HomeMy WebLinkAboutSITE PLAN WITH POOL PAPERWORKFIND IRC
"GCY LB# 4108" (CALCULATED)
t
SW SECTION CORNER OF N 1/4 CORNER OF
SECTION 7-34S540E SECTION 7-34S540E R
12 � S89'41'07"E 2657.08'(TOTAL) 1 `> VACANT W A
664.53' asU �,Dr ` 1 ; �� PARCEL ID k
1418-213-0015-bW/6 V
13 18 ur �« ram„ "
NORTH LINE OF ^� a
SECTION 18-34S-40E /* " 5 �!4
ro viesag♦ 0 I U'-F'(a.+-, �o✓i'[.Q OCJni'�6� \ \ q b
M1 xM1a'C' ry� e r ■ e
60 0'
Oo
N "F W
W al0 0 �' -. 2e.m• . Y�: •J07.46
x ZZ a , 6300 oPosED _
tL O O 10 ~J � 8 R61^ - WELL
OAF m w to
\W Ncr
96.50'.•. ' '�Q iJ
Z z W w a.! i� €, 30' DIY ' 13 d . � ' -g 3{5's.� I ✓4.- Z TN
_ —
vi 4 51
\
U- O O O �i'
O 2 63.75'
2 %
N m ( - '� .. 37. '
90.41'
me W
Qo ""j"" ,� St. Lucie County Health Dept N89'38'29-W 271.93'
Io. I �° �. Environmental Health Section
"'1t`'z Site Plan Approved for Construction MIN, SEZBACK REQ.
+tea I SSDuper vious i fAI S � FRONT
SS## a V ,e P213-0025-000/1 AID
SIDES
o le ewer., CNR SI E
W E 1/4 CORNER OF REAR
SECTION 18-34S-40E LEGEND: ZNQ, - "
1326.35' 3983.66' (C) - CALCULATE TECH. w
N89'34'05"W 5310.01' (M) - MEASURED
W iPL
4 CORNER OF (BEARING BASE) (P) - PLATTED + R
SECTION 18-34S-40E CMS - CORRUGATED METAL PIPE
CNS - COULD NOT SET L
CONIC n. CONCRETE F
FFE - FINISHED FLOOR EI,EVATION S
FND - FOUND 5/8" IRON REeAR
OF SURVEY:l BOUNDARY I PLOT PUN I U/C TIE INI F I NAL ITOPOGRAPHICI IRC = 5/8" IRON REAAR WITH PLASTIC CAP
ALEXANM J. PIAZZA PSK N Q aw K:\LI8VrMf
Stry7M9 " maPpl9 " Conlla "09 REF K: \
1216 SE ' ',, - ' Boulevard FLO gt/CS
Part SL Ludo. Flerido 3402
Phans: (77?) 300-WW OFF BIG
�M Fac (772) 3B0-OS20
REV610VN5: By: _ CK& AJP -
' U-
o
-- -- r--
JAN
LOCAT 1 t
NOT TO ---
CITY WATER AND SEWER
LEGAL DESCRIPTION:
THE SOUTH HALF OF THE NORTHWEST QUARTER OF THE SOUTHWEST
QUARTER OF THE NORTHEAST QUARTER OF THE NORTHWEST QUARTER
OF SECTION 18, TOWNSHIP 34 SOUTH, RANGE 40 EAST, ST. LUCIE
COUNTY,FLORIDA, LESS THE WEST 60 FEET THEREOF.
SURVEYORS NOTES
1. UNLESS OTHERWISE NOTED ONLY PLATTED EASEMENTS ARE
SHOWN HEREON.
. NO UNDERGROUND UTILITIES OR IMPROVEMENTS WERE
LOCATED UNLESS OTHERWISE SHOWN.
THIS SITE LIES WITHIN FLOOD ZONE "X', ACCORDING TO
THE FLOOD INSURANCE RATE MAP, COMMUNITY PANEL NO.
1211100070 F, EFFECTIVE DATE AUGUST 19. 1991.
. FLOOD ZONE SHOWN HEREON IS AN INTERPRETATION BY THE
SURVEYOR AND IS PROVIDED AS A COURTESY. THE FLOOD
ZONE SHOULD BE VERIFIED BY A DETERMINATION AGENCY.
. BEARINGS SHOWN HEREON ARE BASED ON THE 1/4 SECTION
LINE OF SECTION 18-34S-40E, IS ASSUMED TO BEAR
N89'41'07"W.
