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1-1
INTRODUCTIONProduct-IOM-2011-0216 SECTION 1
Overview
Prior to shipment, the following inspections and tests are
made to ensure the highest standards of manufacturing for
our customers:
§ Material inspections
§ Manufacturing process inspections
§ American Society of Mechanical Engineers (ASME)
welding inspection
§ ASME hydrostatic test inspection
§ Electrical components inspection
§ Operating test
§ Final engineering inspection
§ Crating inspection
This manual is provided as a guide to the correct operation
and maintenance of your Fulton equipment, and should be
read in its entirety and be made permanently available to the
sta responsible for the operation of the heater. It should not,
however, be considered as a complete code of practice, nor
should it replace existing codes or standards which may be
applicable. Fulton reserves the right to change any part of
this installation, operation and maintenance manual.
Installation, start-up, and maintenance of this equipment
can be hazardous and requires trained, quali ed installers
and service personnel. Trained personnel are responsible
for the installation, operation, and maintenance of this
product, and for the safety assurance of installation,
operation, and maintenance processes. Do not install,
operate, service or repair any component of this
equipment unless you are quali ed and fully understand
all requirements and procedures. Trained personnel
refers to those who have completed Fulton Service School
training speci c to this product.
Warnings & Cautions
WARNINGS and CAUTIONS appear in various chapters of this
manual. It is critical that all personnel read and adhere to all
information contained in WARNINGS and CAUTIONS.
§WARNINGS must be observed to prevent serious injury
or death to personnel.
§CAUTIONS must be observed to prevent damage
or destruction of equipment or loss of operating
e ectiveness.
All Warnings and Cautions are for reference and guidance
purposes, and do not substitute for required professional
training, conduct, and strict adherence to applicable
jurisdictional/professional codes or regulations.
Disclaimers and Local Codes
Installation of the equipment shall conform to all the
requirements or all national, state and local codes established
by the authorities having jurisdiction or, in the absence
of such requirements, in the US to the National Fuel Gas
Code ANSI Z2231/NFPA 54 latest edition, and the speci c
instructions in this manual. Authorities having jurisdiction
should be consulted prior to installation.
The boiler heat exchanger is manufactured and stamped
in accordance with ASME Boiler and Pressure Vessel Code,
Section I or Section VIII, Div. 1.
When working on this equipment, observe all warnings,
cautions, and notes in literature, on stickers and labels, and
any additional safety precautions that apply. Follow all safety
codes and wear appropriate safety protection. Follow all
jurisdictional codes and consult any jursidictional authorities
prior to installation.
Questions? Call (315) 298-5121, or visit us online at www.fulton.com
2-1
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
Unless otherwise noted, this heater is
certi ed for indoor installation only.
A competent rigger experienced in
handling heavy equipment should
handle rigging your equipment into
position.
The equipment must be installed on a
non-combustible surface.
Ensure all labels on the heater are
legible. All connections and safety
devices, both mechanical and
electrical, must be kept clean, with
ease of access for inspection, use and
maintenance.
Do not store or use gasoline or other
ammable vapors and liquids or
corrosive materials in the vicinity of
this or any other appliances.
Placement & Rigging
Proper placement of your Fulton Product (see Figures 1 and 2, and Tables 1
and 2) is essential. Attention paid to the following points will save a great deal
of di culty in the future. Correct placement is the rst step to trouble-free
installation, operation and maintenance.
Adhere to the following for equipment placement and rigging:
1. Consult authorities with jurisdiction over any national or local codes
(including but not limited to National Fire Protection Agency (NFPA),
American National Standards Institute (ANSI), Underwriters Laboratories
(UL), SCA, and ASME, which might be applicable to heater applications
before beginning.
2. Make appropriate determinations for placement, based on the following:
§Check building speci cations and Table 3 for permissible oor loading.
§Ensure the equipment is to be placed on a non-combustible level base
with adequate clearances from combustible materials. See Clearances &
Serviceability section.
§Locate heater as close as possible to the place where the heat will be used
in order to keep pipe work costs to a minimum.
§Ensure that there is adequate clearance around the unit to provide
access for operators and maintenance personnel to all parts of the
equipment. Ensure also that clearance provides for component removal for
maintenance. See Clearances & Serviceability section. The equipment
should be placed in a suitable heater house or well ventilated separate
room through which personnel do not normally pass. The layout should
eliminate tra c in potentially hazardous areas. For instance, the service
engineer or the operator should not have to pass exposed, hot pipe work
to make adjustments to the heater controls.
