HomeMy WebLinkAboutBOUNDARY PLOT PLAN LEGEND:
(C) = CALCULATED
(M) =MEASURED ST..LUCIE COUNTY
(P) = PLATTED �d e Ir -- _,>t -
CMS =CORRUGATED METAL PIPE BUILDING DIVISION
CNS =COULD NOT SET \� � - r7 .:� - a� '� R
CONC=CONCRETE v` IRM11Spp ED
FFE = FINISHED FLOOR ELEVATION \ _ �7 A�!'7�17 �d p
FND = FOUND Q b Q •_, a "' .', n� 6 .26 099 �Q�C� V!�Yid �V� .
IR =5 8° IRON REBER o
PCPR= PERMANENT CONTROLPOINT TH
CAP h �,O . 6^,2o �ep2 �. $o REpvlEW By
@ —
'Y '��l Y m N �Pf�G l' n II
PL PROPERTY LINE Op`0 `` a4 10R 0
PUDE= PUBLIC UTILITIES AND DRAINAGE EASEMEN �,A yy 17 94 28 °' >50 a o �; o' PLANS ARID REKNIT o emu'
R/W =RIGHT-OF-WAY pSPNp �C. pflK ge �0 g0�+teas 18.15 R =Q
R = RADIUS OF CURVE 20 w O�gENG YM NpVO,�Od 18.12 1657' °0jQ�^7,�p h 2 h
L = LENGTH OF CURVE 8 \ 5 5 O- 11 ���KEPT OE+I JOB OR
n 1�
AF =DOELTAEOFOCURVE -yrj RI R �1` p NJE02�0�* O 4'�04� 18.050 SSP6t y10� �y' 6 . 1 ON ALL BE i►IIIADE
0 SET 5/8" I RON REBAR WITH PLASTIC �\ E\-� Ar8 fN M, ILP 0 rJ
CAP °AJP PSM 6330° Nyy ' o� 5o10w �G
Ah�r
BOO 'NN? 6 �20 ,J " o� LEGAL DESCRIPTION:
�, 6 RNFS\ Ot Z 5\2F;• N LOT 30 AND 31 WITH RIPARIAN RIGHTS, TOP OF WALTON,
W000 \ �9 ! BOOKACCORDING7 PAGE 1. OFL THE AT TPUBLIC RECORDS HEREOF AS ROFDST. LUCIE
6 ORN P \ IN PLAT
18.28 18.11 1n
N�,, 4p e7•t Ftl 8.54 °q Tip �G�1O COUNTY, FLORIDA.
0 26.70 ' y`,� •a 18.48
26.76 N� ap Y L, 9 o�y • o� SURVEY NOTES: .
ND MON o Teat pVE�Oµ\�WP t`� y �\ 2� 9 2u� 1 5JI171S A.050(il), FLORIDARY Y AS ADMINISTRATIIVE CODE.ED IN
CHAPTER
LNG Ow 3y1 'm OP r� \ f . Wa'7� 2. UNLESS OTHERWISE NOTED ONLY PLATTED EASEMENTS ARE
G,502a. ` \2� SHOWN HEREON.
0 Wo 66 \SZO 11.E S.
1 O J� o' 1; 3. NO UNDERGROUND UTILITIES OR IMPROVEMENTS WERE
P\. 5 7 0.1Y p`e, 6 \'py LOCATED UNLESS OTHERWISE SHOWN.
6 N�ON i W HO q9\ GOt1pORp ,`� 4. THIS SITE LIES WITHIN FLOOD ZONES "X" AND "AE",
G01i 2 FF m 9, P �1`)Q:J ACCORD I NO TO THE FLOOD INSURANCE RATE MAP,
a � m 54.. COMMUNITY PANEL NO. 12111CO292 K. EFFECTIVE DATE:
04 .99 t1805 FEBRUARY 19, 2020. BASE FLOOD ELEVATION= 5.0
u= \ap0 pN .50' + te. 11 5. FLOOD ZONE SHOWN HEREON IS AN INTERPRETATION BY THE
p 1880 18.66 y0Y 7 LNG �jl SURVEYOR AND IS PROVIDED AS A COURTESY. THE FLOOD
G p p f8.60 PNOHOP Val�p,N P p0E ZONE SHOULD BE VERIFIED BY A DETERMINATION AGENCY.
