Dry saturated steam at 500 RK flows in a 20-cm I.D., 21 cm O.D. pipe. The pipe is covered with 8 cm of insulation that has a thermal conductivity of 0.10 W/m-K. The pipe's conductivity is 52 W/m-K. The ambient temperature is 300 2K. The unit convective coefficient on the inside is 18,000 W/m2-K. and the outside is 12 W/m2-K. Determine the heat loss from a pipe 4 m long. Calculate the overall coefficient of heat transfer based on the outside area

Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
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Author:Kreith, Frank; Manglik, Raj M.
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Chapter7: Forced Convection Inside Tubes And Ducts
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Problem 7.29P
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Dry saturated steam at 500 RK flows in a 20-cm I.D., 21 cm O.D. pipe. The pipe is covered with 8
cm of insulation that has a thermal conductivity of 0.10 W/m-K. The pipe's conductivity is 52
W/m-K. The ambient temperature is 300 2K. The unit convective coefficient on the inside is
18,000 W/m2-K. and the outside is 12 W/m2-K. Determine the heat loss from a pipe 4 m long.
Calculate the overall coefficient of heat transfer based on the outside area.
Transcribed Image Text:Dry saturated steam at 500 RK flows in a 20-cm I.D., 21 cm O.D. pipe. The pipe is covered with 8 cm of insulation that has a thermal conductivity of 0.10 W/m-K. The pipe's conductivity is 52 W/m-K. The ambient temperature is 300 2K. The unit convective coefficient on the inside is 18,000 W/m2-K. and the outside is 12 W/m2-K. Determine the heat loss from a pipe 4 m long. Calculate the overall coefficient of heat transfer based on the outside area.
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