Chromalox PQ410-4 User Manual

PQ410-4
161-048978-001
JULY, 2009
4 CES
SERVICE MANUAL
(Supersedes PQ410-3)
Electric Fluid Heat Transfer Systems
GENERAL
This Service Manual is furnished as an aid to help start-up and service Chromalox Heat Transfer Systems. Listed below are con­ditions which could occur during start-up and operation.
CAUTION: Hazard of Electric Shock. Any installa­tion involving electricity must be grounded to earth to eliminate shock hazard.
1. USE THE RIGHT HEAT TRANSFER FLUID
DO read manufacturer’s technical bulletins and instructions care­fully. Some heat transfer fluids may ignite or burn spontaneously if not properly used.
Chromalox Fluid Heat Transfer Systems are designed for a par­ticular heat transfer fluid or a class of heat transfer fluids. If you are not sure you are using an accepted heat transfer fluid, check with your local Chromalox sales and application engineering office listed on back cover or consult Chromalox Bulletin PQ301 for the correct heat transfer fluid.
DO NOT
mix heat transfer fluids unless authorized and approved
by the fluid manufacturer.
All heat transfer fluids are not compatible with each other, whether made by the same manufacturer or a different manufac-
turer. If you plan to switch fluids, check with the fluid manufac­turer to determine the following.
A. Is the new fluid compatible with the old? B. What is the recommended cleaning method to remove the old
fluid, its sludge, or any deposits remaining in the system?
C. Does the fluid manufacturer have a reclaiming service for used
fluid? Do they have a recommended procedure for disposal of used or old fluid?
CAUTION: To avoid possible damage to the heaters do not energize the heater unless the system is filled with fluid.
DO
provide for expansion and contraction of process piping and connections to the system. Piping strains can cause pump and motor mis-alignment, excessive wear on pump body, bearings and stuffing box packing or mechanical seal and will eventually cause failure of the pump and system.
Piping should be properly supported so pump can be removed without changing the position of the piping. If piping moves when the pump is removed, pump malfunction is probably due to stress­es and twisting caused by the piping. These stresses will multiply when the system is hot due to thermal expansion.
DO
provide sufficient cross sectional area in the process piping connections equivalent to the system pipes. In order to prevent undue pressure drop, maximum velocity in all piping should be less than 10 feet per second.
DO NOT
use process piping connections smaller than the pipes
used in the system.
If there is a high differential pressure between the inlet and out­let of the heat transfer system at operating temperature, this is probably due to a piping restriction. A continuing high differential
pressure can cause excessive wear on the pump and pump stuffing box packing or mechanical seal and will eventually cause prema­ture failure of the pump. The major causes of restrictions are:
A. Inlet and outlet pipes smaller than provided on the system. B. Piping many processes in series with one another. To reduce
the pressure drop of the system, equipment should be re-piped in balanced parallel flow.
2. PIPE STRAIN
3. PIPING RESTRICTIONS
C. The use of globe valves in the system. Globe valves have a
much higher pressure drop than gate valves. Therefore use globe valves only for balancing parallel flows.
D. Small inlet and outlet connections on customer’s process.
Examples being:
1. The use of small rotary unions on roll applications. These should be sized properly for the actual pumping rate to give minimum pressure drop.
2. Small inlet and outlet nozzles on jacketed vessels or the use of an agitating nozzle on the inlet of a jacketed vessel.
These should be sized properly for the pumping rate to give a minimum pressure drop.
3. The passageways or coring of a platen manifolded in series. These should be re-manifolded for parallel flow to give a minimum pressure drop.
DO
provide for bypass of oil when using pneumatic or electrical­ly operated process valves. System damage may occur if process piping return lines are restricted or blocked by closed valves.
3. PIPING RESTRICTIONS
4. PIPING GENERAL
5. AIR, WATER OR FOREIGN LIQUID IN THE HEAT TRANSFER FLUID
6. EXPANSION TANK LOCATION
DO mount expansion tank 15 feet above system.
Mount the expansion tank so it is the highest point in the sys­tem and if possible at least 15 foot above the height of the pump. To safeguard employees and equipment, run the vent line either out of the building or down into a 55 gallon drum. This vent line should be a minimum of
1
/2” internal pipe size.
CAUTION: To avoid possible rupture of expansion tank due to pressure, vent line should be checked on a regular basis to be sure it is always open to the atmosphere. Failure to do so may result in rup­ture of the expansion tank or other parts of the sys­tem causing injury or hazard of fire.
DO
install bleed valves on all process piping.
The presence of air in the system is indicated by a knocking or hammering of the pump. Air bleed valves should be provided at all high points in the system and every place where the heat transfer fluid flow drops in the vertical plain. These are the places where air pockets will form.
The presence of water (does not apply to water or water-glycol systems) in the system would not normally be noticed until a tem­perature above 212°F is reached. Its presence would be indicated in exactly the same manner as air in the system. Follow the air removal procedure.
CAUTION: During the initial start-up operation, the liquid level in the expansion tank must be checked
continually. This level should not exceed the three­quarter mark on the glass nor drop below the one­quarter mark. Note: If abnormal expansion of fluid is detect-
ed, this is probably due to a pocket of air or steam still present in the system. Check all bleed valves. If problem continues, de-ener­gize pump and check bleed valves.
Foreign liquids in the heat transfer fluid may not cause trouble immediately. However, after this system has been in operation for a period of time at the normal operating temperature, the foreign liquid could cause a chemical change in the heat transfer fluid which could lead to sludging, the formation of carbon on the heat­ing element and eventually, failure of the heating element and pump.
DO NOT
use Magnesium bed or porous insulations which can absorb oil. When oil soaked, these insulations may ignite sponta­neously and burn at temperatures as low as 400°F.
DO NOT
permit leaks of any heat transfer fluid to continue unat-
tended. Periodic inspection of piping and insulation is essential.
DO NOT
insulate expansion tank lines or the expansion tank. These components must be kept cool and below 130°F for most heat transfer oils. (See #6 Expansion Tank Location)
DO NOT
insulate flanges, valves or other connections which may
leak without being observed.
DO NOT
use screwed pipe connections on any piping over 1 inch diameter. Use flanges for connections with spiral wound or Grafoil
®
gaskets.
DO NOT
use Teflon tape or pipe seal on threaded connections on hot oil systems. Use Copalite
®
or SilverSeal®or other high tem-
perature sealants compatible with heat transfer oils.
DO
check all vent tubes, purge valves, and bypass relief valves at least once a month. All heat transfer oils oxidize in the presence of air and sludge can block critical piping. Blocked vent tubes may cause excessive system pressures and/or an explosion.
DO
retighten all bolted connections and joints at operating tem-
perature. Joints will expand and leak as they get hot. Check all
threaded connections on controls, gauges, etc. for leaks.
DO
vent all systems operating at atmospheric pressure properly. Vents must be rigid metal piping terminating outside the building or into a suitable container. The vent line should never be made of plastic, rubber or other low temperature material and should be
1
/2
inch or larger pipe.
WARNING: Oil saturated insulation on piping may ignite spontaneously at elevated temperatures. Repair leaks and replace oil soaked insulation immediately!!
-2-
Loading...
+ 4 hidden pages