Ohs 'ty 0 gym' zyo0 0\\G fNO CC oN *pg00o p1, 6. .BOF LOT 315HOWN ASSUMEDRTON ARE BEAR BSS19D34N51HE EAST LINE
R 0\O O !1` '( 7. ALL LOT DIMENSIONS SHOWN ARE PER PLAT UNLESS
�P OTHERWISE NOTED. ALL SURVEY MEASUREMENTS ARE IN
FEET.
LOj 29 Zp 87 W GONO 0' 8. ALL MAPPED FEATURES SHOWN HEREON ARE UNDER THE
Cr �7"l ,��0 �� DIRECT ZSZUPERV I S I ON AND RESPONSIBILITY OF ALEXANDER
OQ m r J�`I,NGE p 9, SURVEY MAP AND REPORT OR THE COPIES THEREOF ARE NOT
•2o,8O04`h �701 VALID WITHOUT THE ORIGINAL SIGNATURE AND SEAL OF A
dj6 �oPN � y FLORIDA LICENSED SURVEYOR AND MAPPER.
7 C 10.ADDITIONS OR DELETIONS TO THE SURVEY MAP OR' REPO
P�
oO Fc�oN Po�F�, 3oN BY OTHER THAN THE SIGNING PARTY OR PARTIES
5 WNp POP P W 7� PROHIBITED WITHOUT THE WRITTEN CONSENT OF T
3,N 0 460
�N ,dog GAO vo\,N��p pGE�l v O O 11.AODSIGNINONS PARTY
DELETIONS PARTIES.
THE SURVEY MAP OR REPORT
,0;�0'�� `a�$a �P pgOOK b1, J lu �y nUJ PROHIBETEOHWIITHOUT CONSENT OF THE SIGNING ATHE SIGNINGTY OR RTIES 15
PARTY OR
PARTIES.
tu
l CERTIFIED TO:
DIANA A. EWING
12035 SOUTH INDIAN RIVER DRIVE
TYPE OF SURVEY: BOUNDARY PLOT PLAN U C TIE INI FINAL TOPOGRAPHIC ��111i111►ti1lFp
COMPLETED ON: 1 4-10-21 1 1 LAST FIELD DATE: 3-30-21
ALEXANDER J. PIAZZA PSM INC. CAD K `
Surveying • Mapping Consulting REF K:�
619 SW Biltmore Street FILD FB, 000 PG. 00 JOB a ➢�°
® Port St.Lucie,Florida 34983 CREW21-7165 -
Phone: (772)340-7770 OFF OFFICE DATE 4-10-21 ALEXAANU:` PIA
DATE REVISIONS: By: 1BL79d0 Fax. (772)340-2250 Pro(_f s;brtal Surveyor',&' p
CKD AJP SHEET 1 OF 1 DWC C ppar
_1190 Fl or it, 3QartA.(,j,9aAe'No1,ti�6330
K:\BUILDERS\DWG2021\21-7165.dw9,4/14/2021 12:48:04 PM ��',(1t11j111y1,�e�o
i
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I
GAS PIPING INSTALLATIONS
Gas I Undiluted Propane
TABLE 402,4(28) Inlet Pressure h
SCHEDULE 40 METALLIC PIKE ,1 Pressure Drop 0;5 in W
Specific Gravity
INTENDED USE Pipe sizing between single-or second-stage(low pressure)regulator and appliance.
PIPE SIZE(inch)
Nominal 112 31, 1 111, 11/2 _42 21/2 3 4
Actual ID 0.622 0.824 1.049 1.380 1.610 2.067 2.469 3.066 1 4.026
Length(ft) Capacity in Thousands of Btu per Hour
10 291 $608 1,150 2,350 3,520 6,790 10,800 19,100 39,000
20 200 418 787 1,620 2,420 4,660 7,430 13,100 26,800
30 160 336 632 1,300 1,940 3,750 5,970 10,600 21,500
40 137 287 541 1,110 1,660 3,210 5,110 9,030 18,400
50 122 255 480 995 1,480 2,840 4,530 8,000 16,300.
