HomeMy WebLinkAboutGAS PIPING SCHEMATICSCANNED
BY
•
BOARD OF
COUNTY.
COMMISSIONERS
i
GAS PIPING SCHEMATIC
i
[Al] [A3] ; [A5]
TANK SIZE: p CJ GALS.
APPLICANCE — TYPE/SIZE
Al 02 merzL.k.,c,f
A2
A3
A4
A5
A6
35S ; o o D BTU
BTU
1 BTU
I BTU
BTU
BTU
PIPING LENGTH & SIZE
L1 50 FT.
���I INCH DIA,,
12
FT.
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.
PLANNING & DEVELOPMENT
SERVICES DEPARTMENT
Building and Code Regulation
Division
RECEIVED
MAY 10 2018
ST. Lucie County, Permitting
(PIPE SIZE WAS TAKEN FROM
THE 2D4,4FBC FUEL GAS CODE—
Website: www.stiucieco.aov
2300 Virginia Avenue - Fort Pierce, FL. 34982-5652
Phone (772) 462-1553 FAX (772) 462-1578
Revised 7122/14
a .
=RECEIVED
: . � a� � � •, �
FILE COPY
.a
ST. LUCIE COUNTY —°
BUILDING DIVISION
REVIEWrl- �.
FOR COldli� G nl
REVIEWED BY
DATE ' f _ —
'' PLANS AND PERMIT
MUST BE KEPT ON J013 OR
Z a j NO INSPECTION'VILL BE MADE
i
1 '
Maximum Capacity of
ImIth a Geis Pr
y1: 1 1-u 11'. m; and a pressure prop of 0,6 in. �rC 1eum C-as
(based on a 1.62 specific rout
9 ty gas)
04 74 67 • T 56or
ae•.45'1� 41 3: 81073 720571 484 425 383 325 286 257 e 3• 6a 3°3 m
354
29
1391 934 740 627 56497 0 261983 1331 1054893 1 .333 305 192 169 1523563 2391 78708 600 283 264 249 219 197894 1605 1412 1272 1078 528 47 435 403 3764724 3247 1948 311 280
232 10063 6755 6351 435 2 1534 1369 1232 81 723 76636 804989 3592 S044 1054 9828 7501 2207 204934
4 797 1581 1424
1010
20 .Om a
11,° ° m 129 113 10 9 9B7668 m
a a s a o
167 147 l32 112 99I 89 81 58 64 61 48 8 8 7 7
238 249 13 75 70 42 qq q2 40
238 760 140 726 116 107 10o q 863 9 b0 67 54 52
376 338 287 252 227 208 85 642 669 516 441 391 192 180 169 160 81 78 75
1207 1061 956 810 7 654 326 303 286 269 255 162 146 140 134
12 642 587 544 508 478 244 233 224 216
463 431 417 394 379
Maximum Capacity city Pipe in Thousancis of BTU per Flour of Liquefier Petroleum Gas
with a Gas Pressure of 2.0 psi and a Pressure Drop of 1.0 psi 251687Uh_)CFti
(based on a 1 x2 specific gravity gas)
3962 1319. 1045
2]1041°3� 00 9785o38bmm 886 779 702 69o05 • 523
• 4.°16008 5092 44791033 3418 74' 399 373 361
s
3007
309707 2478 22927,85 7796 6602 68071 2Q18 1775 1592953
9877 74014 3898 3510 321382757461 6315 2975 278037514 25183 19946 16905 02 4678 4233962 2617 230 2073 13389 11348 372943429 8 23969 20615 1818 3105963 71131 474 14100 12496 7618 7119 3729 689450747750 4237820 82084 28194 11210417 9691 8689 7612 689738 23234 21617 20108 18926 16647 14990
11100 9408 9092 236 m� .mm as :aa aam
207 187 158 139 125 •ae ao am
]355 1192 1073 175 106 99 93 10 '°
1355 1192 107 l9 0 .1037 72 855 611 571 88 e4 80 77 74
2503 2202537 6D8 484 462 443 425
4498 3956 3563 019 2476 1831 1218 1128 1054 992 939 62 59
5903 3962 3563 90 7 2656 2391 2189 2027 1894 1783 1688 1606 1533 1818 78
5903 6232 -07-00 8529 3596 3288 2997 2788 818 786
127D5 1117b 10063 8529 7502 6755 6182 2788 2616 2471 2347 2239 069 1985
630 2131 2060 ]985 5036 4767 4535 4331 4150 3988
MOXirnum Cappcify of PE pipe In 11`lousands of BTU per Hour of Liquefied Pefroleum Gas
with p Gas Pressure of 10.0 PSI and a Pressure prop of 1.0 psi 2516BTUha1CFH
(based on a 1.62 specl6o gravity gam)
2476 ° ° ' •
]6b2 1316 1116 981 884
74234 9556 749 659 '� •0 ' '
7568 6414 6642 6080 4306 3787 3410 3121 2 90 270503 0 2�42 ,
18455 12388 9812 8316 7315 6687 642 389 360.
