HomeMy WebLinkAboutGAS PIPING SCHEMATICBOARD OF
COUNTY
COMMISSIONERS
GAS PIPING SCHEMATIC
TANK SIZE: Sy DGALS.
APPLICANCE - TYPELSIZE
Al�l,(oaFe. a�oclP�✓
A2
A3
A4 _
A5�
A6
PIPING LENGTH & SIZE
� 1-116i 1L BTU
LO '�__ 1 Z_ BTU
1151 O NL BTU
BTU
BTU
BTU
L1 ( j) FT.
'�!IA.SA_INCH DIA.
L2 1 (�'_ FT.
3 1 -INCH DIA.
L3___�-A_R
FT.
Z, INCH DIA.
L4 3
FT.
3 j A 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.
Revised 7122/14
PLANNING ✓£ DEVELOPMENT
SERVICES DEPARTMENT
Building and Code Regulation
Division
SCANNED
BY
St. Lucie County
(PIPE SIZE WAS TAKEN FROM
THE 2014 FBC FUEL GAS CODE -
TABLE 402 (__J)
Website: www.stfuciem.gov
2300 Virginia Avenue - Fort Pierce, FL 34982-5652
Phone (772) 462-1553 FAX (772) 462-1578
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Table P-1 Propane Low Pressure (Standard)
Maximum Capacity of Omegal'i"TracPipe C55T In Thousands of BTU per Hour Propane Gas
s�� s .I Ala �Vu+75gt`n
(Based on a 1525pecific Gravity / 2520 BTU per cubic foot Gas)
3/8" 15 100 77 59 52 46 r r• rr as r er a
43 36 rcqq 33 30 28 27
f 24 22 19 17 16 14 13 71 9 r
`"`=77Dx3 '' s�1' + 1`(711', '�v s. pg7 3 ''r s m• y; m ,..'� 9 B 8 8 8 6 6 6 6
Mis
3/4" 25 545 ?„,„388 31B 277 249 226 198 177 101 750 146
.,+ ��'f0 ERR "q E me �� : . mw Sn 41 13 27 1 3 3 1 3 1 12 103 90 el 73 6 57 52 49 46 43 �����+nn erg 41 38 36 35 35 33 ' SG - ' zAa�.1. K-0ni 7 ??�d,,,�_.
i er 39 1796 1269 tozg aaa 7aa 7aH sax +. .. •Fib :,,�.(,y.; hxai ,. ti&'1.'a" .;k tt5 R
�m q, qeq az0 42a 402 361 329 287 256 234 203 182 166 154 14 136 130 123 119 114 109 106
n &' z5'... JJ."° s h tl la aYS" 4rjy 1fi,..,� is �' , r"
a 59' ?}m,. S"'r rtr>,r ?
14 uaz �TS834Sa
2" 62 6558 4645 3797 329n 2n a 2voe 2331 uh 1905 1764 1704 1650 1556 7477 1322 1206 7047 936 855 747 663 605 560 524 494 469 448' 429 412 397e 383
L.13n wM1ere Lb Me additl nlale gthoftuhlnya9ndnbeMe numberaraddltana1fiftI grans wltI wri.,, o(bendsanI : .. NguM1allheinwsetlb fie psand/orbends. Y equlvalenllnyM-Itubin,o Mn W-Wng equanan:
0)
CO
Table P-1A
Maximum Capacity ofTmcPipe CSST In Thousands of OTU per Hour Propane Gas
�W
(Based on a 152 Specific Gravity/2520 BTU per cubic foot Gas)
3/8" 15 138 100 82 71 65 59 52 46 43 40 38 36 35 33 30 27 24 22 19
- 17 16 14 73 73 71 11 11 9 9 9
lt' =T4 ..�..:.^f + 9
.+r.. a:lt.ssx-s'w3:'4ct'.. i)"( %3x �,y -
3/4'°� 763 545 446 388 348 318 277"a i , r "� '•' �*�r� f: Z3�.' �47tx i'19qq
249 226 211 a204 �98 187 �� xM m:w3
A A'146 127 112 103 57 54 52 51 49 47
�>`c 90 81 73 68 63 60
Fd�.�'d�fTa`h� a^ssr lax-
. I t.`" y.7f""'1' .ry.