60 110 231 434 892 1,340 2,570 4,100 7,250 14,800
80 101 212 400 821 1,230 2,370 3,770 6,670 13,600
100 94 197 372 763 1,140 2,200 3,510 6,210 12,700
125 89 185 349 716 1,070 2,070 3,290 5,820 11,900
150 84 175 330 677 1,010 1,950 3,110 5,500 11,200
175 74 155 292 600 899 1,730 2,760 4,880 9,950
200 67 140 265 543 814 1,570 2,500 4,420 9,010
250 62 129 243 500 749 1,440 2,300 4,060 8,290
300 58 120•. 227 465 697 1.340 2,140 3,780 7,710
350 51 107 201 412 618 1,190 1,900 3,350 6,840
400 46 97 182 373 560 1,080 1,720 3,040 6,190
450 42 89 167 344 515 991 1,580 2,790 5,700
500 40 83 156 320 479 922 1,470 2,600 5,300
550 37 ,78 146 300 449 865 1,380 2,440 4.970
600 35 73 138 283 424 817 1,300 2,300 4,700
650 33 70 131 269 403 776 1,240 2,190 4,460
700 32 66 125 257 3.85 741 1,180 2,090 4,260
750 30 64 120 246 368 709 1,130 2,000 4,080
800 29 61 115 236 354 681 1,090 1,920 3,920
850 28 ; 59• 111�� 227 341 656 1,050 1,850 3,770
900 27 57 107 220 329 634 1,010 1,790 3,640
950 26 55 104 213 319 613 978 1,730 3,530
1,000 25 53 100 206 309 595 948 1,680 3,420
1,100 25 52 97 200 300 578 921 1,630 3,320
1,200 24 50 95 195 292 562 895 1,580 3,230
1,300 23 48 90 185 277 534 850 1,500 3,070
1,400 22 46 86 176 264 509 811 1,430 2,930
1,500 21 44 82 169 253 487 777 1,370 2,800
1,600 20 42 79 162 243 468 746 1,320 2,690
1,700 19 40 76 156 234 451 719 1,270 2,590
1.800 19 39 74 151 226 436 694 1,230 2,500
1,900 18 38 71 146 219 422 672 1,190 2,420
2,000 18 37 69 142 212 409 652 1,150 2,350
For SI: 1 inch=25.4 mm, 1 foot=304.8 mm, 1 pound per square inch=6.895 kPa,1-inch water column=0.2488 kPa,
1 British thermal unit per hour=0.2931 W,1 cubic foot per hour=0.0283 m3/h,1 degree=0.01745 rad.
Note:All table entries have been rounded to three significant digits.
CYLINDERS
DOT Cylinders
60# & 100# Cylinders*
ITEM NO. SIZE T DESCRIPTION
CYL100-4 100# Port.Cyl.,Collar Type,Less Outage
CYL1.00-5 100# Port.Cyl.,Collar Type,w/Outage
CYL100-7 100# Port.Cyl.,Collar Type,Multivalve
CYL100-8 100# Port.Cyl.,Collar Type,w/Liquid withdrawal
Rust resistant mastic coating applied to footring
H pL
ITEM NO. D OL H C B TW
CYL100-4 '14-.50" 49.00" 43.68" 0.50" 14" 71#
CYL100-5 14.50" 49.00"L . 43.68" 14" 71#
CYL100.7 14.50"ILI -- 49.00" 43.68" 0.50" 14" 71#
CYL100-8 14.50" 1 49.00" 43.68" 71#
D
200#-420# Cylinders*
TRUCK
REM NO. SIZE LOAD OTY. DESCRIPTION
CYL200 200# 192 White Enamel
O
CYL420 t O 420# 99 White Enamel,QUADRIFITT
j REM NO.