26296 17652 13981 11849 10423 9385 7954 2997 630D .2476 5340 4990 . 4606 2236 2014
47252 31720 26123 21293 18729 1'6866 14294 12572 11321 10361 3747 3592 697 2899 2611
53960 37087 29782 25489 22591 20469 17519 16527 14068 12943 1959s2D41 18967 84401 9458 4131 3729
133476 89601 70967 60148 82905 47640 7423 6b86
40376 3Sb]4 31980 29267 27104 25329 23671 8569
mm ° • o . 20970 18882
297 261 235 mm OA .ma as :gym
199 175 ..5$ T44 134 •�� �mm
1707 1801 1362 1746 1008 126 118 111 106 ]
2213 3962 1763 1485 130b 907 830 769 719 676 101 97 93
1176 1077 997 640 609 682 557 536
3163 2773 2497 2116 1862- 1676 1534 1421 1328 1250 1183 1126 2975
5665 4983 4487 3803 3346 3012 2757 2553 1328 830 790 754 723 695
7334 6500 6890 6041 4468 2246 2126 2022 1931 2997 g90
16004 14077 1267b 30743 5665 8509 7787 7212 6739 6343 2975 5712 5665 1561 2476
4048 3724 3465 3251 3077 2916 2782 2664 2551 2476
5227 6024
Ph: 1,800.662.0208 • Fax: 615.325.9407 Web: 4yyyyy,gpstlte.co111 2616BTUh=1CFH
7
1-u%'m I IVIV MAT-'
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an
THE NORTH 100 FEET OF THE FOLLOWING DESCRIBED PROPERTY, LYING EAST OF F.E.C, RAILWAY: COMMENCE AT A
POINT WHERE THE SOUTH LINE OF GOVERNMENT LOT 1, SECTION 12, TOWNSHIP 36 SOUTH, RANGE 40 EAST, ST, F'"-/-22,
LUCIE COUNTY, T 1, FO EAST NTERSECTS THE INDIAN RIVER; THENCE GO WEST ALONG THE SOUTH LINE OF SAID GOVERNMENT LOT 1, FOR R; T FEET; THENCE GO NORTH 485.76 FEET; THENCE GO EAST 1,749LESS, TO THE INDIAN RIVER; THENCE IN A SOUTHEASTERLY DIRECTION MEANDERING THE SHORE OF THE INDIAN
RIVER TO POINT OF BEGINNING. EXCEPT, HO FEET, MORE ORWEVER. RIGHT OF WAY FOR SOUTH INDIAN RIVERDRIVE,
LEGAL DESCRIPnnm
tm .• t r
S. •mt
4 all t
ieim! �•,
¢11' i ¢n• e
\ Wg
ROMANELLO ESTATES � \
..¢patio \
E 768.:
na,
7Y:.' 1
ei \ NI �� - - --- ;.m'C • aapr ^�4 r r.at.lr
a
UNPLATTED �p "' m SB ' 1_'33'W "" • a' 77Z
UNPLATTED 4
U
_ • ' ld,M ltK V (anal[41 t!» 1 — —
aW'tm n 1M.—,
�4ttw naen •n w.wne
` I 89'01'33-E 75'
�� •�_: txp per, _
89'S1'33'W 74'
p nn.
