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VAPORTHERM F™ HEAT TRANSFER FLUID
VaporTherm F™ food grad heat transfer fluid is rated for service to 600F. The fluid is non-toxic and carries USDA certification for use in food processing plants. The high quality feedstock is formulated specifically for extended service. It has outstanding thermal stability under sustained high termperature operating conditions. The Vaportherm F fluid is non-corrosive to steel and other system materials and has a vapor pressure below atmospheric at its maximum rated operating termperature. These characteristics provide a long service life and low operating cost for both fluid and equipment, and allow Vapor Corporation to guarantee the heater coil for 10 years. The fluid is suggested for use in wide ranging applications including food processing and bulk transfer and storage, and in batch operation and continuous service in industrial process equipment. The fluid is easily disposed. It can be mixed with used lubricating oils and recycled locally.

Typical Physical Properties
Feedstock   Hydrocarbon
Appearance Clear
Taste & Odor   None
Maximum Bulk Temperature 600°F (316°C)
Maximum Film Temperature   640°F (338°C)
Flash Point (coc) ASTM D-92 345°F (174°C)
Fire Point (coc) ASTM D-92 385°F (196°C)
Autoignition ASTM E659-78 691°F (367°C)
Atmospheric Boiling Point,
10% Fraction
ASTM D-1160 650°F (343°C)
Coefficient of Thermal Expansion 0.00031/°F
Average Molecular Weight   350
Density, lb/gal @ 75°F (24°C) 7.25
Pour Point ASTM D-97   -45°F (-43°C)
Pumpability: Centrifugal @ 2,000 centipoise   -13°F (-25°C)
Heat of Vaporization (Calculated)   90.72 Btu/lb

Typical laboratory values, not guaranteed for all samples.

FLUID STORAGE
Do not allow water to collect on head of drum. If fluid must be temporarily stored out of doors, drum must be laid on side.

PRESSURE TESTING THE SYSTEM
Do not use water to pressure test system if at all possible. Consider inert gas.

CHARGING THE SYSTEM
Use small self-priming pump. Fluid should be added as close to pump suction as possible. Do not use main circulating pump. Open all block and control valves and all high point vents. Close vents when fluid comes out. Add until expansion tank is 1/2 full. Close block valve on pump discharge and start pump. Open valve one quarter open to allow fluid to circulate slowly through system. If pump does not cavitate after 5-10 minutes, open valve more. Increase valve opening until circulation can be maintained. If pump cavitates, shut down and add more fluid. Repeat as necessary until all air pockets have been removed. Fill system to appropriate level in expansion tank. DO NOT ALLOW PUMP TO OPERATE WITH VALVES WIDE OPEN UNTIL ALL AIR POCKETS HAVE BEEN ELIMINATED.

INITIAL STARTUP AND BOIL-OUT
Allow fluid to circulate at 220°F. Increase temperature in 5°F intervals. If pump begins to cavitate or fluid comes out of expansion tank, reduce temperature 3°F. Allow time for water to vent from expansion tank. Once system has stabilized, increase temperature 5°F. Repeat as necessary until system is stable. (This heat transfer fluid is immiscible with water. Allowed to stand, water will gravitate to the bottom of the mixture. Liquid water may be easily drained from the system's low point drain valves.)

THERMAL FLUID ANALYSIS
Heat transfer fluid should be analyzed after 6 months of operation and annually thereafter. Contact Vapor Corporation to arrange for these analyses.


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