I O" D TW W.C. 1B8•.
CYL200 0 . 24-" 1390 476#
CYL420 87"
45.62" 30" 277# 1000#, 24^
�L 'Rust resistant mastic coating applied-to footring.
Only stocked in white.
•H
i Quadrifitt Design Features
j •Easy replacement of standard hardware at lower cost
•Fills IWto 15%faster
•Liquid valve can be used
l •Multivalve available
`• .,_ Manchester 200#&400#tanks are finished with our Armor Clad finish.
e Note:2009&400#tanks are stocked in our Suwanee, Fayetteville and Geneva locations.
e.
VERTICAL TANKS HORIZONTAL TANKS
RAMON Tm Si2E
no GALLONS
text[#Al rA41K suc
lone GA�LWiS
pD1TDH 11 YE�EL REG'D RARDIWI TANK SIZE
TO at ABDVE BASt:FLTIDD 1600 t11u 1 an
_ EI.EYATIDM
l' QO
1!/8' --
`--SOLID RASDNRY SOLID IU1,1100 t H 16'%kX �' �ilB D111Q!CA6LE3
(an SAL1DP) G
TDMR (TYP!(TYP) (71p) p Bl0C�1lETE1 C
QYFh ANwfffS CK
AM
e_11fu1Selr•� FRONT F1.EVATtnNr CUBE
r� ... rl
N 'HORS 1+ 1 �, ,+�,�,,�_�(,,-i fi -0L1..0 v ti 11u_
_.. ..i _.,,. Ti•.�L 4iLl i:LE..V1 i .. �i :ii't►...1 it�•
i taut
.• M 1 �1_GUJ
=YUt� DESIGN CRITERIA �►_
i-111 11 CWM LWAL WHIMREAUIRDWS FOR ACCEPTABLE TAM
• ND SPEEih 170 Vol 132 Von BASDE VELOCITY PRESSURE 86A1 LOCATM 1W SUBJECT FRDPEATY,
XPOSIIRE a 9 HEIGHT a JW MAX g)CPU To BE 1!e' x 7%19 GALVwuo AIRCRAFT CABLE,
ISm CA'Wr&my SUIT, CONDITION a SAND ONLY 3a<ANpm ro BE him a• x 181•% Ire'•NERRM-BEHAAI,
A— 7--10 7ASLE 17-!) 14IMtOE ame AM ORS;
NOT FOR USE IN ORGANIC STIRS G ISE I LMIMLE�S CABLES FOR 1NiTpil gilBN VlTNIN IS90�OP
ABOVE GROUND PROPANE TANK H(ILDDOWN
STEPHEN R. 1�UALSl-1 �':E. PRESCRIPTIVE DESIGN rI)R PERMITTING IN
coca Raton.eoxtls3on.Ft 33428 UNINCORPORATED PALM BEACH COUNTY
I58l1962 0237
PE 43MB SCALD lktx R[VISIDt# Ie-Bi-18
SHEET, A-1
PROPANE CONSTRUCTION NOTES
I. All pipe and fittings above ground and inside building shall be
SCH. 40 Galvanized ASTM A120 or AGA approved corrugated
stainless steel (C.S.S.T.) pipe.
2. All polypipe and fittings shall.be ASTM D2513 or ASTM D2517
and shall be buried outside underground at a depth of 18" with
warning tape and tracer wire.
3. All pipe and meter locations are approximate and subject to
change.
4. All- polypipe shall be joined by heat fusion or approved mechanical
couplings. ,
5. .All"galvanized pipe shall be threaded.
6. All pipe shall be pressure.tested to 20 # PSI for a period of 24
hours.
