcistife.com