ELEVATIONS SHOWN ARE BASED ON BENCHMARK "C 167" WITH
AN ELEVATION OF 21.00 NAVD 88 AND ARE REFERENCED TO
A 600 NAIL LOCATED IN THE WOOD POWER POLE 8 FEET
NORTH AND 62 FEET WEST OF SOUTHWEST PROPERTY CORNER.
ELEVATION - 25.37
7, ALL LOT DIMENSIONS SHOWN ARE PER PLAT UNLESS
OTHERWISE NOTED.
8. NOT VALID WITHOUT THE SIGNATURE AND ORIGINAL RAISED
SEAL OF A FLORIDA LISCENSED SURVEYOR AND MAPPER.
— PROPERTY CORNER
- PERMANENT CONTROL POINT
- PROPERTY LINE
- R I GHT-0E-*WY
e. RADIUS OF CURVE
LENGTH OF CURVE
- SQUARE FOOT
DELTA OF CURVE
- SET 5/8" IRON REBAR WITH PLASTIC
CAP "AJP PSM 5330"
Fe. 24 PG 24 JOB 42
GTE 11/18/OS
1 ur 1
CERTIFIwww"LDEfNCCO
N
LIBERTY .
hereby certify that the survey shown hereon is true and
orrect and is based on actual measeurements taken in the
ield. This survey meets the Minim= Technical Standards
f Chapter,•61G17 Florida administrative code,
ALEXAN J. PIA
Profess ono Surveyor k Mapper
Florida Certificate No.: 6330
ABOVEGROUND/UNDERGROUND DOMESTIC TANKS
120 - 2.000 avt�
- NEIJ!
8" dome in black plastic or white
galvanized steel.
POWDURV OneCure;` Super Durahle Topcoat
with Zinc Rich Primer on Aboveground
rJDURA oneCure' Two coat system properties include:
• Zier. ,irli ppoil, bfimrr
• supCr rlur,dk- 761C ;iG�'Jr:h•r luliro:::
• Snprnr:: r cone• .,.n :aid uarnr W rAcbon .
• DUZI serve== DL, D�s for above or underground applications
• -Option 01: Ready -to -bury red oxide durable povider coating with Glacd
• polyethylene AGUG dome'
• Option # •, Abov=_ground option with steel 8- AGUG dome
• All valves and float gauges are centered under dome
• Fabricated to the latest F.S.M.E. Code, Section Vlll, Division t _
• Registered 'with the National Board
• 472 liquid level outage valve orifice reduces refueling emissions
• Vacuum pre -Purged to -Save time. money and product
- Applrcable federal. state, or local regulations may certain speOf requim_menis for
CONTAINERS1 protective coatings and calhod2 protection. Tnepamhaserand.hsta:'er sire responsible
for compliance io:th ad federal, state, local and ArFPA industry raulabon5. CatnoYc
ontafnin. • • protection is required and mating must be continuous and uninterrupted and must
comply with an local, mate or national code.
www.TrinityContamers.com Call Toll Free: 888-558-8265
I
TRINITY
&.nW ing Our Wolld'e EnergDTM
Iv
General Specifications
Conforms to the latest edition of the ASME code for
Pressure Vessel, Section Vlll, Division 1. Complies with
NFPA 58.
Rated at 250 prig from -20` F. to 125' R All tanks may be
evacuated to a full (14.7 PSI) vacuum.
Vessel Finish: Coated with epoxy red powder. ( Tanks coated
with the epoxy powder must be buded). For Aboveground use,
tanks may be coated with TGIC powder.
Applicable federal, state or local regulations may contain
specific requirements for protective coatings and cathodic
protection. The purchaser and installer are responsible for
compliance with all federal, state or local regulations,
AOAT
SERVICE /
MULTNALVE
RELIEF
VALVE
FJT WGS LAYOUT UNDER DOME
�TE
Rev: Jan. 27, 201E
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 current flows 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 overtime.
Corrosion rates are generally higher in wet soil environments since the
conductivity of the soil promotes the flow of DC current in the corrosion
circuit.
Corrosion generally exhibits Itself on underground tanks In either a
general overall rusting or more commonly, apitting anack 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
r Protecting underground
' tanks from corrosion is
easilyachieved bythe use
of two commonly applied
protection . methods:
external coating and
cathodic protection.