�J VI
t. QCIJ
c d
J )�
PAUL
nu=c roc p.t uta, .atr"ea"'it a w tome nwa °' �y„n • .a ew _
tm �� m �¢tw't'0ro tat _. m „� e. c a'm'n p,'�i • e.r o � � ua �°'au. e'a'wn's a>rm",°ie.e"`°"a
v pa,tt✓p d c¢'tm V tem.o tNntp 'O1,mei ='
nn
gyp' ptw44n c,o mn°�pat � ' ,ume4m p im�iu"rirs+tvr.x"inv. °A ocew�m'wri .tc'0Ct =r na°�mtr � 'OL'Scm !m � ¢uwup .M � t.� alo®, ,u01W p . G Nretu Yt h _� V Q,OII mpM
CUp /a=I -,•,� U•...0 u¢,ta rR iN,p. •,p, �� .r,ft.-14q 114 M �rRt
¢l O,u,r,4Q top '•�'vfie' aM �., pN�Y[ 4¢n,r IMalygq Ni p v ,y „�, II peal U,man
Na OtnQ¢ 4¢ ItY U[N taip ap N� 4N•Wq p �tpwp Wv 9,l¢na
1. PROPERTY ADDRESS: 6401 S. INDIAN RIVER DRIVE
Z CER71FIED T0:
— TERRY L. & KAREN E. HEIZLER
— FIRST AMERICAN TITLE INSURANCE COMPANY
— FIRST INTERNATIONAL TITLE, INC.
— ACOPIA, LLC, ITS SUCCESSORS &/OR
ASSIGNS, AS THEIR INTEREST MAY APPEAR
,e.p 4p..no
t•m
u auwt tw¢
t,c
wvtielt. Irp pn,[pv
� aCetptd,t lit
Yee
�'� syq W WVNt t4i
�, d � 'ntt001 wawa w
VALIDNOT WITHOUT 1SIGNATURE
ORIGINALRAISED SEAL OF AFLORIDA LICENSED
SURVEYOR AND MAPPER,
STEPHEN J. BROWN, INC
STEPHEN J. PRO SSIONAL SURVEYOR AND MAPPER
REGSTRA ON NO 4049. STATE OF FLORIDA
Dots of field surve.y
w rtn 1. ....•,..
GRAPHIC SCALE
1 �I tptap"'n � t+p.011 p
TUC
I loth = 40 tL
NOTES:
L Surrey of destrfption as furnished by Client.
2. Londs shorn hereon trcre not abslroctcd for cosomanis andl_
rfghls-of-way o! record.
J, is bearings are referenced la the South line of lfamandto Estate; plolfe0
as 5895133'W, all olhgm rdot;,. Ihcralo.
4. Etemlions shown hereon are relafim to North American Vertical
Datum of i988, and are based on bench mark _ltJg.
ra !here ara no obove ground encroochmcnts,
P.lanteerrdse s
6. e ficumar flood insurance Pregrom doslgnotfons osofh;nd�colwshonown.
the F.EM.A. Atop No._I2111 .0292
do(ca 02 rtf.: 201n IneWas the parcel in 7nne •i, base flood Nemlion N r to any scaling ono inlarnalat;on ieclws ossaewlea pith rt o feel; suhjecl
actatrnr. P. t;s data is an fat refatlon A fhe 1--sur.- pp;ng of Ih.:
ys Unde urles , The flood :on ) should by
verified by a dete m inclfon to
Y
rgrauna rouncal;ons & ufgilles na1 located unless sllotrn. gaol'
' � �ti yft'"Ff� 4 .'1'`'y .fi=:''_....s.z. �v�,� ' " r�''. m'"'4'+^r�k•",pe"T"r^v+n �,. ""^+-•^-->st-Y..._..�„
g �-c � j �}asl Ef � � � � 1 j - _" "'s�-•c.ti�r:......•-i.si,.{ � k,�s ".� p ,
`: d tr,4 �5s X•S±r UjijIt.- �� �: �, �Ol.��Y ' �{j�jp•,,� �� LIE,
c
r � f ray i' i :4. 3 �„'. .,R.'r °; z � rn - '. -'•.