4 CAUTION
Do not allow weight to bear on
equipment components to prevent
damage.
2-2
§Ensure the equipment is to be placed in such a way that the electrical
components are protected from exposure to water or excessive humidity.
3. Determine rigging procedure, based on the following:
§Units are shipped upright and crated for forklift transport. Once uncrated,
all units can be transported with a forklift.
§If means of lifting are not available, place rollers beneath the frame of the
equipment for guidance to the position of where it is to be installed.
§Under no circumstances allow weight to bear on the jacket, control panel,
burner, fuel train or fan housing of any Fulton heater.
4. Install a 4 inch (102 mm) curb completely around the unit. In the event of a
large spill, this will help contain the uid.
Adhere to the following for equipment clearances and serviceability:
1. Ensure appropriate front, back, sides and top clearances are met. This
will allow access around the equipment to facilitate maintenance and a
safe work environment, and ensure technicians will commission the unit.
Technicians will not commence commissioning if hazardous conditions
exist.
2. Place heater with clearances to unprotected combustible materials,
including plaster or combustible supports, not less than the following:
§Heater Front 36” (1m)
§Heater Sides 18” (0.5 m)
§Heater Rear 18” (0.5 m)
§Flue Pipe 18” (0.5 m)
§Heater top (for burner removal) 36” (1 m)
NOTE: ´Burners may weigh up to 250 lbs (113 kg) depending on the type and
con guration.
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct, and strict
adherence to applicable jurisdictional/
professional codes and regulations.
Crystalline silica may be present in
components of this equipment. Exposure
to crystalline silica may pose signi cant
health hazards, including but not limited
to eye and respiratory system damage.
Per the Centers for Disease Control and
Prevention (CDC) and Occupational
Safety and Health Administration
(OSHA), appropriate Personal Protective
Equipment must be worn to minimize
exposure to hazardous substances. Refer
to most current guidelines o ered by the
CDC and OSHA for more information,
including Personal Protective Equipment
recommendations.
3. Pipes must not be run within 10” (254 mm) of any control cabinets or
combustible material.
4. Verify that all clearances are acceptable with the local ordinances.
Environment, Ventilation and Combustion Air
Requirements
Ventilation must be su cient to maintain a building temperature of 120 F (49 C)
or less. Consistent proper ventilation of the equipment room is essential for good
combustion.
NOTE: ´When calculating ventilation requirements, heat losses from the Fulton
equipment (and other equipment) should be considered.
Adhere to the following to meet ventilation and combustion air requirements:
1. Install two fresh air openings, one at a low level, 24” (610 mm) from the
oor, and one at a higher level on the equipment room wall. This will
provide a ow of air to exhaust the hot air from the equipment room.
2. Ensure the burner has an adequate supply of air. Based on NBIC
recommendations, unobstructed air openings must be sized on the basis
of 0.5 square inch of free area per 1,000 BTU/hr input maximum fuel
input of the combined burners in the equipment room or as speci ed by
applicable codes.
Failure to provide required and safe
access to the equipment could impede
commissioning and maintenance.
Service technicians are instructed not to
commence commissioning if hazardous
conditions exist.
Failure to provide proper minimum
clearances between equipment and
combustible materials may result in re.
Questions? Call (315) 298-5121, or visit us online at www.fulton.com
2-3
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
A
Legend
A Top Mounted Burner
B Electrical Control Panel
C Convection Fins
D High Density, High Temperature
Insulation
Notes
The top-mounted down red burner
delivers a spinning ame down the
length of the furnace. As the ame swirls
downward in a controlled ow pattern,
the uid spirals upward in the pressure
vessel. Hot gases from the ame are
carried up the outside of the vessel in
the secondary ue passage convection
area. Convection ns welded along the
full length of the vessel transmit the
remaining heat through the outer side
of the uid vessel and into the uid. The
result is even heating of thermal uids
for optimal thermal e ciency.
B
C
D
D
FIGURE 1 COMPONENT VIEW OF THE FTA THERMAL FLUID HEATER
Questions? Call (315) 298-5121, or visit us online at www.fulton.com
2-5
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct, and strict
adherence to applicable jurisdictional/
professional codes and regulations.
A quali ed installer, service agency or the
gas supplier must perform installation and
service on the fuel delivery system.
Do not use matches, candles, ame or
other sources of ignition to check for gas
leaks.
What to do if you smell gas:
Do not try to light the appliance.
Do not touch any electrical switch.
Do not use any phone in the building.
Leave building and contact gas supplier
from neighbor’s phone. If you cannot
reach gas supplier, phone the re
department.