3, >KQ+,„'a6;1¢ a . Z I �T5 `Ytia�r'" ^�6i*,i7Q 1Y4' 9yy*/ ,1",$fi" t" a-; '. ygg^^I
7 7/ "39 2g67 1756 1438 1249 1119 1023 Bea """ aa '" + krk.S "Pip 1•. -
796 728 674 652 632 597. 567 507 464
err,, 402 361 329 287 256 234 217 203 192 182 174 766 160 7
ac�1,s. &7 "A n 54 149
2" 62 9259 6558 5367 4645 4158 3797 3290 - £ s ""� ''1" '" +i'`x^'�e. +1 "'hn!'t38:�Nr-
2945 2688 2490
N.1,19h tlEgmmlesnN 2407 2331 2198 2085 1867 1704 ig77 1322 7206 1047 936 855 792 741 698 663 632 605 581 560 541
ydraulic Olametu) q thearet V oMwldM g Vabl the gy tr icpedasmanavfthe[ubing. ItBnata We physiralmeasure. Thisnumberis used totompare intlivitluelalzes between different manufanures.
Thehighertha EHO nu no n. grea ,3n eowrapadtyadd p'ping. Tablesabove Indutlelossesfarfaur9o-degreebendsandtwoend fittings. Tubing rusawiM la
a(Nhinylo MefollasWng equabamtal3nwhereLlrtheaddxbvlleng[hvltubinyantlnls thenumbeofaddNonainhin911 M orbends rgernumhers orbenasane/orfiti+n gashaVbe lnveaeed by Meegalvalen[length
dNtAiASI-LO8 *041$ gIOf#[?4'v#
■ Corrugated stainless steel tubing (.CSST) gas piping systems will be bonded
in accordance with Section G2411.1 (310) of theFlorida 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.
Designed to reduce first stage pressure of 5 to 20 PSIG down to
burner pressure, normally 11" w.c. Ideal for mediumcommercial
installations, multiple cylinder installations and normal domestic
loads.
• 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 2 PSIG with the seat disc removed.
g
n
e
Incorporates integral relief valves.
Replaceable valve orifice and valve seat disc.
.Straight line valve closure reduces wear on seat disc.
Unique bonnet vent profile minimizes vent freeze over when
property installed.
Large molded diaphragm is extra sensitive to pressure changes.
Built in pressure tap has plugged 1/8" F.NPT outlet. Plug can be
removed with a 3/16" hex alien wrench.
• Baclpncunt design
Maximum 0mv based on 10 PSIG inlet and 9' w.c. delivery pressure.
m
Body ................
-Bonnet .............
Nozzle Orifice ..
Spring ..............
Valve Seat Disc
Diaphragm ......,
........................................ Die Cast Zinc
........................................ Die Cast Zinc
.................................................... Brass
Steel
.................................. Resilient Rubber
integrated Fabric and Synthetic Rubber.
LV4503BSedes
A16 10o Rego or. P.O. Box 247 Son. NC 272" USA wirx.regopmduc6.wm Phone (336) 449-T707 Fax (336) 449b594 ;7-56Y-
Application Materials
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
-BTU's per hour. The regulator is factoryset to reduce container
pressure to an intermediate pressure of approximately 10 PSIG.
Features
Compact design can be connected to a service valve using either
a POL adapter or a RegO product pigtail.
Large threaded%" FNPT 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 conosion protection.
Mounting bracket available as an accessory: part number 2302-31
Ordering Information
Body...............................................
.............................. .............. Zinc
Zinc
Bonnet............................................................................ Steel
Spring....... .............. ....................................................................
