HomeMy WebLinkAboutcut sheetsN
O
►-1
T
r-
O
D
W
C
Z
G)
n
O
0
m
m
O
Z
BOARD OF
COUNTY
COMMISSIONERS
TANK
SIZE
tA2)
[L4]
L3]
L2]
[Al]
ST.
LU-CI
E
COUNTY
F
L O R
I D
A
GAS PIPING SCHEMATIC
[A4]
[L8]
L5 L7 L9 L11
[L6] [L10]
[A3] [AS]
TANK SIZE: %�" GALS.
APPLICANCE — TYPE/SIZE
Al G.,f c,: ; 7
A2
A3
A4
A5
A6
PIPING LENGTH
& SIZE
L2�' FT
-INCH DIA.
FT.
—IL
INCH DIA.
L3
FT.
INCH DIA.
L4
FT.
INCH DIA.
L5
FT.
INCH DIA.
L6
FT.
INCH DIA.
L7
FT.
INCH DIA.
L8
FT.
INCH DIA.
L9
FT.
INCH DIA.
L10
FT.
INCH DIA.
L11
FT.
INCH DIA.
L12
FT.
INCH DIA.
c C3C.' BTU
BTU
BTU
BTU
BTU
BTU
PLANNING & DEVELOPMENT
SERVICES DEPARTMENT
Building and Code Regulation
Division
[A6]
[L12
(PIPE SIZE WAS TAKEN FROM
THE 2014 FBC FUEL GAS CODE -
TABLE 402 ( ))
Website: yt",sti&i .r_n v
2300 Virginia Avenue - Fort Pierce, FL. 34982-5652
Revised 7/22/14 Phone (772) 462-1553 FAX (772) 462-1578
i20-21000 wg
Finished with ArcClad",
Superior Aboveground Coating
8" dome in black plastic or galvanized steel
Fabricated to
A.S.M.Ecode Secti [��t7l'-PIAIJII
MI
;Ar-'-
S rank Features:
• Dual se
ice options for above or under
ground
pplications
Option 1
Superior, ready to bury, red
oxide d
rable powder coating with black
polyeth
'en dome'
Option
: Aboveground option with
Arcaa
coating and an 8" steel
AGUG d
me
�. ,,;;•. R on " Av'sion, ° All valve and float au
e9is[ered with the National Board gauge are centered
- - - - ... under
.......
md _me
iob�"maticri #Vacuu Purged - ..............
888.558.8265
#72 liqui level outage valve orifice
�e
10
p
12
GENERAL SPECIFICATIONS
Conforms to the latest edition and addenda of the ASME code for
Pressure Vessels, Section Vill, Division 1. Complies with NFPA 58.
Rated at 250 psig from -202 F. to 1252 F. All tanks may be
evacuated to a full (14.7 psi) vacuum.
Vessel Finish: Coated with epoxy and red powder. (Tanks coated
with the epoxy powder must be buried). For Aboveground use,
tanks will be coated with ArcClad', zinc rich epoxy primer and
super durable TGIC polyester topcoat.
'Applicable federal, state, or local regulations may contain specific r
installer are responsible for compliance with all federal state local and iremFPA Industry regulations.
equirements for protective co
continuous and uninterrupted and must comply with local, state or national code.
Waterftee
ide
Head
Capacityeter
Type
120 wg.'
Ellip
454.2L
mm
250 wg."
Hem!
946.3 L
mm
9"
320 w .Hemi
1,211.2 L
mm
500 w"
21,892.5
Hemi9
L
mm1000
wg.
6"
Hemi3,785.0
L
mm
All vessels dimensions are approximate.
............