These two methods
are complementary
and should be used in
conjunction with the
other. An effective
external protective
coating insulates the steel from the soil environment, thus preventing
the flow of corrosion current from the anode to the cathode. An effective
external coaling can protect over 99% of the tank surface area. However,
no coating is perfect Damage from construction or soil stresses create
tiny defects, which may result In accelerated corrosion Ithe defect.
Cathodic protection prevents corrosion at those defect by applying
DC current from an extemal source, forcing the tank to become
cathode. Application of sufficient DC current to the tankwill 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 pmpane tanks. Impressed current systems
are more commonly used for large structures such as large diameter
pipelines. Electrical isolation of the tank from metallic piping systeths
and electrical grounds is critical for the cathodic protection system's
effectiveness.
How 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 coupled to steel results in DC current flow from the
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. By connecting the
two metals together, the difference of 1 to 1.25Vvoits results in current
flow to the tank that overcomes the natural corrosion cells that exist on
thetank W'dhthis current available tothe tank, nocorrosion occurs.
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 AZ63) and
High Potential. The 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 99% pure magnesium having an open circult potential
up to -1.8V. This alloy should be used for soil applications over 10,000
ohm -cm resistivity.
The two most common anode sizes used for underground propane
tanks are9lb. and 171b. The size designation relates to the metal weight
10' of #12 TW insulated wire is attached to the anodes. Anodes are
then bacldilled in a mbdure of gypsum, bentonite, and sodium sulfate
to lower the electrical resistance of the anode to soil. The mbdure is a
low cost, nonhazardous, electrically conductive backfill. The anode and
backfill is then packaged in a cotton bag and either a cardboard box or
paper bag. Actual shipping weight of these anodes with backfill is 27
lb. and 45 lb.
Application Recommendations
Magnesium anodes can protect underground tanks in most soil
conditions. The H-1 alloy Is generally very effective. The following chart
provides size and quantity recommendationsforvarious size tanks based
on conservative design assumptions. This chart covers soil conditions
up to 10,000 ohm -centimeter resistivity. Resisiivities higher than
10,000 ohm -centimeter generally represent very dry solls. Verification
of soil resistivity can be performed through soil analysis. Contact us
for design recommendations in locations where soil resistivities exceed
10,000 ohm -cm, or if there is no effective extemal coating on the tank
The propane service line from the tank to the house also must be
considered in the cathodic protection design, unless the service line
is plastic. All underground steel pipe should be externally coated with
a corrosion resistant material. The service line should be electrically
isolated at the house with an insulating fdting or union. If service pipe
is less than 50' in length, the tank anodes will provide sufficient current
to protect both tank and pipe. For longer lengths of pipe, an additional
anode may be required at the house connections.
If another metallic material such as copper is used for service piping,
the pipe should be electrically isolated from the tank at the fill pipe
connection. Copper and steel create a galvanic couple that will accelerate
corrosion of the steel tank when directly connected to copper piping.
Generally, copper piping does not require cathodic protection.
Soil Type 'fwipe Soils, clay, Sand, Gravel, Rocky
Sandyi.Darn Areas
Tank Cap. 510 5008 ohm -cm 5000 to 10000 ohm -cm
at. Size oly. Alloy Size Oty. Alloy
120 93 1 H-1 9i' i H-1
150 9t 1 H•1 9F 1 H 1
250 98 1 H-1 91 2 H-1
325 91 1 H-1 9# 2 H-1
500 17.4 1 H-1 91 2 H-1
1000 174 2 H-1 9¥ 4 H-1
150a 171 2 H-1 91 4 H-1
2000 170 3 H-1 — a H-1
=Based on 90% effective external coating, 2 maM currant density, and 30-
yaw Anode L fe.
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.
F-1
tode 2anodss 4anoctes
4.Anodes are shipped in either cardboard boxes or multi -wall
papersacks. Remove outer container and burythecloth 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 of the tank Anodes work best
in locations with permanent moisture, so generally the deeper
the better.
6.After placing the anode, stretch out the anode connection wire
and extend over to a connection point on the tankfill 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.
B.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.
1D.Verify performance of the anode using an appropriate test
procedure.
Mechanical Connection Under Dome
Cathodic Protection Testing Procedure
Equipment Needed: Digital Voltmeter, Red Test Lead Min.12' Long
& Black Lead Min. 2' Long, Reference Electrode (Copper/Copper
Sulphate Half -Cell)
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 mumvalve. A good solid connection is very important.