TABLE 3 APPROXIMATE FLOOR LOADING*
ModelFree StandingSkid Mounted
FT-0200-A400250
FT-0380-A400250
FT-0520-A400200
FT-0690-A400250
FT-1050-A400300
FT-1740-A600400
*All weights are lbs/ft2
3. Ensure the equipment room air supply openings are kept clear at all
times.
4. See Table 4 for minimum make-up air required and the
recommended area of each opening for each model.
5. If positive forced ventilation is adopted, ensure that there will be no
appreciable pressure variation in the equipment room.
6. Avoid ventilation which creates a negative pressure in the building
as it will seriously a ect combustion and proper operation of the
stack. Please note that exhaust fans or similar equipment can create
a down draft in the chimney or starve the burner’s air supply. Either
case may result in poor combustion or nuisance failures.
When making gas piping joints, maintain
proper ventilation to reduce breathing
hazards.
An exhaust fan may draw products of
combustion into the work environment
creating a possible hazard to personnel.
4 CAUTION
It is essential that only fresh air be allowed
to enter the combustion air system. Foreign
substances, such as combustible volatiles
and lint in the combustion system can create
hazardous conditions. If foreign substances
can enter the air stream, the combustion air
inlet must be piped to an outside location.
Failure to do so will void the warranty.
To avoid failures due to poor combustion,
ensure make-up air system is properly
designed.
Some soap used for leak testing is corrosive
to certain types of metals. Clean all piping
thoroughly after completing the leak check.
TABLE 4 MINIMUM MAKEUP AIR REQUIREMENTS AND RECOMMENDED AREA OF
OPENING FOR VENTS
ModelMinimum Make-
Up Air (SCFM)*
FT-0200-A5011540
FT-0380-A9519565
FT-0520-A130290100
FT-0690-A175385130
FT-1050-A265585195
FT-1740-A435965325
*Minimum make-up air requirements are based on 25% excess air at high re.
**Opening areas are calculated based input of a single heater and do not account for the
ventilation needs of the equipment room. These measurements are subject to state and local
regulations.
Opening Area
(in2) Lower
Vent**
Opening Area
(in2) Upper Vent
NOTE: ´A properly designed make-up air system in the equipment room will
preclude these possibilities and is required to maintain proper combustion.
7. Eliminate potential for high risk situations for particulate matter to
be in the combustion air supply (e.g., as a result of construction and
maintenance activities).
Adhere to the following for gas supply (Figure 3) installation:
1. Install gas piping in accordance with all applicable
codes.
2. Ensure pipe and ttings used are new and free of dirt or
other deposits.
3. Ensure piping is of the proper size for adequate gas
supply to the gas head assembly. Consult your gas
company for speci c recommendations.
4. When making gas piping joints, use a sealing
compound resistant to the action of lique ed
petroleum gases. Do not use Te on tape on gas line
piping.
5. Ensure no piping stresses are transmitted to the
equipment. The equipment shall not be used as a pipe
anchor.
NOTE: ´Even when the unit is shut down, the gas supply
pressure must never exceed these values.
NOTE: ´When operating, the supply pressure must not drop
below these limits: Not less than 11 “ w.c. where 14” w.c is
required. Not less than 50” w.c. where 60” w.c. is required.
Not less than 100” w.c. where 120” w.c. is required.
11. After gas piping is completed and before wiring
installation is started, carefully check all piping
connections, (factory and eld), for gas leaks. Use a soap
and water solution.
¡ The Oil Supply
Fuel OilViscositySpeci c
Gravity
#2Less
than 31.9
Seconds
Redwood
#1 at 100 F
(38 C)
0.824 to 0.852
at 59 F (15 C)
Sulfur Content
Less than 0.40%
by weight
6. Ensure all vent connections on diaphragms, gas valves,
pressure regulators, and pressure switches (gas- red
units) are vented per local code.
7. On gas- red units with NFPA valve trains, ensure the
vent valve is piped to atmosphere per local code.
8. During any pressure testing of the system at pressures
in excess of 1/2 psig (14 inch W.C.)., disconnect the
heater at the heater manual shuto valve (located at
the end of the supplied gas train) from the gas supply
piping system.
