HomeMy WebLinkAboutGAS PIPING PAPERWORKBOARD OF
COUNTY
COMMISSIONERS
UCOUNT
T.CI°Ev-„-
GAS PIPING SCHEMATIC
Division
SCANNED
BY
St. Lucie County
OR NO INSPECTION WILL BE MADE,dOB
TANK SIZE: 500 GALS.
APPLICANCE - TYPE/SIZE
Al-rcmcless W&wNe�+err 180�000 BTU AS (3ba (0,000
A2 ricq e- 35, 000 BTU
A3 C-xi L,o6+ 70' 000 BTU
A4 S1-eye� (eSr Ooa BTU
A5 L,as L;oln� ZD+000 BTU
A6 TonklesS UAw Ne.�tr /80,000 BTU
Al Or4e,r _ 35.00fl g-ru
PIPING LENGTH & SIZE (PIPE SIZE WAS TAKEN FROM
L1 3 o T. l INCH DIA. THE 2014 FBCFUEL GAS CODE -
L2 S FT. 3/4 INCH DIA. TABLE 402 (_ J)
L3 zo FT.
3/4
INCH DIA.
L4 / O FT.
3/4-
INCH DIA.
L5 2�S FT.
3/4
INCH DIA.
L6 Ce FT.
3/4 INCH DIA.
L7 3o FT.
3�
INCH DIA.
L8 / O FT.
3/4
INCH DIA.
L9 30 FT.
2Z-,�--INCH
DIA.
L10 G FT.
3/�
INCH DIA.
L11 1 ':� FT.
34-
INCH DIA.
------L-12-1 o FT.-----�
INC-H--DIA:----- -
L13 Zl FT.
Lt-
Wesite:wwws8ucieco.aov
2300 Virginia Avenue - Fart Pierce, FL
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34982-5552
L. 11} / U F'�. Phone (772) 482-1553 FAX (772) 482-1576
Revised7/22/14 2 INLN DIA-
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SITE PLAN
PUA2
i M.
■ Corrugated stainless steel tubing (CSST) gas piping systems will be bonded
in accordance with Section G2411.1 (310) of the Florida Building Code and
NFPA 54.
■ Underground gas piping will be installed at a minimum depth of 12 inches
below grade in accordance with Section G2415.12 (404.12) of the Florida
Building Code and NFPA 58.
■ Polyethylene pipe will be installed in accordance with 6.11.4 of NFPA 58
and the Florida Building Code.
Carbon monoxide monitors will be installed prior to inspection and will
meet all code and safety requirements of NFPA 54 and the Florida Building
Code.
Application Materials
.................I....:...... Ideal
—
Ideal for use as a first stage regulator on any domestic size ASME or Body ........................ -•r .-•-•••-•.--• .••••• Zinc
DOT container in propane gas installations requiring up to 1,500,000 Bonnet ...... .............. .••-•-•-••• •• """""'•....................... , ,,.Steel
BTU's per hour. The regulator is factory set to reduce container Spring ,,,•..................•-�-^•--••-•--•"""""""""".......................
"••Resitieni Rubber
pressure to an intermediate pressure of approximately 10 PSIG. Seat Disc-: .............••• -.,^.-Integrated Fabric and Synthetic Rubber
Diaphragm ........................
Features
Compact design can be connected to a service valve using either
a POL adapter or a Rego product pigtail.
Large threadedY." 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 Bow regulation at both high and low
container pressures.
Built In relief valve and travel stop comply with NFPA 58 over
pressure requirements.
Incorporates W F.NPT downstream pressure tap for an easy
inline check of the regulators delivery pressure.
Molded daphragm 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: pad number2302-31.
)00
FLOW PROPANE
LV3403TR
MaxGnum Co, based on Intel pressure 20 PSIG hlgherlhan the re9WaWrse0N9 and tlelivery Pressure 20%lower lhm Ne regWabseRurg end delivery pressive 2e%lower Nan Ne se 9
A14 RM".
100 Rego Or. P.O. Bar 287 Don. NL 2r244 USA wvnvregcPmducL..cam aim (13fi)449-T/9r Fax (306) 449b594
Designed to reduce first stage pressure of 10 PSIG down to 2 PSIG.
A line pressure regulator is required -downstream to reduce the 2
PSIG to a nominal 11" w.c.
ELa es
• Large vent helps prevent blockage and has °%' F.NPT for vent piping.
• With 15 PSIG inlet pressure, regulator is designed to not pass
more than 5 PSIG with the seat disc removed.
• Incorporates an integral relief valve.