(DO NOT connect to shroud).
STEP 2: Insertthe blacktest lead into the Common jack on the meter,
and connect the opposite end of the lead to a charged reference
electrode (h cell).
STEP 3: Remove protective cap from the porous plug at bottom and
of electrode. Place porous plug end into native soft (remove grass if
necessary) atfour locations around the tank (one on each side of the
tank, and one at each end of the tank). if difficulty is encountered
obtaining readings, moisten soil with water or dig Ya cell deeper into
the soil.
STEP 4: Record all four meter readings on an appropriate form. The
least of all four readings should be a minimum of-0.850v or more
negative. {Note: If any of the four readings are below (less negative)
-0.850v then the tank is not fully protected}.
Charging Reference Electrode
STEP 1: Unscrew and remove porous plug and of new reference
electrode. Add deionized or distilled water to the copper sulfate
crystals, filling electrode completely. The solution will turn blue in
color and there should always be excess crystals at the bottom of
the tube. DO NOT USE TAP WATER.
STEP 2: Replace porous plug end 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 porous plug
to became completely saturated before use.
Caution: Do not allow electrode to eontactoil, road salts, or other
substances that may contaminate the solution by,absorptfon
through porous plug. Du not allow electrode to freeze.
Distributed By.
Loss of Pressure
Freeze-up inside the regulator.
This will prevent the regulator from regulating properly.
Regulator freeze -ups occur because there Is excessive moisture
In the gas. Freeze -ups can also occur In pigtails that are kinked or
bent where free flow of the LP -Gas is restricted. These freeze -ups
can occur when the moisture, gas flow and temperature combine to
create a hazardous condition. Freeze -ups can occur at temperatures
above 32'F.
Action Required: All LP -Gas should be checked for moisture content
prior to delivery to consumers and proper amounts of anhydrous
methanol added if the gas cannot be returned to the supplier. Any
container suspected of having excessive moisture should be treated
with the proper amount of methanol.
Customer Safety
Since regulators are often used by consumers without previous
knowledge of the hazards of LP -Gas, and the LP -Gas dealers are the
only ones who have direct contact with the consumers,
IIt Is the dealer's responsibility to make sure that his I
customers are properly Instructed In safety matters relating
to their installation.
At the very minimum, it is desirable that these customers:
1. Know the odor of LP -Gas and what to do in case they smell
gas. Use the NPGA "Scratch 'n SntfP' leaflet
2. Are Instructed to never tamper with the system.
3. Know that when protective hoods are used to enclose
regulators andfor valves, that these hoods must be closed,
but not locked.
4. Keep snow drills from covering regulators.
5. Know the location of the cylinder or tank shut-off valve In
emergencies.
Underground installations
Special hazards can occur if regulators are not properly installed in
underground systems. Water, dirt, mud and insects can get into the
regulator if the bonnet cap is not tightly in place and the vent Is not
protected with a proper vent tube, opening above any potential water
level.
Most problems occur because the waterproof dome on the buried
storage tank does not extend above the ground level sufficiently to
keep out water and mud.
Refer to NPGA No. 401. ,
Regulator adjustment dosure
cap must be tight
End of regulator vent or vent tube
Grade ground downward and b be lotafed above the highest
away around housing dome probable vatarlevel.
This prevents water mlledng
and running into orstandmg 2to6inches
amunddome. \ minimum,
6 Inches minimum /
(18 fnches mlNmum if
subject to whkular traffid.
Note: Water mark left in housing dome at level
above regulator vent, or end of vent tube requires
replacement of regulator. Then correct installation.
General Warning
All RegO Products are mechanical devices that will eventually
become inoperative due to wear, contaminants, corrosion
and aging of components made of materials such as metal
and rubber. As a general recommendation,Regulators should
be replaced in accordance with all of the recommendations
outlined in this safety warning. The recommended service
life of a regulator is one of many factors -that must be
considered in determining when to replace a regulator.
The environment and conditions of use will determine the safe
service life of these products. Periodic inspection and maintenance
are essential.
Because RegO Products have a long and proven record of quality
and service. LP -Gas dealers may forget the hazards that can occur
because a regulator Is used beyond Its safe service life. Life of a
regulator Is determined by the environment in which it 9ives.° The
LP -Gas dealer (mows better than anyone what this environment Is.