R122H R222H, R222, R232A and R232E Series
Instruction Manual LP-Gas Regulators
MCK 2156
November 2015
R122H, R222H9 R2229 R232A and R232E Series
Instruction Manual
WARNING
Failure to follow these instructions or
to properly install and maintain this
equipment could result in an explosion
and/or.fire causing property damage and I 1k ilk
personal injury or death. Type R122H
Type R232A
Fisher'equipment must be installed,
operated and maintained in accordance
with federal,state and local codes and
Fisher instructions.The installation in most
states must also comply with NFPA No 54
and 58 standards. tf'
Only personnel trained in the proper
procedures,codes, standards and
regulations of the LP-Gas industry should Type R222H
install and service this equipment.
/ Things to tell the gas customer:
1. Show the customer the vent or vent assembly or vent
tube.Stress that this.opening.must-remain unobstructed
at all times.Tell the.customer to check the vent opening
after a freezing rain,sleet storm or snow to make sure Type R222 Type R232E
ice has not formed in the vent.
2. 'Show the customer the shutoff valve on the Figure 9.R122H;R222H, R222, R232A and
container.The customer should close this valve R232E Series Regulators
immediately if gas is smelled,appliance pilot lights
fail to stay on or appear higher than usual or any
other abnormal situation occurs.
3. Tell the customer to call.your company to service the Introduction
regulator if the regulator vents gas or a leak develops
in the system. Only a qualified gas service person scope of the Manual
should install or service the regulator.
4. Tell the customer to call your company to have a This Instruction Manual covers installation and maintenance
leak check performed if the gas supply has been for the R122H, R222H, R222,.R232A and R232E SeFies
shutoff_or interrupted for any reason. A leak check regulators,which includes first stage., second stage,integral
must be performed by a qualified gas service person two-stage and integral two psig service regulators used on
on the piping system immediately after turning on LP-Gas vapor service applications.They are not to be used
on liquid service.
the gas supply.
A.7*br
`; G
[F—ISHER _-EMERSON,
�, l�cLcn, KLLL, KL.JZA and H232E Series
LP-Gas Regulators
Specifications
Specifications and Tables 1 and 2 list the specifications for these regulators. Contact the factory if the regulator is to be
used on any service other than LP-Gas, natural gas or air.The following information is located on the spring case:type
number, orifice size, spring range and date of manufacture.
Pressure Taps Size Restriction Outlet Pressure Standard Setpoint
118 NPT:#54/0.055 in. Drill on outlet and inlet R222H Series: 10 psi/0.69 bar or 5 psi/0.35 bar
Orifice Sizes R122H Series: 10 psi/0.69 bar
R122H Series: 0.15 in./3.8 mm R222 Series:Second Stage.11 in.w.c./27 mbar
R222 Series: 0.14 in./3.6 mm R232A Series:First Stage:approximately 9 psig/
R232A,R232E and R222H Series:0.193 in./4.9 mm 0.62 bar at 100 psig/6.9 bar, 50 SCFH/ 1.42 Nm3/h
Wide Open C.for Relief Sizing Second Stage:11 in.w.c./27 mbar
R122H Series:23 R232E Series:First Stage:9 psig 10.62 bar at
R222 Series: 18 100 psig 16.9 bar, 50 SCFH/ 1.42 Nm3/h
R232A and R232E Series: 19 Second Stage:2 psig/0.14 bar
R222H Series: 37 Outlet Pressure Spring Ranges
Maximum Allowable Inlet Pressure R222H Series: 8 to 11.9 psig/0.55 to 0.82 bar or
R122H, R222H, R232A and R232E Series: 4 to 6 psig/0.28 to 0.41 bar
250 psig/17.2 bar R122H Series: 10 psig 10.69 bar+I- 1 psig/0.07 bar
R222 Series: 10 psi/0.69 bar (non-adjustable)
Maximum Emergency Inlet Pressure R222 Series: Second Stage.9.5 to 13 in.w.c.I
R122H, R222H, R232A and R232E Series: 24 to 32 mbar
250 psig/17.2 bar R232A Series: First Stage:non-adjustable
R222 SeriesVr: 75 psi/5.2 bar when used with a Second Stage:10.2 to 13 in.w.c./25 to 32 mbar
Fisher®Types R122H, R222H or R622H first stage R232E Series: First Stage.non-adjustable
regulator.40 psi/2.8 bar when used with any other Second Stage.1 to 2.2 psig/0.07 to 0.15 bar
first stage regulator. Approximate Weights
Temperature Capabilities R222H Series with POL:2.12 Ibs/961.8 g
R122H,R222H, R222, R232A and R232E Series: R222H Series with NPT fitting: 1.73 Ibs/784.8 g
-20 to 160OF/-29 to 71°C(2) R122H Series: 1.2 Ibs/544 g
Pressure Registration R222 Series: 1.4 Ibs/635 g
Internal R232A and R232E Series with POL:
1.9 Ibs/865 g
R232A and R232E Series with NPT fitting:
1.5 Ibs/671 g
1.In the event the R222 series malfunctions during a Maximum Emergency Inlet Pressure condition these inlet pressures and the R222 Series relief performance will limit downstream
pressure to 2 Psi 10.14 bar or less.
