Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
8th Edition
ISBN: 9781305387102
Author: Kreith, Frank; Manglik, Raj M.
Publisher: Cengage Learning
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A 1 in. o.d. (outer diameter) tube reactor is insulated with a 3 inch layer of asbestos. If the temperature of the outer surface of the insulation is 100 °F and the rate of heat loss per foot of reactor length is 50 BTU/hr, what must the temperature of the inside of the reactor be? [for asbestos, k = 0.105 BTU/hr ft °F]
a pipe with an outside diameter of 2.7 inches. insulate with a 2 inches. layer of asbestos (ka = 0.396 btu-in./hr-ft-F), followed by a layer of cork 1.5 inches. thick (kc = 0.30 btu-in/hrft-F). if the temperature of the outer surface of the cork is 91 F, calculate the heat lost per 100 ft of insulate pipe. The temp of the inner surface of the pipe is 275 F.
Required info: There is a 2.00 cm thick stagnant air pocket.
a) What thickness of cork would have the same R-factor as the stagnant air pocket? The thermal conductivity of air is 0.0230 W/m-K and of cork is 0.0460 W/m-K.
b) What thickness of tin would be required for the same R-factor as a 2.00-cm-thick stagnant air pocket?
The thermal conductivity of air is
0.0230 W/m:K and of tin is 66.8 W/m-K.
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