s�.u�sr^�•,.�.�-'�s"''.''>'�,i'`ar '� rY�' t� i T �,� �(, � r a �r ��?�iN[
'�� �) � ��! � t I' � ro- ".:,. •'" �'K .+ . a,. � lief { .p o-i.fel. I� -� ° ., r, ' s � : ,
,i `•=�_. �i _ o ��1���"i i f; F'� c..Ae�. S L � I"' S � � f �� � ••
t . 'Ki' ,. OR?
�F �,Y� .,�iy`.^•,M r � ,
t ? x �. Q11,eC111VO �Sup�r�Dur�ab a °opcoat x
! It(1 C G Rtithl LAW , � /O�� /�►��`1r w
fiOR1]a,U@E�
l�rar1,H)
L _
A QG[ZtnTivo soaisY fe
dotlirup
e Ill •� ,Y11Gir,G11
biac{c? 1 t` io>i�uiptrner i '
,t? asttc.or=wh`I�te
galvar�i•-. 1 -
zed steef fi" !i? w1���etiopcolth fix;;°.
a5llpt�Gtorvrari'd�[otl l [1 a
r §epatet�ft�at�tu '
t�atelil�pend�tng
"'=-�— - ,.z�_ �,,�• , �.. st tt ted p4tn t:�i n�! � �
--e---+.va.-..�,...._.�- 1.--u. - _ 'y'' �`.':^ {w.y. 2 N C. F - Ft•:;k
• Dual service options for above or underground applications~
• Option-1i•7; Ready -to -bur o Y re d ' oxide 'de
durable powder coating with black
All-
r t • polyethylene AGUG dome'
Option ,,2i Aboveground option with steel 8" AGUG dome
•All valves and float gaugesare centered under dome
<: �; • Fabricated to the latest A.S.M.E. Code, Section VIII,°Division 1
" • Registered• with the National Board
�' r.�. ' • 1172 liquid -level outage valve orifice reduces -refueling emissions it I ?fi IT
Y
VaCUUir1 pre -(]Urged to savetime;money and product
.. kva�y�its, 11�M1 � 'ApplicahIe'rr deral, state, orlocal'regulations may contain specific requirements for
Containing protective coatings and cathodic protection. The purchaser and installer are responsible
• • for• compliance with all federal, state, local and NFPA industry re_nutatit can,ocric
t Protection rm0required and coating must be continuous and uninterrupted and must
i comply with!an local, state nr national code.
www:TlinityContainers.com Call Toll Free; 888-558-8265 I
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General S ecifications
Conforms to the latest edition Of the ASME code for
Pressure Vessels, Section Vill, Division 1. Complies with
NFPA 58,
Rated at 250 prig from -20" F to 125° F. All tanks maybe
evacuated to a full (14.7 psi) vacuum,
Vessel Finish: Coated with epoxy red powder,
With the epoxy powder must be buried). ForAboeTanks
ound use,
tee '
Tanks maybe coated with TGIC powder.
Applicable federal, state or local regulations may containI
specific requirements for protective coatings and cathodic
Protection, The purchaser and installer are responsible for
compliance with all federal, state or local regulations,
i
WATER OUTSIDE
CAPACITY DIAMETER
120 wg,
464.2 L
2— 50
141.8
320 wg.
1211,2 L
500 wg.
1892.5 L
1D00 g
3785.0 L
24"
609.6 mm
31.5"
80--- =1-mm
31.5°
800.1 mm
3 mm
I'll.,
505-m-- m .