• Replaceable valve orifice and valve seat disc.
• Straight line valve closure reduces wear on seal 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 Y: F.NPT outlet. Plug can be
removed with a Y16° hex allen wrench.
Select blue finish.
*$alSun
Mounts directly to house line piping. Eliminates need for union joints,
elbows, and mounting brackets. Quick and easy to install.
MTATM
Body (LV4403Y Series) ..............................................
Die Cast Zinc
Body (LV5503Y Series .....................................
Die Cast Aluminum
Bonnet (LV4403Y Series) ...........................................
Die Cast Zinc
Bonnet (LV5503Y Series) .................................
Die Cast Aluminum
Nozzle Orifice........................................................................
Brass
Spring.....................................................................................
Steel
Valve Seat Disc ....................................................
Resilient Rubber
Diaphragm ........................
Integrated Fabric and Synthetic Rubber
LV44MSerlcs
LV4403Y4,LV4403Y46R
u
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23.
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rn
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r
LV5503Yserks
r "1
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500.000 750,000 1,000,000 1,250,OOD
INMI
tM'
'■
�T,o 100 -200 300 400 500 600 700 800 goo moo Imo lzoo
C SjUAT, 500,000 1,250,000 2,000.000
cn LV5503Y8
n
a
m
a`
m
220
CFYM.0
Initial SettN
2.80
15 PSIG Inlet
1.60
PSIG Inlet
10 PSIG Inlet
1.605
100 200 300 400 500 600 700 800
9001000 11001200
= BTUft.. 5,000,0m 1,250,000 2,000.000
6
'5440 Y
Me F. NPT
W F. NPT
A'
2 PSIG @ 10 PSIG Inlet
Over Inlet
1,000,000
LV4403Y46R'
Me F. NPT
'/4" F. NPT
'''A'
2 PSIG @ 10 PSIG Inlet
Over Inlet
1,000,000
LV5503Y6
'/.° F. NPT
'/.' F. NPT
'
i /."
2 PSIG @ 10 PSIG Inlet
Over Inlet
2,200,000
LV6503YO
°/; F. NPT
11" F. NPT
9/32'
2 PSIG @ 10 PSIG Inlet
Over Inlet
2,200,000
Maximum flaw b based on 10 PSIG inlet pressure and 1.5 PSIG delivery pressure
AM ?GO100 Rego D, Elan, NC 27244 USA vmrw.regoprcducts.wrn +1 (336) 449-TM7
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Table P-3 Propane Elevated Pressure 2 psig
Maximum Capacity of TracPipe CSST in Thousands of BTU per Hour Propane Gas
;Min SPa{Ipxessure4 �'! 1 X ps(g
,$r{550r2➢mp t
(Based on a 1.52 Specific Gravity / 2520 BTU per cubic foot Gas)
Tubing Length (feet)
r 15 20 25 30 .r 50 .r 70 75 .r 90 100 r 200 Al 300 ,Fa 500 600 700 .Ft 900 1000 1 iOQ 1200 i3oo 1400 i5oo
3/8° 15 649 558 453 389 347 316 271 243 220 203 196 189 177 169 144 137 118 105 96 84 74 68 63 60 57 54 52 49 47 46 44
_�a.a 7$1 7Q1 c'3S9 50$ i459 , 426` 412ir `39�( #Z7 358 321s 29 a 256T '2#0 2T i 1844 165 )150` 139 x131 1 3 117, ,112 7 8 143 1d0 97
l2Y 14 i1528 1706 848 3i C 1 0 s ce
..._u+t. ..,,..uu' ....ax. n rr . �...........�. �nfo u m ;ass ,..� err ,-�.,, _ d_ ..,_ � a�^ _
s>-.r...,a „..- r._ a.a, ,w . _ w_ ...m si.a .... _
- 4 25 3847 2745 2253! 1959 1757 1607 1398 1254 1146 1064 1029 997 942 895 903 735 638 ,572. 324 454 408 374 347 325 306 291 277 266 256 247 239
I
O
1(f �31 6i68111 4756s 3900k s3387p `3035 2715 2410 216'7 i1976 t183 770a 1T,16 1620 1339. 1374e 1,260i. '1g9A 198i' 898 r77 498 38 59'�yy'�r 554,, 5_22 A97 473 'A59� 437 421' 4tl7E.