NOTE: There is a developing trend in state legislation and
in proposed national legislation to make the owners of products
responsible for replacing products before they reach the end of their
safe useful life. LP -Gas dealers should be aware of legislation which
could affect them.
k
6
BAG0. 100 RagO nr. Elan. NG 27244 ❑SM1 vrww re9oproduclarnm «t (335) 449 7707
First Stage Regulator
with Relief Valve and Second
Pressure Tap Regular.
with Lai
Pressur
First Stage
'r: a regulator is truly the heart of an LP -Gas installationjfPS-S'1(G3t
xrpensate for variations In tank pressure from as low aj 10 PSIG — and still deliver a steady flow of LP -Gas atconsuming appliances. The regulator must deliver this
:esp',te a variable load from intermittent use of the appliances.
---cuah a single -stage system may perform adequately in many
'• rations, the use of a two -stage system offers the ultimate in pin-
�C--1 regulation. Two -stage regulation can result in a more profitable
_P Gas operation for the dealer resulting from less maintenance and
`e,,asr installation callbacks —'and there Is no better time than now for
`stalling RegO Regulators in two -stage systems.
Urdfonn Appliance Pressure
he installation of a two -stage system — one high pressure regulator
al the container to compensate for varied inlet pressures, and one
xv pressure regulator at the building to supply a constam delivery
€!assure to the appliances - helps ensure maximum efficiency
and trouble -free operation year-round. It Is important to note that
woe pressure at the appliances can vary up to 4' w.c. using single -
stage systems, two -stage systems keep pressure variations within
7F w.c. New high-efidency appliances require this closer pressure
control for proper ignition and stable, efficient operation. In fact, one
major manufacturer requires the use of two -stage systems with their
appliances.
Reduced Freeze-ups/Service Calls
Regulator freeze-up occurs when moisture in the gas condenses and
ireezes on cold surfaces of the regulator nozzle. The nozzle becomes
dulled when high pressure gas expands across it into the regulator
body. This chilling action is more severe in singie-stage systems as
gas expands from tank pressure to 114 w.c. through a single regulator
nozzle.
Size The System Correctly
Prior to installing your two -stage system, be sure the system pipe
and tubinb Is property sized. Proper sizing will help ensure constant
delivery pressure to the appliances during fluctuating loads at all
times. Just as important, be sure the RegO Regulators you choose
are capable of handling the desired load. This Is another advantage
of two -stage systems — they are capable of handling much
more BTU's/hr. than single -stage systems. The RegO 'LP -Gas
Serviceman's Manual` provides complete Information on pipe sizing
and proper regulator selection.
Two -stage systems can greatly reduce the possibility, of freeze -ups
and resulting service calls as the expansion of gas from tank pressure
to 11' w.c. Is divided into two steps, with lass chilling effect at each
regulator. In addition, after the gas exits the first -stage regulator and
enters the first -stage transmission line, it picks up heat from the line,
further reducing the possibility of second -stage freeze-up.
Service calls for pilot outages and electronic Ignition system failures
are also reduced as a result of more uniform appliance pressure from
two -stage systems.
Economy of Installation
In a single -stage system, transmission line piping between the
container and the appliances must be large enough to accommodate
the required volume of gas at 11' w.c. In contrast, the line between
the first and second stage regulators in two -stage systems can be
much smaller as it delivers gas at 10 PSIG to the second -stage
regulator. Often the savings in piping cost will pay for the second
regulator.
As an additional benefit, single -stage systems can be easily
converted to two -stage systems using existing supply lines when they
prove inadequate to meet added loads. This is the least expensive
and best method of correcting the problem.
Allowance for Future Appliances
A high degree of flexibility is offered in new installations of two -
stage systems. Appliances can be added later to the present load —
provided the high pressure regulator can handle the Increase — by the
addition of a second low pressure regulator. Since appliances can be
regulated independently, demands from other parts of the installation
will not affect their individual performances.
Replace Pigtails
If you are replacing an old regulator, remember to replace the
copper pigtel. The old plgtal may contain corrosion which can
restrict flow. In addition, corrosion may flake off and wedge
between the regulator orifice and seat disc — preventing proper
lock -up. '
RequfreFirstStapRegulatoxF) w"th Ruflt-wHelleff Valves
First Stage Regulator
with Relief Valve and
Pressure Tap
First Stage Piping
Second Stage
Regulator
with Large Vent
and Pressure Tap
r To AppllanceslFumace
T'ruperatore
With no first stage relief valve,
propane liquid may form here... 70' F."'.'