9. Ensure the supply pressure is regulated by a nonstacking, tight, shut-o regulator.
10. Arrange gas piping so that it does not interfere with
any cover or burner, inhibit service or maintenance,
or prevent access between unit and walls or another
unit.The burner assembly and gas controls terminate
at a manual stop valve to which the gas supply should
be connected. Piping must be sized for a gas ow
consistent with the required BTU/Hr input. Large
pressure drops must be avoided. Fulton recommends
that the supply piping between the pressure regulator
and the inlet to the heater be kept to a minimum. The
minimum required gas pressure at the stop valve varies
with the model of heater. The requirements for FT-A
natural gas- red models are 7 to 11 in. w.c.
Adhere to the following for installation:
1. Fuel pipes must be of approved materials and of a
diameter suitable for the quantity of oil being delivered
to the burner and the static head available. See Figure
4.
2. Make fuel connection in accordance with the details on
the enclosed fuel pump cut sheet.
3. Ensure fuel oil piping is in accordance with local/
national requirements. In addition, if a two pipe system
is employed, a check valve must be tted into the return
pipe.
4. Meet the maximum pressure allowed at the fuel oil
pump inlet per the National Fire Protection Association
(NFPA).
NOTE: ´If for some reason the pressure of the fuel supply will
exceed NFPA maximum, tting a regulator to the fuel line
must be considered, e.g. when there is a tank situated with an
oil level eight feet (2.4 m) or more above the pump.
5. On units tted with NFPA 85 controls, ignition is
obtained by means of a gas pilot. A natural gas or LP
supply is required for these units. The required gas
supply pressure is 7” w.c. If a guaranteed supply of
natural gas is not available, then a supply of bottled
Questions? Call (315) 298-5121, or visit us online at www.fulton.com
gas at 11“w.c. is required. For details contact a local
liquid propane dealer.
Instrument Air
Instrument air provision for pneumatically actuated
control devices should meet the minimum and
maximum ow rate and delivery pressures speci ed by
the individual equipment. Additionally, it should be a dry,
dust free supply with a dew point of -40 F (-40 C).
Electrical Supply
Adhere to the following for electrical supply installation:
1. Install wiring and ground in equipment in
accordance with authority having jurisdiction
or in absence of such requirements the National
Electrical Code, ANSI/NFPA 70.
2. Provide a wall-mounted, fused disconnect sized for
the unit. This must be tted by the client/contractor
if disconnect is not supplied on the panel.
3. Size fuses according to motor name plates and
local electrical codes.
4. Connect power to the terminal strip as supplied on the
inside of the panel box.
NOTE: ´Single skid systems are generally shipped completely
prewired.
NOTE: ´The liquid level switch on the expansion tank, when
supplied, will be shipped in the parts box and must be
installed in the eld.
5. Determine multiple skid systems wiring requirements
(between the skids). Fulton will run conduit and wire
the devices on each skid. For the devices that have to
come down for shipping, the wire will be left at the end
of the conduit where possible and wired in the eld (by
others). When the system has multiple skids that are
adjoining, the conduit will be installed to break at the
skid joints. The wire for the conduit running between
the skids will be shipped loose to prevent damage
when the skids are put back together. These wires
will need to be run by the installing contractor in the
eld and wired to proper locations. If there is wiring
between skids that are not adjoining, then this will need
to be done by quali ed personnel.
Questions? Call (315) 298-5121, or visit us online at www.fulton.com
FIGURE 4 TYPICAL NO. 2 OIL FIRED FUEL TRAIN
2-9
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
NOTE: ´If the unit is not skid-mounted at the factory, the client/contractor is
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct, and strict
adherence to applicable jurisdictional/
professional codes and regulations.
required to wire the circulating / feed water pump starter.
NOTE: ´ If the circulating pump motor is not supplied by Fulton, the motor starter
will not be supplied.
6. Locate electrical schematic diagram, a copy of which is inside of the panel
box.
The vent line connection on the gas
pressure regulator must be piped to
outdoor air by the installer in accordance
with National Fuel Gas Code, ANSI Z2231-1991 or latest addenda. In Canada, gas
installations must be in accordance with
the current CAN/CGA B149.1 and 2 and/or
local codes.
Assure all electrical connections are
powered down prior to attempting
replacement or service of electrical
components or connections of the
equipment.
7. Ensure the information on the electrical drawing corresponds to your
voltage and frequency.
8. Adhere to the following:
§Typical 120 VAC controls allow for a +10% and -15% voltage uctuation.
§Motors are designed to operate within the following limits at the motor
terminals: AC power supplied is within +/- 10% of the motor rated voltage
with the rated frequency applied; or AC power supplied is within +/- 5% of
the rated frequency and with the rated voltage; or a combined variation
in voltage and frequency of +/- 10% (sum of absolute values) of rated
values provided the frequency variation does not exceed +/-5% of rated
frequency.