40,96"
1040.4 mm
AGUG VESSEL D fMENS,
proximate
HEAD
OVERALL.
LENGTH
OVERALL
HEIGHT
Rip
5' - 6 13/16"
31 0„
1671.3mm
911.4 mm
Hemi
T-2112"
."
31-7711211
2197,1 mm
1104.9- mm
Hem!
8' -11 3/4"
3' - 7 1121,
2736,9 mm
1104.9 mm
Hemt
91.1011
4' -1 7~ /�~
2997,2 mm
1266.7 mm
Hemi 18'
-10 13/16"
4' - 4 5/16"
4846.E mm
1344.6 mm
FLOAT ,' r OTiCE, WIT
AI VERAWAL
eAuoE LF. US
ANODE
CONNECTION
O �I VALVE
SERVICE / O /
MULTIVALVE
RELIEF "—"�'
PLATE
VALVE
FITTINGS LAYOUT UNDER DOME
NAL INFORMATION
LEG LEG
WIDTH SPACING WEIGHT.
10 1/8"
26---7'2 mm
12 3/4"
32---3m
12 3/41,
32— 3�m
15"
381.0 mm
18
412.8 mm
3'_oil
914.4 mm
3' , 611
106---.—mm
V
4' - 0 1/41,
122--,-5_6 mm
152— m
9'-0"
27'43.2 mm
245 Ibs,
11-- 1-
472 lbs.
214—
588 Ibs,
266---'7 kg:
871 Ibs.
395.1 kg
1729 Ibs.
784.3 ka
QUANrITY
F� U_�
PER
LOAD
STACK
96
12
63
g
45
g
30 .6 —
16 5
Rev; Jan, 27, 2016
Why Tanks Corrode I
Underground steel tanks corrode due to an electrochemical reactiol
between the tank and the surrounding soil. The process of corr sjor
occurs due to small voltage differences on the steel surface that result
In the -flow of DC current from one location to another. Whore t current
flows from the tank into the soil corrosion occurs. This location Is call
the anode !n a corrosoon circuit. Where current flows from the s ent
tank, no corrosion occurs. The: called
the amount of current flowing between the anode and the Cathoion is de
determined by
whether the locations of the anode/ cathode remain constant over time
Corrosion rates are generally higher In wet soil environme athode and
conductivity of the soli .,
e th
circuit, promotes the
flow of DC current in the corrosion I
Corrosion generally exhibits itself on underground tanks in et
general overall rusting or more commonly, a pitting attack. Pit loc
may result from metallurgical conditions of the steel surface they a
variations such as rocks, salts, fertilizer, moisture concentration o arsons
concentration, etc, or soil
. xygen
Preventing Corrosion
Protecting underground
tanks from corrosion is
easily achieved bytha use
Of two commonly applied
Protection methods:
.external coating and
cathodic protection.
These two methods
are complementary and should be used in Application Recommendations
:onjunctlon with the Magnesium anodes can protect underground tanks !n most ►they. An effective conditions, The H-1 alloy is generally very effective. The following chart
oaring Insulates the steel from the soil environment thus Preventing st soil
external Protective providessizeandquantltyrecommendationsforvarioussizetanksbase
1eflowofcorrosion currentfrom the soil
the cathode. An effective on conservative design assumptions,
�temalcoating can protectover99%Ofthetanksurfacearea. Howeve9 up to 10,000 ohm -centimeter resistivity. d
P This chart covers soil conditions
coating is perfect, Damage from construction or soil stresses create 10,000 ohm -centimeter generally represent Verydry
iy defects, which may result in accelerated c Resist(vities higher than
Of soli resistivity can be performed through soil analysis. Contact us
for design recommendations inlocations where sa soils. Verification
corrosion at the defect. 10,000 ohm -cm, or if there is no effective eater
thodlc protection prevents corrosion at those defects b I reslstion the
exceed
current from an external source, forcing the tank to become ,� nai coating on the tank.