SeatDisc ................. 1.......... ..................................... Resilient Rubber
Diaphragm ........................•••• integrated Fabric and Synthetic Rubber
FI.UW PROPANE
ItV IR '� war uuue� 1,500,0()0
/'FNPT h'FNPT %a" 10 PSIG 9,00
VVdOaTRV9 Pa/I N P W 9
Maximum flow based on inlet pmssure 20 PSIG higher than Ne mgulamr seeing and dulneq pressure 20%l ma 9 mo9 �Y P
nassuas
A14 RHO.
100 Rego Gr. P.O. ea[ 247 FJon, NC 27244 USA wwwre9opmm ducls.m Phne (036) b49dTOT Fax (336) 049.659d
uwtmsrm. -
Qui,„ 'y Steel Corporation AG/UG Propane Tanks
-yiLc, 'A'iDT?
1450 ea Mr- U=
APPROXIMATE ABOVEGROUND/UN DEG ROUND (AG/UG) VESSEL DIMENSIONS AND SPECIFICATIONS
WATER
CAPACITY
DIAMETER
(OD)
HEAD
TYPE
OVERALL
LENGTH
OVERALL
HEIGHT
LEG*
WIDTH
LEG**
SPACING
WEIGHT
(lbs.)
**QUANTITY
FULLLOAD
PERSTACK
*120 wg.
24"
Ellip.
5'-B"
3'
V-1 1/2"
2-101/2"
or 3�11"
260
108 196
161 12
*250 wg.
30"
Hemi.
7'-10"
3'-8"
1'-S"
4'-11"
480
54
9
*320 wg.
30"
Hemi.
9'-7"
3'-8"
V-5"
5
620
45
9
500rw�i
371/2"
Hemi.
10'
4'-2"
V-8"
5'
950
37130
816
1000wg.
41"
Hemi.
16'
4'-5"
1'-8"
10'1"
1,800
17115
615
1450 wg.
461/2"
Ellip.
17'-4"
4'-11"
V-9"
11'-7"
2,650
12
4
1990 wg.
461/2"
Ellip.
23'-11"
4'-11"
V-9"
16'
3,520
8
4
Dimensions and specifications shown are approximate. Individual vessels may vary.
-Leg spacing+/-2". Leg widths and spacing may vary based on mfg.location. Check with your salespuson for details. 120,250,320 wg. standard tanks
-no holes in legs lone center hole on request). 500 and 1000 wg. standard tanks-2 holes 16" an center. 1450 wg. and up as shown above.
--Full load and stack quantities vary by shipping location. Check with your salesperson for details.
General Specifications
- Conforms to the latest edition of ASME Rules for Construction of Pressure Vessels, 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 service. options 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
1LV. CABLE W/
CLAMPS TO
(PULLED
ANCHOR STRAP
CLAMPS TO
(PULLED -
UNDERGROUND .TANK HOLD DOWN DETAIL
GENERAL NOTES: PER
1.. HELICAL ANCHORS SHALL HAVE AN ALLOWABLE PULL -
ANCHOR CAPACITY AS SHOWN AEIOW. ANCHORS SHALL BE INSTALLED
ANCHOR WjdIJ AWRERJO ACHIEVE STATED LOAD CAPACITY. CAPACITY VARIES WITH SOL TYPE. VERIFY ANCHOR CAPACITY WITH
SOILL7�$'i ,�1.CdP UffiRED;.:.:,,. -
�5tl TfA `Ti1NIc
�`1p (3�L T`K } 350.
2 ` 2CHECK �OR'UNDERGROUND`CI TILITIES PRIOR TO ANCHOR INSTALLATION
3. °LOCATION OF TANK RELATIVE,, O ADJACENT STRUCTURES AND FEATURES ARE DEFENpE�JT UPON LOCAL CODES AND IS THE
RIS, P,ONSIBIUTY aF OTHERS.
4.%,', THE JANK,.AS SHOWN HAS. BEEN DESIGNED TO PREVENT FLOTATION, COLLAPSE, OR LATERAL MOVEMENT DURING THE VASE
FLOOD. EVENT
O COPYRIGHT 2016—'FARLEY ENGINEERING, LLC
P± I AMERIGAS r cnosmung Engineer #am1i — cazsloH .