i v.a v.6 ,..d r...5A� ss 45N7j
1"'' 39 12617 8977 7356 1 6387 5724 5233 4544 4072 3724 3452 3338 3233 3051g 2897 2597 2373 2061 1848 1689 1466 1314 1202 1113 1043 995 934 B91 855 822 792 766
I r-. o r. s m r l+,ry s`n, wcxi: v t m2,ra a r*
ri 2,1574 15198 1�387: $ 0706 95ff5 8722, �t541,r 673,7. 6j,45, ,$5 4 5Q89 ,Saj,'2, 1,�0,�5, IR74r`� 4ZA0, .3$5G_ 3342y 2486. 272i .23e5� ;2104 f°91 , T 7 r 1bu9 '�Sb,°S_ i,R�is lrrjiy2 Xr},5,j, i298 1249, ,j �OG
2" 62 48362 34257 27999 24265 21715 19832 17186 15381 14047 13010 12571 12174 11480 10894 9750 8904 7717 6906 6306 5465 ' 4466 4137 3871 3651 3464 3304 3163 3040 2931 2831
Notes: END (Equivalent Hydraulic Diameter) A theoreticalslze which reflects the hydraulic performance of the tubing. It is mots true physical measure. This numberis used to compare Individual sizes between different manufactures.
The hlgherthe EHD numberthe greaterthe flow capacity of the piping. Tabledoes notinclude effect of pressuredrop across throhne regulator. lithe regulatorloss exceeds 1/2 PSI tbazeclon n inch outlet pressure) Do notusethischan.
Pressuredmps across a regulatorwlll varywith flow rate. FGP-REG-5Phas a 1/2P51 pressure drop ataflow of 307 cubic feet perhour074 MOMm. CAUTION: capacities shown mine table may exceed the muimomcapacity fora selected
regulator.
V
O I
I
Table P-6 Propane Elevated Pressure 26 psig
I Maximum Capacity of TracPipe CSST in Thousands of BTU per Hour Propane Gas
t14'l�n G,asPressur¢"25 ps(g, $
,P e;Ysure;,l toP:.. °'.110 g i..t`'z,.,.
(Based on a 1.52 Specific Gravity / 2520 BTU per cubic foot Gas)
Tubing Length (feet)
1 is 20 25 30 41 so 60 70 75 .f 91 100 125 150 200 250 300 400 500 600 700 800 900 1000 1100 1200 1300 1r11 11
3/8" 15 2741 1982 1640 1434 1292 1187 1037 936 858 800 774 750 711 676 610 559 489 440 405 353 318 293 272 255 242 230 220 212 204 196 190
I
1'J TSFL 5934 A 0 a3600 31W 2853 '2625 23P2 _3l')80 'T914 iZ94 'T729p k678 )�41 _IS17 �'1370 128tl 1105 899 9 8 SOb 728 470 62d' 'S87 ' 7848 s988f A7� Ig59 442h
T'.. ^< n_., w _...t. ±..... ;m.. re...e..u, x°w.,..v as+ "_ .._ n .. as s ;&. ," Ln a a,.". v. a_ .,.a_ s �.p. s.
3/4" 25 14775 10787 8972 7874 7115 6550 5749 5195 4781 4458 4321 4196 3977 3792 3426 3154 2768 2502 2302 2020 1826 1681' 1567 1476 1398 1333 1276 1227 1183 1145 1108
ns'K A*ws,m* r•e+^..
ty 31 g S�T2, t8341, 1532� 3'34b9 T2785 112(25 9864 8923 82 2 !7, 7]" 7437 7224 deS3, 6534 59T2 S4A6. A786 A329F 3Q88� 35y�1 3970/ 2921n 2725 2566 2935 2321 32, 2139 ?063 i997 r193 ,
_.. .�... .",. w R.W. aw .,. ,...w... .."� ,..,..m. T .
1 'r'' 39 39390 28936 24159 21257 19248 17747 15616 14139 13037 12174 11805 11471 10885 10386 9405 8672 7630 6909 6369 5605 5074 4690 4370 4116 3908 3729 3573 3437 3317 3209 3113
1,1Y, ,46 tD139 51042 42447 31216 3360¢ 3119,10 7,s7f109 448P 22522 20989 2033i9 i9747 18713 ,17B32 16TU3 14815 129&9'F1??9 1a792 9462: SS143R &t}Y°�F 3326 �e92 b53} 6�224 i958 S,7iS SS,t ,5336 ,057 '
... .. ., w ....... ... .. M... ... .... �..
2" 62 26376 93908 78935 69783 63421 58655 51854 47126 43586 40801 39612 38532 36635 35019 31827 29435 2602323649 21873 19336 7573 16254 15214 1436 13662 305 1253 1207 1167 1130 10977
Tabledoes notinclude effen of pressure drop across the line regulatocifthe regulator loss exceeds I P51 jorme on 11 inch outlet pressure) Do notuse this chart. Pressure drops across a regulatorwlll vary with Row rate.