2.Product has passed Fisher testing for lockup,relief start-to-discharge and reseal down to 40°F/40°C.
Description Integral Two psig Service Regulator
Second Stage Low Pressure Regulator The Type R232E integral two psig service regulator
contains a non-adjustable first stage regulator on the
The Type R222 second stage regulator provides low inlet.The second stage provides 2 psig/0.14 bar outlet
pressure, inches of water column,delivery pressure. It pressure.The second stage portion has a high capacity
is set at 11 in.w.c./27 mbar pressure and comes with internal relief valve construction. The first stage does not
a high capacity internal relief valve. The regulators are have an internal relief valve. The regulators are painted
painted PALM GREEN. GRAY with a WHITE CAP.
Integral Two-stage Regulator First Stage Regulators
The Type R232A integral two-stage regulator contains Types R122H and R222H regulators are designed for
a non-adjustable first stage regulator on the inlet.The high pressure (pounds per square inch)vapor service.
second stage provides 11 in.w.c./27 mbar outlet These regulators have high capacity internal relief valves.
pressure.The second stage portion has a high capacity When used on first stage service,the Type R122H regulator
internal relief valve construction.The first stage does not reduces container pressure to a
have an internal relief valve.The regulators are painted p pprotage e g 10 psig/
GRAY with a BLACK CAP. regulator.The �1
0.69 bar inlet pressure to a second stage
Type R222H regulator reduces container pressure to
2 0 0
DOMESTIC&STORAGE • PROPERTIESAVERAGE . PROPANE.�
TYPES OF UNDERGROUND TANKS
CAPACITY DIAMETER OAL WEIGHT FOrmulq.. ........................ C3H8,.
BOilln Point F.... ELEVATED GRADE REGULAR
100 24" 5'-5 13/16" 245 -44 UNDERGROUND TANK UNDERGROUND TANK
Specific Grayi.V of Gas'Air 1 00.. .. 1.50 1 200 24" 41.9" 188 Q Q Q
Specific Gravity of Liquid Water=1.00 0.51: SHORT RISER LONGRISE" R SHORT RISER LONG RISER
260 31 1/2" 7'-21/2" 472 lr24„r24" 6"
bs per Gallon of Liquid at 60 F .......... - 4.24 I
320 31 1/2" 8'-113/4" 588 BTU per Gallon of'Gas at 60 F 91547 24"
ago 30" 53.8" 291 BTU per Lb of Gas................................... 21591
BTU per Cu Ft.of Gas at 60°F 2516 500 371/2" 91-10" 871
Cu Ft of Vapor at 60°F/Gal of Liquid at
1,000 41" 15'-10 13/16" 1,729 60 F =
391
2,000 46 5/8' 23'-9 3/8" 3,676 Cu.Ft.of Vapor at 60"F/Lb.of Liquid at 60"F 8;547;
3,900 84° Latent Heat of Vaponzation at Boiling Point,
16'-3" 5,73.1 BTU/Gal
.... ... 785.0
6,565 84" 25'-101/2"_ 9,418 Combustion Data:Cu Ft.Air Required'to • •
12,000 _ Brn 1u Cu:Ft,Gas.................... 23:86 • • • , • ,
84" 44' 101/2" 17,400 ••- , .