Overall
Length
5'— 5— 13/16"
1.671.6 mm
2,197.1 mm
8'-113/4"
2.736.9 mm
2,997.2 mm
IT-1013/16"
4,846.6 mm
FOI r Ore iiv'Ol'fTlctlon
888.558.8265
Overall
Height
3' - 3/16"
919.1 mm
3' - 711/16'
1.109.6 mm
3' - 711/16'
1,109.6 mm
4' -15/8"
1,260.4 m,n
4' - 5 3/16"
1.350.9 mm
Leg
Width
101/8"
2572 mm
12 3/4"
323.9 mm
12— �
323.9 mm
381.0 mm
161/4"
412.8 mm
OVERALL LENGTH
F= -=� /— DOME
WITHDRAWAL
�aj�
VALVE
ANODE
CONNECTION
O ; FILLER
VALVE
NAMENAME
PLATE
and cathodic protection. The purchaser and
dic protection is required and coating must be
LegrWeig1t
Quality
Spacing
ght
Full
Per
Load
Stack
lbs.
96
12
914.4 mmg.
3' - 6"
1,066.8 rnmkg.
bs.
63
9
4' - 01/4"
bs.
45
91.225.6
mm
kg.5'-0"s.
mm
kg91
30
61,524.0
-0"bs
15
52.7432
mm
kg.
Eng. Update: April 5, 2016
---------------
f
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
conductivity of the soil promotes the flow of DC since the
circuit. current in the corrosion
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 surface 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
t protection methods:
external coating and
cathodic protection.
The
se two methods
are complementary
and should be used in
conjunction with the
other. An effective
coating insulates the steel from external protective
the soil environment, thus preventing
the flow of corrosion current from the anode to the cathode. An effective
external coating can protect over99% of the tanksurface 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 sys
are more commonly used for large structures such as large diametetemsr
pipelines. Electrical Isolation of the tank from metallic piping systems
and -electrical grounds*Is-critical for the cathodic protection-system's.
effectiveness.
Now 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 c upled to steel results in DC current flow from the
magnesium to a steel. The open circuit potential of steel is about
-0.50 volts refs nced to a copper sulfate electrode. The open circuit
Potential of ma nesium is about -1.55V to -1.80V By connecting the
two metals toge or, the difference of Ito 1.25V volts results in current
flow to the tank hat overcomes the natural corrosion cells that exist on
the tank With is current available to the tank, no corrosion occurs.
Magnesium An it
There are a va 'ety of anode sizes and alloys used for cathodic
protection. The WO primary alloys are designed as H-1 (or AZ63) and
High Potential. a 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 9% pure magnesium having an open circuit potential
up to -1.8V. Thi alloy should be used for soil applications over 10,000
ohm -cm resist' ' .
The two most c mmon anode sizes used for underground propane
tanks are 9 lb. an 171b. The size designation relates to the metal weight.
10' of #12 TW f sulated wire is attached to the anodes. Anodes are
then backfilled in a mixture of gypsum, bentonite, and sodium sulfate
to lower the elect cal resistance of the anode to soil. The mixture is a
low cost, nonh dous, electrically conductive backfill. The anode and
backfill is then pa kaged in a cotton bag and either a cardboard box or
paper bag. Actu shipping weight of these anodes with backfill is 27
lb. and 45 lb.
Application Reco mendations
Magnesium ano s can protect underground tanks in most soil
conditions. The H 1 alloy is generally very effective. The following chart
providessizeand antityrecommendationsfor various size tanks based
on conservative design assumptions. This chart covers soil conditions
up to 10,000 oh -centimeter resistivity. Resistivides higher than
10,000 ohrn-centii later generally represent very dry soils. Verification
Of soil resistivity c in be performed through soil analysis. Contact us
for design recom endations in locations where soil resistivities exceed
10,000 ohm -cm, o If there is no effective external coating on the tank.
The propane servi a line from the tank to the house also must be
considered in the athodic protection design, unless the service line
is plastic. All unde ground steel pipe should be externally coated with
i corrosion resists t material. The service line should be electrically
isolated at the hou a with an insulating fitting or union. If service pipe
is less than 50' in I ngth, the tank anodes will provide sufficient current
to protect both tan and pipe. For longer lengths of pipe, an additional
anode may be requ ad at the house connections.
If another* metallic aterial such as copperis used for service piping; - - - - - - the pipe should be electrically isolated from the tank at the fill pipe
connection. Copps and steel create a galvanic couple that will accelerate
corrosion of the st el tank when directly connected to copper piping.