40' F. 72 PSIG
Resulting in sudden pressure surge due to gashing into vapor here] 90° F 50° F. 86 PSIG
First stage relief can prevent liquid from forming in first stage piping g0- F, 60° F. 102 PSIG
during periods with no gas demandl I I
---
Pressure at which liquid can form
at various temperatures.
Vapor Pressures of LP -Gases
M
Temperature *F.
The Problem
Many modem LP -Gas appliances are equipped with pilotless ignition
systems. Water heaters and older appliances use plot lights, but it
has become a common practice for energy conscious homeowners to
shut-off the pilot when leaving home for extended periods of time. In
each instance, then: is no gas demand at all for extended periods.
The Consequences
If the first stage regulator fails to lock -up tight, usually as a result
of a worn seat disc or foreign material lodged between nozzle and
seat disc, pressure A build-up in the first stage piping — possibly
to a level that approaches tank pressure. Combining this with warn
ambient temperatures and cool ground, propane liquid may form in
the first stage piping.
When gas demand resumes, this liquid may pass through the second
stage regulator into the appliances and furnace. NOTE — the second
stage regulator will not relieve the pressure in first stage piping.
The rapid vaporization of the liquid may cause a rapid pressure surge
that could seriously damage critical components of the appliance and
furnace controls.
A fire or explosion could occur as a consequence.
The Solution
Rego LV4403 Series First Stage Regulators with Built -In Relief
Valves reduce the possibility of this serious hazard In two stage
applications. The built-in relief valve is designed to vent as needed
and reduce the possibility of first stage piping -pressure from
becoming high enough to form liquid.
4
a NEGiF 100 Rego Dr. Flon, NC 27244 USA vmw.regapraduds.com +1 (336)449-7707
Ideal for use as a first stage regulator on any domestic size ASME or one
DOT container in propane gas installations requiring up to 1,500,00b 0BTU's per hour. The regulator is factory set to reduce container
pressure to an intermediate pressure of approximately 10 PSIG.
L'/." FNPT I '/:" FNPT I %/ai' I 10 PSIG " ,
LV3403TRV9 9'00
Meeimum Now based on iNel pressure 20 PSIG hgharthen the regulator setting and dernery pressure 20%lower then
the regulator setting and delhery pressure 20% lower than the setting.
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
Industrial furnaces or boilers. Also Incorporated in multiple cylinder
installations.
1,500,000
10
5-10
/•"
att
06-10
Yes 2,500,000
5
.1S
10
5-10
• When used for final stage pressure control, must either buwiporata integral rerier valve or separate relief valve should be specified in aosrdance
with NFPA Pamphlet 58.
^ Maltinuun flow based on inlet pressure20 PSIG higher than the
regu1stolsettin,
and delivery pressure 2D% lower than the setting.
Designed to reduce first stage pressure of 5 to 20 PSIG down to
bumer pressure, normally 11' w.c. Ideal for medium commercial
Installations, multiple cylinder installations and normal domestic
loads.
MUL
LV440354 . I Y•
LV4403B46 '/z• F. NPT
17' w.c.
LV4403B46R' #ZB 'it10PSIG 9°tc 13' Over Inlet
LY4403666 NPT Dri0 Inlet w-e
LV4403B66R• F. NPT
• ead,mount design
.Mum taw based on 10 PSIG inlet and T w.c. delivery pressure
935,000
LV3403TR
LWMSedes
LV44031111SarMs
ES-D-C,AC_Generator Generac
Job Name _
Job Location
Engineer
Approval
Contractor
Approval -
Contractor's P.O. No.
Representative
SKU
Dormont Supr-Safe®
Flexible Gas Appliance X
Connectors
The flaxible connection between the gas supply and the gas inlet
_
Of a Generac® Stationary Outdoor Backup/Standby Generator.
Features
• Operating Temperature -40•F to 150•F (-40•C to 65.6•C)
For use with Generac'
stationary outdoor backup/
• Operating Pressure MAX 0.5ps1(3.45 W4
standby generators.