�'•
Ignition Temperature in Air,"F................. 920
18,000 109.346" 40'-9 3/8" 26;231 to 1.120
30,000 109.346" 65'-113/8" 43,500 Max!mym.Flame Temperature1n;Air,IF 3595 379,000 536,000 536,000' 536,000 748,000 968;000 968,000 968,000
Limits of-Inflammability
30,000 131.875" 46'-9 7/8" 44,359 Percentage of Gas in Air.Mixture: 325 O.0 472;000 521,000 521,000 635;000 900,000:.990;000 940,000
45,000 131.875" 68'-5 3/8" 63,250 293,000 412 000. 483 000 505,000 6681000 783,000 855,000 912,000
at.Lower Limit- %............................... 2.15
0
at U er Limit=-%............. ,26?,000 406,000. 462,000 483,00.0 517,000 ;726;000. 766,000 874,000
60,000 131.875" 90'-0" 86,900 •••••••••••••••••• .9:6 _. .
Octane Number(ISO-Octane 100 Over._' 241;000 338,000 372,000 469,000 .466,0.00 642,000 701,000 868,000'
90,000 131.875" 133'-3 7/8" 128,100 100 `:
223,000 311.000. 341,000 430,000 429,000 691;000 643,000 805,000:
Notes: LOCATION OF ASME CONTAINERS 200406. 285,000 313;000 399,000, 389,000 542,000' 694,000 747,000
41
1) If the cylinder is filled on site from a bulk truck,the From NFPA 58, Appendix I - Federal; state or local 175,000 259,000 287,000 371,000 343,000 493,000 544,000 695,000.
filling connection and vent valve must be at least 10 ft ordinances and regulations should be observed at
from any exterior source of Ignition,openings Into all times. 150,000 233,000 260,000:.343,000 296,000 446,000 495,000 644,000
direct-vent appliances,or mechanical ventilation air 125,000 206,000 234,000 .315,000 251;000 399,000 448;000 596,000
Intakes. -,
11400 1911000. 217000: 293,000 231,000. 369,000"417,000. 554;000'
2) May be reduced to 10 feet minimum for_-a
single container of 1200 gallons_.water.capacity --
or less if It is located at least 25 feet from any otherAPPROXIMATE VAPORIZATION
CAPACITIES
LP Gas container of more than 125 gallons water Intake to Direct • PROPANE
capacity. � Vent Appliance .Under126'Gallon
,eke c. Window A/C 10 tt Wdter Capacity _ • .,•• LIQUIDTANK
.
o (Source of I nitlon Min.
3) Minimum distances from underground con- oo°%4V gDOMESTIC•
talners shall be measured from the relief valve �4-�1N ea ej Mln• sit_ e ;% WATER LING AIR TEMPERATURE
ae° TANKER PREVAI and filling or level gauge vent connection at the �;' / lore
container,except that no part of an underground 1or� Min. gtt CAPACITY 20'F 60'F
container shall be less than 10 feet from a building Ml°' 1 e unoer Min' 0 120 290,304
or a line of adjoining property which may be built -:1101 e , CentralA/� ..Min. 26Dcr l Jd' 516,096
upon. (Note a1 j.-, d�(Source of Igngion 70 Crawl Space % + 200 90;000 140;000
�;000� 129 rc do0 .MIn Opening , �.� 250 406;080 721,920
4) Where the container may be subject to abra- a cL�Ao�c loft
;'F°�
sive action or physical damage due to vehicular o cP Min. '�•� 325 514,100 937,900
traffic or other causes•it must be either,(a)placed `,�� 2 �c�ac� 420 T55,000 230.000
not less than 2 feet below grade;(b)otherwise pro-. %m 500 165,000 1,127,10
Up to 2000 Gallons
tected against any such physical damage. warercapaafy Min ®�°c 1,000 1,088;472 1,978,051
\rah' 2,000 2,128,897 4,257,795
O N c+)
V Lo 10 n a0 --- - U � �