Generally, copper pi ing does not require cathodic protection.
Soil Type
Fertile sails, Clay,
Sand, Gravel, Roclry
Sandy Loam
Areas
Tank Cap.
(gal.)
5 to 5000 ohm -cm
5000 to 10000 ohm -cm
Size
Q ty. Alloy
Size
Qty.
Alloy
120
150
91
9 ,�
1 H-1
1
9#
' 1
H-i
250
9#
H-1
1 H-1
91
9#�
1
2
H-1
25
3#
9
1 H-1
9,f
2
H-1
H-1
500
17#
1 H-1
9#
2
H-1
1000
1500
17#
17#
2 H-1
2
99
4
H-1
2000
17�
H-1
3 H-1
91
9#
4
6
H-1
H-1
'Based on 90%
yearAnods llle. eflecdve external coating, 2 ma/Ii2 current d— en— s 30-
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;P 7-
. C.
J
4-Anodes are shipped in either cardboard boxes or multi -wall
papersacks. Remove outer container and bury the cloth bagged
anode. If anode is supplied in plastic bag, remove plastic bag
before Installing.
5. Install anodes approximately two to three feet from the tank and
es
at least as deep as the center line of the tank. Anodes work bt
in locations with permanent moisture, so generally the deethe better. per
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.
an
10.Verify performance of the ode using an appropriate test
procedure.
I Connection Under Dome
1
i
2'-3' d
Cath dic Protection Testing Procedure
Equipment Nee ed: Digital Voltmeter, Red Test Lead Min.12' Long
& Black Lead 2' Long, Reference Electrode (Copper/Copper
Sulphate Half-C II)
STEP 1: Using a igital voltmeter insert the red test lead into the Volt
jack of the mete and select the 2 or 20 volt DC scale. Clip red test
lead connector an uncoated metallic area of the tank, preferably
to the fill pipe m Itivalve. A good solid connection is very important.
(DO NOT conne t to shroud).
STEP 2: Insertth black test lead into the Common jack on the meter,
and connect the opposite end of the lead to a charged reference
electrode ('A cell .
STEP 3: Remove protective cap from the porous plug at bottom end
of electrode. Pla a porous plug end into native soil (remove grass if
necessary) at fo r locations around the tank (one on each side of the
tank, and one at ach end of the tank). If difficulty is encountered
obtaining readln s, moisten soil with water or dig'/ cell deeper into
the soil.
STEP 4: Record II four meter readings on an appropriate form. The
least of all four r adings should be a minimum of-0.850v or more
negative. (Note: any of the four readings are below (less negative)
-0.850v then the ank is not fully protected).
CParging Reference Electrode
STEP 1: Unscre and remove porous plug end of new reference
electrode. Add eionized or distilled water to the copper sulfate
crystals, filling el ctrode completely. The solution will turn blue in
color and there s ould always be excess crystals at the bottom of
the tube. DO NO USE TAP WATER.
STEP 2: Replace rous plug end of electrode and place in an upright
Position so that a porous plug end Is facing in the down position
and let stand for hour before use. This will allow the porous plug
to become comp) tely saturated before use.
Caution' Do not a !ow electrode to contact oil, road salts, or other
substances that may contaminate the solution by absorption
through porous p g. Do not allow electrode to freeze.
Distributed By:
112011-500C
Job Name
Job Location
Engineer _
Approval
Dormont Supr-Safe®
Flexible Gas Appliance
Connectors
The tlexible connection between the gas supply and the gas inlet
of a Generac® Stationary outdoor EIackup/Standby Generator.