• Hydrostatic Burst Pressure MIN 250psl (1725 kPa)
• Flexible Tube Material Annealed 304 Stainless Steel
• Flare Nut Material Carbon Steel with Zinc Trivalent
Chromate Plating
• Flare Adapter Material Carbon Steel with Zinc Trivalent
Chromate Plating
CSA Group Certificate of Compliance to
Product Standards
ANSI Z21.7WCSA 6.27 — Connectors for Outdoor Gas Appliances
and Manufactured Homes
Scope states '...Intended for a derior use above ground for maldng
non -rigid connections... between the gas supply and the gas inlet
of an appliance for outdoor installation that is not frequently, moved
after installation.' In addition section 1.5.4 states the connector is
designed for occasional movement after Installation. Repeated bend-
ing, flehdrtg or extreme vibration must be avoided. Normal opera-
tion of a dothes drye, rooftop HVAC unit or SIMILAR OUTDOOR
APPLIANCE DOES NOT constitute extreme vibration or movement.
ANSI Z21.24/CSA 6.1 o — Connectors for Gas Appliances
Fxcludltg 60/61 Series)
sA-
c us
Product Configurations
All installations must completely comply with an Dormont manufacturing company warnings
and instructions, national, state and local codes and all applicable anst standards.
Series 30, 40 and 60
Applicable Codes
ANSI Z223.1/NFPA 54 National Fuel Gas Code Section 9.6
International Fuel Gas Code (IFGC) Section 411.1
8149.1 — Natural Gas and Propane Installation Code
(CSA Group) Section 6.21
Uniform Mechanical Code (UMC) Section 1313.0
Uniform Plumbing Code (UPC) Section 1212.0
Additional Approvals
Commonwealth of Massachusetts Board of State Examiners
of Plumbers and Gas Fitters
Additional Testing
UL2200-2015: Stationary Engine Generator Assemblies
Section 56B Vibration Test.
Dnmout product Wamdore in ILS custlary mils and metric are aypnnimate and are pmydedfur Merence D*,, rmprecise measure-
m*me,Wass*mrhdDormantiechNmlSev Dammrtreashas the rlghtto charge ormoddyprodutdeslgn, mncWchon, spedhcatIms,
W maternal' WOW pdor notice and wfbuf immniT4 any obligation to make such changes and modfications on Dumont poduds prewady
asutaequenty sold. Refs b the owners manual forwanarrty Monet,
DtSrmonr
A WATTS Brand
W l�n N vWHW2
£'la
A
AN�
.V. NN-•
Q
qLOi
_
Op�yNO�.p
,pPp�
�V
,p
.p
Cn'm��C.O
700
(Nli_
NVm�NWN
O0OJ
NP�Pbm
a
L�
a
.
a
Ono
�p
�.11om1
rn� � a
m a�5y5ynnn�awO
[�n+
Z, mC
CnOS O�
m
A N
10a�"�i'iw..
O.d
m
{�QJmpp��a
U�YnwG.�a-
o ,oN�gw_
O
pNp -�p�
(u��ON 0
�
P�00�0 �
� JOa
�'W-'A
V W
�
yn•
W fT p
PmA W V
dNa ON(Vj� �
my dNpp V A
n
p
`OP��NO
qF
N
saute r- i n r. aspwnc
Maximum Capacity of TracPipe C55T in Thousands of BTU per Hour Propane Gas
Min.Gas Pressure: 12-14 in w4
Pressure Drop: 2.0 In w.c
(Based on a 1.52 Specific Gravity / 2520 BTU per cubic foot Gas)
Tubing Length (feet)
.. . :. r ..
.
..1111IRN111111
..
•..
.t.
..
..
..
..r
..
3/8' 15
190 138
114
100 89 82 71 65 59 55 54 52 49 46
41
38
33
30
27
24
22
19
17
17
16
16
14
14
13
13
13
1/Y 19
427 306
252
218 196 179 157 139 128 119 116 111 104 100
90
82
71
63
59
51
46
41
38
36
35
32
30
30
28
27
27
1//4" 25
1069 763
625
545 488 446 388 348 318 294 285 277 261 249
222
204
177
158
146
127
112
103
95
90
84
81
76
73
71
68
66
T 31
1840 1309
1073
933 836 76S 663 595 543 503 488 472 445 423
380
347
301
269
247
214
192
176
163
152
144
136
130
125
120
116''
111
1'H39
3469 2467
2022
1756 1574 1438 1249 1119 1023 948 917 888 838 796
712
652
567
507
464
402
361
329
306
287
271
256
245
234
225
217
211
1`m 46
5711 4023
3277
2834 2532 2308 1997 1783 1626 1504 1452 1406 1325 1256
1123
1023
885
790
720
622
556
507
1469
1439 1
413
'391
374
358
344
331
318
2. 62
13073 9259
7568
6558 5869 5361 4645 4158 3797 3516 3398 3290 3103 2945
2635
2407
20B5
1867
1704
1477
1322
1206
1118
1047
986
936
893
855
822
792
763
Hotev MD(Equlvalent Hydnu1k01arnear) RNeoretluls ea khaffectsthehydmulkperformanceof NetuNn9 Itbnaawephysicalmeasure.
