Dry and saturated steam at 6 Mpa abs. enters a 40 m length of 11.5 cm O.D. steel pipe at a flow rate of 0.12 kg/s. The pipe is covered with 5 cm thick asbestos insulation (k= 0.022 W/m-k). The pipe is located in a tunnel with stagnant air temperature of 27 degree C. The unit outside convective coefficient is 10 W/m2K. Neglecting steam film and pipe wall resistances, determine the mass of steam.

Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
8th Edition
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Author:Kreith, Frank; Manglik, Raj M.
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Chapter7: Forced Convection Inside Tubes And Ducts
Section: Chapter Questions
Problem 7.32P
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Dry and saturated steam at 6 Mpa abs. enters a 40 m length of 11.5 cm O.D. steel pipe
at a flow rate of 0.12 kg/s. The pipe is covered with 5 cm thick asbestos insulation (k=
0.022 W/m-k). The pipe is located in a tunnel with stagnant air temperature of 27 degree
C. The unit outside convective coefficient is 10 W/m2K. Neglecting steam film and pipe
wall resistances, determine the mass of steam.
Transcribed Image Text:Dry and saturated steam at 6 Mpa abs. enters a 40 m length of 11.5 cm O.D. steel pipe at a flow rate of 0.12 kg/s. The pipe is covered with 5 cm thick asbestos insulation (k= 0.022 W/m-k). The pipe is located in a tunnel with stagnant air temperature of 27 degree C. The unit outside convective coefficient is 10 W/m2K. Neglecting steam film and pipe wall resistances, determine the mass of steam.
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