FGINREG-51shasa 1 PSI pressuredrop alallow of 434 cull, feet peshour g0g4 MRTUh). CAUnON: Capacities shown In thetable may exceed themaximum capacityfor a selected regulator.
Quality Steel Corporation AGJUG propane Tanks
APPROXIMATE ABOVEGROUND/UNDEGROUND'(AG/UG) VESSEL DMENSIONS AND SPECIFICATIONS
WATER
CAPACITY
DIAMETER
(OD)
HEAD
TYPE
OVERALL
LENGTH
OVERALL
HEIGHT
LEG"
WIDTH
LEG'
SPAONG
WEIGHT
(Ibs.)
"QUANTITY
FULLLOAD
PERSTACK
•120 wg.
24"
Ellip.
5'-8"
3'
V-11/2"
2 10112'
or 3'•11"
260
108 196
16 112
"250 wg.
30"
Hemi.
7'-10"
3'-8"
1'-5"
4'-IT'
480
54
9
`320 wg.
30"
Hemi.
1 9'-7"
3'-S"
1'-5"
5
620
45
9
371/2"
Hemi.
10'
4'-2"
1'-8"
5
950
37 130
' 81 6
1000 wg.
41"
Hemi.
16'
4'-5"
1'-8"
101"
1,800
17115
61 5
1450 wg.
46 1/2"
Ellip.
17'-4"
4'-11"
1'-9"
117'
2,650
12
4
1990wg.
461/2"
Ellip.
23'-11"
4'-Ir
1'-9".
1V
3,520
S
4
Dimensions and specifications shown are apprmdmate. Individual vessels may vary.
•Legspacing+/-2". Leg widths and spacing may vary based on mfg, location. Check with your salespason for details. 120,250,320 wg. standard tanks
-no holes in legs (one center hole on request(. 500 and 1000 wg. standard tanks - 2 holes 16" on ceder. 1450 wg, and up as shown above.
--Full load and stack quantities very byshipping location. Check with your salesperson for details.
General Specifications
- Conforms to the latest edition of ASME Rules for Construction of PressureVessels, Section Vill, Division 1.
Complies with NFPA 58.
Rated at 250 psig from -20" F to 125" F. All vessels registered with National Board.
-Two serviceoptions available:
Option 1: Ready -to -bury underground option, coated with either powder coated phenolic epoxy finish.
or liquid applied epoxy primer coat followed by urethane top coat, supplied with composite
AG/UG dome.
— Option 2: Aboveground option, coated with either powder coated TGIC polyester finish or liquid - —
applied epoxy primer coat followed by urethane topcoat, supplied with steel AG/UG dome.
All vessels are shipped vacuum pre -purged to enable simplified first fill of the vessel.
Updated June 30, 2015
0. CABLE W/
CLAMPS TO
(PULLED
ANCHOR STRAP
(2)HDG CLAMPS TO
ANCHOR (PULLED -
TIGHT)
UNDERGROUND TANK HOLD DOWN DETAIL
GENERAL NOTES:
1. HEUCAL ANCHORS SHALL HAVE AN ALLOWABLE PULL-OUT CAPACITY AS SHOWN BELOW. ANCHORS SHALL BE INSTALLED PER
ANCHOR M(+j11JF�XMRER,TO ACHIEVE STATED LOAD CAPACITY. CAPACITY VARIES WITH SOIL TYPE. VERIFY ANCHOR CAPACITY WITH
SOIL .gp( t,,�E?J�CCWff!TEl;ED'�,,
50ff GALL NK�:'.-`. ,i. ��.n.�.: -1350# .
?10 a4L T)ANIC
2.+.CHEcU '�OR'UNNERGRO[JNQ (JTIUTIES PRIOR TO ANCHOR INSTALLATION
3. 'LOCATION OF TANK RELATIVEgTO ADJACENT STRUCTURES AND FEATURES ARE DEPENDENT UPON LOCAL CODES AND IS THE
R-'SPONSIBIUTY OF OTHERS.
4;-:. 'i THE,>TANK .AS SHOWN IWA BEEN DESIGNED TO PREVENT FLOTATION, COLLAPSE, OR LATERAL MOVEMENT DURING THE BASE
FLOOD. EVENT' ....�
m COPYRIGFir 2016 — FARLEY ENGINEERING, LLC
PA¢f I;pDAT1.1' I AMERIGAS r 4w -_
Consulting Engineer #40111 — CA28108
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