§For 3-phase motors, the line to line full load voltage must be balanced
within 1% of the rated motor voltage. If the motor is rated 208-230V, the
voltage deviations must be calculated from 230V. Operation outside of
these limits will degrade motor performance. 575V rated motors cannot be
operated at voltages above 600V. Depending on the motor manufacturer,
a 208V rated motor may not be able to run below the design voltage.
Thermal Fluids
2-10
¡ Thermal Fluids at Elevated Temperatures
Personnel must be familiar with the nature of potential hazards when working
with thermal uids at operating temperatures. Unlike steam or high-pressure
water systems, thermal uid attains extremely high temperatures without a
corresponding increase in pressure.
Adhere to the following:
1. Be aware that certain types of thermal uid may have operating
temperatures reaching 600 F (316 C) and above, so all exposed pipework is
hazardous and should be insulated.
2. Check that anged joints are tight during and after the rst warming up of
the system. Turn Burner and pump o before ttings are tightened. After
these checks, exposed hot anges, pumps, valves and ttings should be
tted with some sort of shield.
3. Remember that there is pressure generated in the system by the circulating
pump. Care should be exercised when opening any drain or vent valves in
the system. This is especially important during commissioning, when any
air trapped in the system is vented at high points, and when water, which
will ash into steam, is either expelled from the deaerator vent or drained
o at low points.
¡ Selecting a Thermal Fluid
The selection of the thermal uid most suited to your application is very
important. Factors to be considered include e ciency, thermal stability,
adaptability to various systems, and physical properties, including vapor
pressure, freezing point, and ash and re points.
Heat transfer uids of both mineral and synthetic origin have been specially
developed to give thermal stability over a very wide range of temperature. A
wide variety of thermal uids have been used successfully in Fulton Thermal
Fluid Heater systems, however, your nal selection should be made in
conjunction with recommendations from Fulton Thermal Corporation or the uid
manufacturer.
Consider the following for selection:
1. The Fulton vertical tubeless thermal uid heater is a red heat exchanger
and the safe control and monitoring of the thermal uid temperature is of
paramount importance.
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
4 CAUTION
Proper selection of thermal uid is
critical to system performance.
2. The safe maximum bulk temperature of the uid must be strictly adhered
to. The safe maximum temperature of the uid varies.
3. Special care must be taken when consulting uid manufacturers’ literature,
as maximum uid temperatures quoted are the actual limit to which any
of the uids may be subjected. It is important to remember that in any
red heater there exists a “ lm temperature” which is higher than the
temperature of the “bulk” of the uid. It is the BULK uid temperature and
NOT the FILM temperature that is indicated by the instruments.
4. As a general guide, the following list of uids that have given satisfactory
service over many years is provided. This is by no means a complete list.
Any uid speci cally designed for heat transfer use may be considered;
multipurpose oils are not acceptable.
§ AMOCO Transfer Oil 4199
§ CHEVRON
§ DOW G
§ EXXON 43
§ MOBIL
§ MONSANTO
§ MULTITHERM
§ PARATHERM
§ PETROCANADA T
§ SHELL
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2-11
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
If a re does occur, extinguish using
CO2 foam or dry chemical. DO NOT
USE WATER.
4 CAUTION
Some plastics can be dissolved by
thermal uid.
If excessive amounts of thermal
uid are vented from the system,
additional thermal uid may be
required in the system. Contact Fulton
for further information.
§ TEXACO
5. Any uid speci cally designed for heat transfer use must also exhibit these
characteristics:
§ Be a stable and homogenous liquid to a temperature of at least
100 F (38 C) over and above the maximum intended temperature
of utilization, compatible with metals used in the installation, and
tolerating contact with atmospheric air.
§ No solid matter in suspension.
§ Non-toxic in the case of leakage.
§ Su cient lubricity, i.e. not likely to cause seizure.
6. The thermal uid manufacturer must guarantee the characteristics of the
product, and verify that the uid bulk temperature limitation exceeds the
expected operating temperature
7. After a uid is selected, refer to the manufacturer’s recommendations,
published in compliance with the Occupational Safety and Health
Administration (OSHA).
8. If the uid expansion volume from 50 F to 600 F (10 C to 316 C) exceeds
20% of the initial uid volume, consult Fulton Thermal Corporation.
¡ Routine Analysis of Heat Transfer Fluid
Nearly all leading manufacturers of heat transfer uids provide an after
sales service to monitor the condition of the uid in operation and make
recommendations when replacement becomes necessary.