Features
• Operating Temperature -40°F to 1509F (,4oeC to 65.6•C)
• Operating Pressure MAX 0.5psi (3.45 kPa)
• Hydrostatic Burst Pressure MIN 250psl (1725 Wq
• Flexible Tube Material Annealed 304 Stainless Steel
• Flare Nut Material Carbon Steel with Zinc Trivalent
Flare Adapter Material Chromate Plating
Carbon Steel with Zinc Trivalent
Chromate Plating
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 exterlor use above ground for making
non-rigfd connections... between the gas supply and the gas inlet
of an appliance for outdoor installation that Is not frequently moved
Miter installation.' in addition section 1.5.4 states the connector is
designed for occasional movement after installation. Repeated bend-
ing, flexing or extreme vibration must be avoided. Normal opera_
lion of a clothes dryer, rooftop HVAC unit or SIMILAR 011i'Do0R
opera -
APPLIANCE DOES NOT constitute extreme vibration or movement.
ANSI 7-21.24/CSA 6.10 — Connectors for Gas Appliances
(Excluding 60/61 Series)
SR-
c us
Product Configurations
product asppAd W bothbolh E-"rptishesh
MEMME
All installations must completely comply with all Dormont manufacturing company warnings
and instructions, national, state and local codes and all applicable ansi standards.
Contractor
Approval
SKU
Applicable
ANSI Z223.1/Nf
International FIX
8149.1 — Natur
(GSA (
Uniform Mechan
Uniform Plumh,r
P.O, No.
ES-D-GAC Generator Generac
r*--_�
F
For use with Generac
l stationary outdoor backup/
standby generators.
Series 30, 40 and 60
'A 54 National Fuel Gas Code Section 9.6
Gas Code (IFGC) Section 411.1
Gas and Propane Installation Code
gyp) Section 6.21
rat Code (UMC) Section 1313.0
Code (UPC) Section 1212.0
Additional pprovals
Commonwealth f Massachusetts Board of State Examiners
of Plumbers and a Fitters
Additional ;"aryng
UL2200-2015: S Fsgine Generator Assemblies
Section 66B Vbr Test.
Meats, 7uoduct spe ifraaans in U.S. customary units and mebt are app¢ndmate and are provided for reference oaty. For P.,cim n
or malerrals vri prW robes and with Dormont rdser "the right to change or mo* product dedM �strucUM VW
a subsequanty sold. Haler to the ormcrb movat forh 4><mnati0a , �Oes arw moat+ an Oomwnt product' 1
CA
-1)6-rmont'
A WATTS Brand
Minimum Flow Capacity
at Specified Pressure Drop
(Straight Length BTU/hr. NATUOAL
GAS 0.64 SG, 1000 BTU/cu.fL)
Genarec Pan Nineber Dormont Part tYft6Er
,
SERFS Nomurol ID Nou"I Lwpth
OL4835A CAN30-3131-14GL
h m
30 %
OL4836A CM40-4141.146L
14
40
OL4838C 0AN60-8161-15%
14
60 1-%
15 1
(Straight Length BTU/hr. LP CiAS, 1.55 SG, 2500 BTU/cu.q
6enarac Part Number Dorinont Part Number
' ,
SERIES NDatina110 NgmbWLenplh
rmont Pad number
o Dnetu� 9 0 2.00 in w3ater column preeSsure drop to lyre g�a ator, ' BTU/hr,
D6fMon'
t...........
A VVMS Brand
ES-D-GAC_Generator Generac 1651
M 421a1437555001n00 42748.60050011
00 523715,52,50500rn00 538016.25,00000b00
74
I
32.6,000 200/
4g,00(803677.7.5
OOC
USA Tel: 800) 367-6668 • Fax: (724) 733-4808 •0ormont.cam Canada F. (905) 332-408o . Fees (goal 338-70N . Dormon! ctl
Latin America: Tat (52) 81 1001.6600 • F 52 -8000-7091 ( l Fax: 81 DorrronLcom
0 2016 Dormont
Ideal for use as a first stages regulator on any d0meailc size ASME or
DOT container in propane gas installations requiring up to 1,500,o00
BTU's per hour. The regulator Is factory set to reduce container �L
pressure to an intermediate pressure of approximately 10 PSIG.