y applying The propane service line from the tank to the house.ais
hour. Application of sufficient DC current to the tank will prevent any
Tosion from Occurring. considered in the cathodic protection design, unless the service line
g The two general Is plastic. All underground steel pipe should be external) o must be
terns are sacrificial and Impressed current Sac if(clalsystems protection
a corrosion resistant material. The service line should be electrically
When the amount of current required for the protection is small, � y coated with
isolated at the house with an insulating fitting or union. If service i y
h as in underground propane tanks. Impressed current systems
is less than 50 in length, the tank anodes will provide sufficient current
more commonly used for large structures such as current
arge diameter pipe
to protect both tank and pipe. For longer lengths of pipe, an additional
lines. Electrical Isolation of the tank from metallic piping systems
electrical grounds is critical for the cathodlc protections systems anode may be required at the house connections.
tiveness, if another metallic material such as co the pipe should be electrically isolated prom he dtan�k service fl11 pipe
Sacrificial Cathodic Protection Works connection. Copper and steel create a galvanic sou le li
1ficial systems work by creating a galvanic connection between two
corrosion of the steel tank when directly connected t that
pip piping.
Generally, copper piping does not require cathodic protection.
different metals. The most common -anode material is magnesiu
Which when coupled to steel results 'in. DC current flow from t
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, g rcuit
two metals together, the difference of i to 1.25V volts results in
y connecting the
flow to the tank that overcomes the natural corrosion cells that exist current
the tank. With this current available to the tank, no corrosion occu S
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
Nigh potential. The H-1 alloy is produced from recycled magnesiu
and has an open circuit potential of approximates _ AZne and
is well suited for protection of underground Propane y 1.55V, m
Potential alloy is 99% pure magnesium having an open circuitThis alloy
A pane tanks. The High
Dh to m re This alloy should be used for soli applications avep10,Ma
ohm -cm resistivity
the two most common anode sizes used for underground propane
tanks are 91b, and 171b. The size designation relates to the m
10' of 012 TW insulated wire Is attached to the anodes. eta) weight
then backfllled (n a mixture of Anodes are
to lower the electrical resistance of the anode totso In Thedmixtureissulfate
low cost, nonhazardous, electrically conductive backfill. The an re is a
bacol► is then packaged In a cotton ba ode and
paper',bag, Actual shipping weight of he a anodes with bacrd box or
lb. and, 45 lb, kfill is 27
sort type
Fertile $olis, Clay,
Sandy Loam
Gravel, Rocky
tank Cap.
foal.
5 to 5000 ohm•om
Areas
5000 to 10000 ohm -pn,
120
size Qty, Alloy
g#
Slze
Q1Y• Alloy
150
1
9# 1 H-1
H`1
9#
1
250
325
9#
9# 1
9
50o
H-1
i7# 1 H-1
9#..
2
1000
1600
17# 2
17# 2 H-1
9#
2 H-1
4 H-1
2000
17# 3 H-1
9#
4 H-1
'Based on 90% effective external coatin p m s H-1
yearRnode life. 9. alft2 current dens/ty, and 30-
Anode Installation
1. D When
a 1 size' and quantity of anodes from applicatlo
2. When a single anode is installed, It should be located near the
tank center on either side of tank. n chart.
3. When multiple anodes are installed, space them
the tank, See examples below. evenly around
1 anode
2 anodes 4 anodes
.Anodes are shipped in either cardboard boxes or multi -
node. acks. 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
at least as deep as the center line oft
f the tank.
In locations with permanent moisture, so Anodes work best
the better, generally the deeper
6-After placing the anode, stretch out th
and extend over e anode connection wire
7to a connection point on the tank fill pipe,
.Cover the anode with approximately six inches of backfiil and
Pour 5 gallons of water on the anode to saturate the prepared
bacicfill. Water Is necessary to activate the anode,
8. Connect the anode wire to the tank with a row electrical
resistance connection action. Examples are threaded stud on the
tank fill pipe or any accessible metallic connection
tank. All connections should be coated vulth a moisture -proof
material. Point to the
9.ldeal(y, the tank connection Is made in the area of the rank fill
PIA, within the IS dome. With access to the anode wire,
subsequent testing of the tank can Include measurement of
anode output and verification of performance.