Each uid manufacturer has procedures for regular testing and analysis of the
uid. These usually allow for a sample to be taken and analyzed at least once a
year, although actual frequency will depend on operating temperature, number
of hours operated weekly, and the results of tests made during the rst weeks of
system operation.
Fulton Thermal Corporation recommends that the thermal uid in your system
be analyzed within the rst two months after startup and annually thereafter.
During the rst few months of operation, sampling may be carried out at
frequent intervals to con rm that system performance has been predicted
correctly.
If the supplier of your thermal uid does not contact you within four weeks of
commissioning, contact the supplier and make certain that the “ ll” is registered
for routine analysis.
¡ Thermal Fluid Breakdown
The possibilities of thermal uid breakdown are very slim in a typical closed loop
thermal uid system. Fulton’s combination expansion/deaerator/thermal bu er
tank creates a “cold seal” of uid that is slightly above ambient temperature. This
prevents oxidation that will otherwise happen when high temperature uid
Oxidation of the uid will also occur when hot thermal uid contacts air at a leak
in the system piping. Oxidized thermal uid becomes acidic and will damage the
thermal uid system. Thermal uid breakdown can occur in sections of piping
where there is a low ow condition. A low ow rate through the heater will result
in high lm temperatures leading to breakdown of the thermal uid.
} THERMAL FLUID BREAKDOWN PREVENTION
§Multiple pressure switches and a di erential pressure switch are used to
prevent this condition from occurring. See Figure 5. These safeties must
not be bypassed at any time.
§Exceeding the maximum operating temperature of the thermal uid will
also result in thermal uid breakdown. Fulton heaters are equipped with a
temperature limit switch (located on the front of the panel box) to prevent
this from occurring.
§A high temperature limit switch is an over temperature safety device.
If the high temperature limit shuts down the unit, the manual reset
button on the limit switch must be pressed. The reset button on the
ame programmer must also be pressed to reset the unit before it can be
restarted. See Figure 6. Refer to Maintenance section of this manual for
troubleshooting activities.
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
FIGURE 5 PRESSURE SWITCHES
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2-13
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
Non-Fulton product information is for
reference purposes only. No Fulton
document may substitute for full
review of documentation available
from the component manufacturer.
Piping Specifi cations
For piping, the basic considerations are: the design temperature, the pressure
retained by the pipe, the uid in the pipe, the load resulting from thermal
expansion or contraction, impact or shock loads imparted such as water hammer,
external loads, wind loads and vibration from equipment.
FIGURE 6 TEMPERATURE LIMIT DISPLAY
Adhere to the following for piping installation (see Figure 7):
1. Ensure the arrangement of the piping and its appurtenances takes into
consideration the location of other structures and equipment adjacent to
the piping, which may result in freezing interference and/or damage as a
result of expansion, contraction, vibration, or other movements.
2. Consider the appropriate location and orientation of valves necessary
for safe operation and isolation of the piping. Valves are used in piping
systems to stop and start the ow of uids, to regulate ow, to prevent the
back ow, and to relieve excessive pressure build up in the piping.
3. Ensure all piping and piping components are suitable for the design
temperatures, pressure and uid used in the system.
4. Ensure all components exposed to thermal uid ow, including pipe,
valves, and screens, are not copper, copper alloys, bronze, brass,
aluminum, or cast iron. Cast iron is porous to thermal uids, and copper
and aluminum act as catalysts in the degradation of some thermal uids.
Carbon or stainless steel, or ductile iron, are recommended.
5. Ensure all pipework is constructed from seamless mild steel pipe,
conforming to ASME SA 106B or SA 53B, Schedule 40, Schedule 80, or
equal, based on design temperature and pressure of the system.
2-14
6. If an isolating valve is completely closed, the pressure in the system will
rise to the deadhead pressure of the pump. Suitably sized pipe will enable
the system to withstand the total head generated by the circulating
pump, should this occur. In applications where it is desirable to design
to pressures lower than 100 psig, an alternative safeguard is to install
appropriately sized safety valves.
7. Where secondary circulating pumps are installed, ensure the system is
suitable for the aggregate head, against a closed valve, of both pumps.
8. During construction of the installation, ensure that no dirt, water, or
residue from welding is left in the system.
9. Consider expansion joints or pipe loops to accommodate thermal
expansion. Design should be per latest edition of ASHRAE Systems and
Equipment Handbook to prevent detrimental forces and stresses at
connected equipment. Thermal expansion should be calculated using the
maximum possible utilization uid temperature, regardless of whether the
pipe considered is in the feed or return circuit. Steel pipe will grow axially
and can be expected to expand approximately 1” over 100ft @ 100dg F
temperature rise (1mm per meter over 100 C rise).