LV3403TR -
LV3403TRVg Y" F NPT�VkNP7 �fu" 7%,w7,,,,
10 PSIG500,000
kAexnum flow Eased O11 inlet Pnsoure 20 PSIG htghcr than iha theregulatorsetting end delivery Prca3ure 20% lower than the sellir g• Sew °ad dakvery preyaurc Zt)
Provides accurate first stage regulation in two -stage bulk tank
systems. Reduce tank pressure to an Intermediate pressure of 5 to 10
PSIG. Also used to supply high pressure burners for applications like 9L
Industrial furnaces or boilers. Also Incorporated In multiple cylinder
Installations.
LV4403SR4 r4 % .
F
' t
••.
LV4403TR4 NPT
5
1-5
LV4403sR9
1/2• F
NPT
10
5-10
LV4403TR9
Y.
5
1-5
LV',6033R90 F POL
10 t
5 90 Yes 2,500,000
I-V4403TR96
3' "
F.NPT
5
1-5
' When used for final stage
with NFPA Pamphlet 5& pressure
10 5 10
control, must either Incorporate integral slier valve or
" Maxlm,m flow based on Inlet
aoparwo rclisr valva should bo �� � 800D1d11Op
Pressure
20 PSIG hi
higher gran the regulator
aetdng
and deliverypn#sWe
20% bwar than th sating.
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.
LV440384
%"
LV..403846 '/" F. NPT
LV4403846R' #28 11' w.c. at
Drill 10 PSIG 9" to 13' Over Inlet
LV4403H36 '�' F. NPT Inlet W.C.
L1r4403366R` a4" F. NPT
eackmount design
fdeximum flow based on 10 PSIG intct and 9' w c. delivery
LV3403TH
LV4403Sei ies
iLV44W]3S=Ies
n
100 Rego Dr. Ekx:, NC 27244 USA www.reg0pr0duetLGw1, +1 (336) 449-7707 1 '+` {,_,�•• f`• ~
Ass a m g
I
.ta
on'."mianig.) oao,
mv
B
( se".,
-Ole 'o-
STC-P :t
Verify the polyethylene
(PE) pipe being
assembled Is the
correct size.
S7r'P 2
Cut pipe ends square.
Iris s
earl piping thoroughly
assure there is no
t grease or oil in
Sembly area.
P4
mfer end of pipe
g Continental's
nfering tool with I.D.
fe.
Patent 4s 8.366,26e,5,692,785 & 5,853,272
Ph: 1.800.662.0208 o Fax: 615.325.9407 o Wab: www.gclstife.com
87i.p 5
Mark the stab depth by
Inserting the pipe into
the chamfer tool and
marking the pipe at the
entrance as shown.
ae%S� C
if using chamfer tool
t i wiih ID gauge, check
for proper chamfer by
Inserting pipe over
gauge.
876P 7
Stab pipe completely
Into filling entrance.
.w
STC
L' Stab pipe completely
,. Into filling so that the
mark on the pipe is
Within 1/8" from the
rifting entrance.
STEP
Repeat steps T Lough 4 for all Con -Stab 10Infs.
07FP 10
To assure prop r assembly and to
CFR 1comply With 49
92 Subp it J-Test requirements, the joint shall
be leak tested.
Ma„Imum 111 C, Gas
of PE pipe to Thousands of BTU per H ur of Uquetied Petroleum Gas
wifil a Gas Pressure of 11.0 Ira, WCand a Pressor Drop of OS d Petroleum
(based on a l.52 spectBc arovliv ...
1391 1073
720
571
484
425
383
56
45
41
3�_g "
. ,
1983
934
1331
740
18
627
551
497
325
421
286
370
257
218
35
204
33
192
3563
2391
1894
893
1605
786
1412
708
600
528
333
475
305
305
435
283
264
249
4724
10063
3247
26p8
2232
1978
1272
1792
948
854
781
403
723
376
354
6755
5361
4535
3989
3592
1534
3044
1359
1232
1133
1054
989
989
636
934
2678
2411
2207
2044
1970
7797
169 152
219 197
371 280
560 504
828 750
1561 1424
- 129
`
15 13 � 1ame1 'I° °
1 ]3 102 76 10 9
86
+rr
r
9
167
238
147 68 63 58 54
132 112 99 gq
8 8
8
7!'d°
7
427
S1 75
376 188 160 140 126 111 15 70
338
44
66 63 46 57
60 57
4P
40
642
.1207
252
287 227 208 192 180
569 516 441 391
94 89
169 160 85 81
78
78
52
75
.