).Verify performance of the anode using an appropriate test
Procedure , J
Mechanical Connection Under porn,
Cathodic Protection Testing Procedure
Equipment Needed: Digital Voltmeter Red Test Lead Min.12' Lo
& Black .Lead Min. 2' Lon
Sulphate Half-Celi) . g� Reference Electrode (Copper/Co ng
PPer
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 ve
(DO NOT connect to shroud), i
STEP 2: Insert the black test lead Into t ry 1mP°rtant
and connect the opposite end: of the lead to a cMon harged ged t efere ter,
electrode (% cell).
�STEP 3: Remove nce
of electrode. Place porous plug and into natIve s Plug
necessa P g at bottom end
►Y) at four locations around the tank (one oin�ea h sidremove e of the
tank, and one at each end of the tank),
If obtaining readings, moisten soil with water or t11g IY cell Is encountered
-the soil.
STEP 4: Record all four meter readings on an appropriateper into
least of all four readings should be a minimum of-0,850v o
negative. {Note: if any ofthe four readings are belowform, The
-0.850v then the tank is not fully protected}, r more
(less negative)
Charging Reference Electrode
STEP 9,: Unscrew and remove electrode. Add deionized or distilledswalt r to Chef copper reference
crystals,lfflling electrode completely. The solution will turn btu
color and there should always be excess crystals at the bo sulfate
the tube. IDO NOT a in
8TEP2: ` USE TAP WATgR, ttom of
Replace porous plug and 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
to become completely saturated before use.
Caution: Do got allow efeetroffe to contact ell, road $alts porous plug
substances that may contaminate the solution
through porous plug, pe not allow electrode to /ree4e. " r other
by ahsorptloA
Distributed By.
11na».S000
Idea( .for use as a first stage regulator on an! diinstallations requlr(ng up to 1,500,000 BT a per
pressure to an Intermediate pressure of aoornvt.
�u•�3�IrBo�� aala�®c�uu��:na��a
t.V3403 i 1?<<9 '/411 F NPT' %" fi N P T 7132Il
Maximum flow based on etlfng and delivery pressure
INao pressure 2p P higher Ihen the
a20/0 lowar than the sang,
Elp
Provides accurate first stage regulation In two.
siege
Intermediate
tote pressure of 5 to 10 PSIG. Also used to e
industrial furnaces or boilers. Also inrs,.nn�
t!o size ASM! or OCT
The regulator Is factory in propane gas
10 PSIG. 4' sat to reduce container
10 PSIG 11 Over Outlet
9;00 11500,000
rterselling and delivery pressure 20% lower than the regulator
I'
Installations, =rwluaitons like
when used for Posh 88. aIle
With NFPq pamphlet pleasure control, muel either Incorporate integral1O 5-
valve OF
" Maximum flow based on Intel pressure 20 P810 higher than Iha regule(oi se IUIg and delivery roller valve should be spacifled 1n accordance
® a � ry pressure Pacified
lower then the selling.
Designed to reduce flrststage pressure of 5 to 20 PSIG down
Ideal for medium commercial Installations,
Dirdernuatg Burogotrmultiple cylinder insioaaai o�ti�
--
on 10 PSIG inlet end g' 1yo, dallverypmSoUle.
r pressure, normally 11" w,c.
and normal domestic loads,
e LV3403BR Back Mount Regulator is designed to reduce first stagure o a
to
burner pressure ,1 p normally 11 w c. Designed designed
a second stage regulator for smaller a
requirements up to 50,000 BTU/hr, and ere ideal for homes 10 PSIG down w
�4•c�9C>;'tirrd ,mobile homes, and cottages, toatlons with flow
Maximum ROW based on 10 PSIG inlet and 9" r'SiG inlet
i W c, delivery pressure.