10. Provide properly designed supports and anchors for all piping where
necessary to prevent undue stress from being imparted on equipment
such as pumps, valves and the heater. Care should be taken as end
reactions transmitted to rotating equipment, such as pumps, may deform
the equipment. Therefore equipment manufacturers’ recommendations
on allowable forces and movements should be followed. See Figure 8.
11. Ensure all pipe joints are of either welded or anged construction. Screwed
joints must be avoided where possible. In no instance should screwed
joints be used in the ow circuit. All anges should be welded to the pipe
and not screwed. Depending on the size, anges should be 150# or 300#
raised face anges, SA105.
12. Ensure heaters that are skid mounted with pumps and tanks are equipped
with a y-strainer, a ex connector and a valve in the inlet run between the
pump and the combination tank. Piping between the discharge of the
pump and the inlet of the heater will include a ex connector and a valve.
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
4 CAUTION
The weight of all piping must be
properly supported. Failure to support
piping may result in equipment
damage and/or system leakage.
Piping must take into consideration
potential for damage as a result of
expansion, contraction, vibration, or
other movements.
Dirt, water, and/or other debris in the
piping system after welding may result
in equipment failure.
13. If screwed connections have to be made, e.g., to items of control
equipment, use a thread sealant suitable for use with uids at elevated
temperature. Te on tape, standard pipe sealant, or hemp and paste are not
acceptable.
14. Cut screw threads carefully and accurately. If possible, new tools should
be used. Threaded connections larger than 1” are not to be used. It is
recommended that GR5 or higher tensile steel bolts be used for all anged
joints.
15. Use gaskets to make all anged connections. Gasketing material must be
suitable for use with the pressure, temperatures and uids in the system.
Flexible graphite gaskets are suited for most applications. Recommended
gasket thickness is 1/10 - 1/8 inch. Ensure that all bolts are tightened
evenly and to the torque recommended values provided by the gasket
manufacturer. Refer to Figure 9 and Tables 5-8 for guidelines.
NOTE: ´Typical gaskets used by Fulton include JM Clipper Elastograph gaskets and
Flexitallic gaskets. Adhere to installation instructions and torque requirements for
these gaskets.
16. Install high point bleeds at all high points in the system piping. 1/2” x 12”
Questions? Call (315) 298-5121, or visit us online at www.fulton.com
2-15
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
7
6
3
8
9
13
11
10
12
14
15
16
17
19
18
2
1
4
5
nipples welded in the top of the piping with ball valves
and plugs attached are to be used.
NOTE: ´It will save a considerable amount of time during the
cold ltration if the system piping is cleaned prior to assembly.
The mill scale (the results of oxidation) on the inside of the
piping as well as construction debris can foul the uid and
cause the need for the lters (strainers) to be cleaned more
than need be. This can range from simply using a rag to
ordering pickled pipe. (“Pickling” is a process where the piping
is rst soaked in an acid bath, then soaked in a neutralizing
bath, then given a protective oil coating.)
17. Install all pipes with a pitch to facilitate draining and
venting.
Legend
1. Thermal Fluid Heater
2. Thermal Fluid Circulating Pump
3. Safety Relief Valve
4. Thermometer
5. Pressure Gauge
6. Thermal Fluid Heated
Equipment
7. Bypass Valve
8. Expansion Joints
9. Anchor and Pipe Guides
10. Expansion Tank
11. Vent Piping
12. Deaerator Tank
13. Deaerator Tank Inlet (must be
highest point of piping)
14. Thermal Bu er Tank
15. Catch tank (for drain of
pressure relief valve, cold seal,
expansion tank, vent)
Pipe Support Must Be
Provided (Not To Be
Welded On Both Ends)
6 - 10 Pipe Diameters
1
2
3
4
5
6
7
8
FIGURE 8 TYPICAL PUMP PIPING
FIGURE 9 BOLTING SEQUENCE FOR 4 AND 8 BOLT FLANGES
Questions? Call (315) 298-5121, or visit us online at www.fulton.com
2-17
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
Non-Fulton product information is for
reference purposes only. No Fulton
document may substitute for full
review of documentation available
from the component manufacturer.
TABLE 5 - RECOMMENDED GASKET LOADS FOR FLEXITALLIC SPIRAL WOUND CLASS 150#
GASKETS SAE GRADE 5 BOLTS OR EQUAL
Nominal Flange
Size (in.)