354
1061 966 810 326 303 285
712 642 687
269 152 146
255 244
140
134
544 508
Maximum Capaclty of PC pipe
233
478 453 431 411
224
3IT
216
379
In Thousands of BTU per Hou of Uquefied
with a Gas Pressure of 2.0
25168TUh=1CFH
psi and a Pressure
Petroleum Gas
(based on a 1.52 specific
rop of 1.0 psi
gravity gas)
1966
1319 1046
8 ' 779
°
-
11300
14652
7586 702 595 523 7
6008 5092 4479 4033 3418 3007 471
9835 7790
i° 17
43) 399 373 351
j
20877
6602 5807 5229 2707
14014 17100 9408 8275 4432 3898 3510
2478 2296 2144 2018
213
1709
1599
37514
43429
25183 19946 16905 127.5 1451 1633 5
29846 82
2975 2780 2617
578 4239 3962 3729
2302
2073
105963
95
89882
23969 20515 18182 16474 14100 12496 11322
71131 56339 47750
226 7618 7119 6700
3280
5894
2953
42000 37820 3205q 28194 25388
0417 9691 9092 8689
3234
7612
5307
6897
236
° °j 11 �°
21517 20108 18926
16647
14990
7355
207 187 158 i1
739
1192 1073 125 1)S 106 qq
910 800
f1
93
1757
2503
1545 720 659 611
1391 1179 1037 934 571508
88 841 80s
77r
t1
74
4498
2202 )983 1680 1478 1331 12 g 1792 1 $ 740
3956 3563 3019 1054
96 659 484 462
627 599
443
574
425
8%3
12705
5232 4740 4057 2656 2391 2189 2027 1894
3596 3258
2 939 893 853
1
1347
818
551
786
11175
10063 2997 2788
8529 7502 6755 6182 2W
1605 1533
71
71 2347 2239
1469
1412
5725 5350
Maximun') Capaolty
4767 4 2144
2060
1985
3988
or PE Plpe in Thousands of BTU per Hour t U ue6ed Petroleum Gas 13TU
With a Gas Pressure of 10.0 Psi and a Pressure pr q 2516BTur,�1CFH
n a 1.52 specific gravity gas)
p OI 7.0 psi
C410
1662
131— 6
1� 1' j6
9"
981
�
1
14234
18485
9555
12388
7568
6414
884
5080
749
4306
659
593
26296
9872
8316
7315
6587
5964
3787
4910
4422
4
47252
63960
31720
37087
25723
21293
18729
19385
6865
7954
14294
6997
6300
133476
89601
29782
70967
25489
60748
4bg0
175191�76
12572
11321
68
70
`
52905
- —
.--�
35527
31980
12
1707
-
3153
5665
7334
16004
1501 1352
1946 1753
2773 2497
4983 4487
(500 ' ' $t390 '
14077 12676
1146
1486
2116
38
SO4i
10743
1008
1306
1862
4468
9449
158
907
1176
1676
4048
8509
- 144
830
1077
1534
3724
7787
�134 125-
769 125
712
1421 1328
2553 ...2386. _
3465 3251
7212 6739
Ph: 1-800.662.0208
• Fax:615.325.9407
• Web: www,gastite.com
r 2890
2701
2542
2236
°�
2014
F:
3747
y 11340
3502
4990
3296
2899
2611
t 'i
1 9595
3
8967
4697
8440
4131
7423
3720
6685".4
1
12041
' 27104
11297
25329
10671
9458
FF
23840
20970
T888
FFf'
rt
!^�
0
609
582
557
596
�
83
830
1183
790
754
723
69S
2726
7125 1075
2022 - - 1931- -
1030
-1851-
q90
2916
6005
2782
5712
2664
2560
• 1779
2466
& -I
6465
5227
502q
i
2516BTUh=1CFH
I
l.,