WsoumberisusedtocomprelndlvMual
siresbetween different manuleclure.
higher the END number Ne g waar the row capatlty d the piping.
1aDEe r-4 rropane Iv.ata.tan rrceem—
Maximum Capacity ofTracPipe CSST in Thousands of BTU per Hour Propane Gas
Min.Gas Pressure: 13.14 inw.e
Pressure Drop: 25 In W.C.
(Based on a 1.52 Specific Gravity / 2520 BTU per cubic foot Gas)
Tubing Length (feet)
..
...
..
:a.
•..
t..
..
..
•..
..
3/8" 15
222 159 131 114 102 93 81 73 67 62 60 58 55 52
46
43
36
33
30
27
24
22
21
19
17
17
16
16
14
14
14
1/2" 19
491 353 290 254 228 209 182 164 150 140 135 131 124 118
10B
97
85
76
70
57
51
46
43
40
38
36
35
33
32
30
30
3/4" 25
1192 850 698 606 545 497 432 388 355 329 318 309 291 277
249
226
198
177
161
141
127
116
106
100
95
90
85
82
79
76
73
1" 31
2512 1863 1720 1343 1106 976 883 825 771 719 696 673 632 596
533
470
398
352
320
239
214
196
182
169
160
152
146
139
133
128
125
1 'H' 39
3870 2753 2256 1959 1756 1605 1393 1249 1142 1058 1023 991 936 888
796
728
632
567
518
450
402
367
340
320
301
287
272
261
252
242
234
1tm 46
6393 4503 r$668 3173 2834 7584 2234 1997 1821 1685 1626 1574 1484 1406
1256
.1145
990
885
12085
806
697
622
568
526
491
462
1439
1418
401
385
370
358
2" 62
14609 10347 8456 7329 6558 5990 5192 4645 4243 3930 3797 3676 3467 3290
2945
2688
2331
1905
1650
1477
1349
1249
1168
1102
1047
997
955
918
885
B55
-Holes, Tabksahaselwlu&imwsfarfour90.de9r ndsand,vv dfittings. TuNsgrunswlthlargernumbeesol bendsandler fittings shall be lnoe3se4 by Ne equivalent kn9th of tubing tome fdtheingequatbn:
L=13n whx L Is Ne additlanal ImgM d lu dsg aiM n is Ne numbu d atltl hlonal fittings aM/or bmtli
�CXIO
V �Q.
30'*t IT'r4�p;P�
e
— U 's"
ST. LUCIE COUNTY
BUILDING DIVISION
REVIEWED
FOR COIYI on
REVIEWED BY
DATE
PLANS'ANIYPERMIT
MUST BE KEPT ON JOB OR
NO INSPECTION WILL BE MADE
-2,6' 3ly'fTla-c?;Fe
MIS 314 TI-1L V,?e
I �� �•,�,„¢e 5a1�a„,2e�
(�-IzGPP
hose.
rUe�
t�-- S 3Iy 4.rAve.,, -Le c
z^aS�y«CSVICJnr
)111 14"u,C,
36' 31Y` Path
.z56
Gallon
1-PTU I<
LI 3 Au3er
�-) 16 Ano,� I
15Tsi�c���c5ulc.�-ate
C�I u
25o
Lkr�4r5rour,�
1=veA 44G�``s Ca �� Zn�Uo� Cu►� �ovs� �� A,C
Ci 4-i r. 4zf rr1 t.n,
y32-0.C43
i
_Urq C i u S' U�
%,_ CC.n Esc % Msoor Lz)y-.6vs�;ov,
II
C,', r \roecx,0f ureCc Ci vab�� e FeeQ�ll
-011C iecjv,reL Y\o