1/241/245
3/441/245
141/245
1 1/44 1/2 45
1 1/2 4 1/2 45
2 4 5/890
2 1/24 5/890
3 4 5/890
3 1/285/890
485/890
583/4150
683/4150
883/4150
10127/8240
Number of BoltsDiameter of Bolts
(in.)
Preferred Torque
Req. Per Bolt (ft-lb)
TABLE 6 - RECOMMENDED LOADS FOR FLEXITALLIC SPIRAL WOUND CLASS 300# GASKETS
TABLE 7 - RECOMMENDED LOADS FOR JM CLIPPER ELASTOGRAPH 150# GASKETS SAE
GRADE 5 BOLTS OR EQUAL
Nominal Flange
Size (in.)
1/241/230
3/441/230
141/230
1 1/44 1/2 30
1 1/2 4 1/2 30
2 4 5/860
2 1/24 5/860
3 4 5/860
485/860
583/4100
683/4100
883/4100
10127/8160
TABLE 8 - RECOMMENDED LOADS FOR JM CLIPPER ELASTOGRAPH 300# GASKETS SAE
Number of BoltsDiameter of Bolts
(in.)
GRADE 5 BOLTS OR EQUAL
Preferred Torque
Req. Per Bolt (ft-lb)
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
Non-Fulton product information is for
reference purposes only. No Fulton
document may substitute for full
review of documentation available
from the component manufacturer.
Nominal Flange
Size (in.)
1/241/230
3/445/860
145/860
1 1/44 5/860
1 1/2 4 3/4100
2 8 5/860
2 1/283/4100
3 83/4100
483/4100
583/4100
6123/4160
8127/8245
10161160
Number of BoltsDiameter of Bolts
(in.)
Preferred Torque
Req. Per Bolt (ft-lb)
Questions? Call (315) 298-5121, or visit us online at www.fulton.com
2-19
INSTALLATIONFTA-IOM-2013-0227 SECTION 2
! WARNING
All information in this manual is for
reference and guidance purposes,
and does not substitute for required
professional training, conduct,
and strict adherence to applicable
jurisdictional/professional codes and
regulations.
Non-Fulton product information is for
reference purposes only. No Fulton
document may substitute for full
review of documentation available
from the component manufacturer.
To maintain a reasonable
temperature in the equipment area
and ensure safety to personnel, the
section of the chimney duct within
the building should be insulated.
Due to extremely high operating
temperatures of the thermal uid,
all exposed pipework should be
insulated, and exposed hot anges,
pump, valve, and ttings should be
shielded. Refer to Insulation section of
this manual for details.
Insulation
After the appropriate system tests have been satisfactorily completed
(see Testing section of this manual), all hot pipework and vessels must be
adequately insulated with material suited to the temperature and application
to prevent both heat loss and personnel injury.
Adhere to the following for insulation installation:
1. For inspection and maintenance purposes, leave pumps, anges, valves
and ttings uninsulated but suitably shielded for safety.
2. Insulate the deaerator section of the combination tank.
3. Do not insulate the thermal bu er and expansion sections of the
combination tank. On units operated with inert gas blankets above the
uid in the expansion tank, the entire combination tank, including the
expansion and thermal bu er sections, may be insulated but it is not
necessary.
4. Ensure hot oil pipe insulation is a minimum of 2” (51 mm) thick,
high temperature, laminated, foamglass cellular glass insulation as
manufactured by Pittsburgh Corning Corporation or equal.
System Interfaces
Proper selection and installation of the components in the hot oil system will
ensure proper and safe operation of the heater.
¡ Heater Connections
Adhere to the following for heater connections:
1. Connect the outlet of the pump directly to the inlet of the heater via
an isolating valve (preferably a throttling valve) and pump exible
connector.
2. Pipe heater outlets directly to the system via an isolating valve.
3. A safety relief valve may be shipped in the parts box accompanying
the fuel- red heater, and must be installed in the outlet manifold. On
all units, the outlet must be piped to a safe discharge area. The piping
from the outlet of the safety valve must be piped to a catch tank. The
discharge ow must not be restricted, i.e. no valve should be installed.
The weight of the piping must be properly supported in order to prevent
damage to the safety valve. If the valve body becomes warped, leakage
may result.
¡ Thermal Fluid Circulating Pump
Installing the pump in accordance with the manufacturer’s speci cations
and these instructions will prolong the life of the pump and contribute
signi cantly to the successful operation of your Fulton heater system. The