A long pipe carries hot water and loses heat by convection to the surrounding air at Too=16 °C and h=20 W/(m2°C). The pipe has a thermal conductivity of k=1.7 W/(m°C), inner radius of r1=0.2 m and outer radius of r2-0.22 m. Assume that the inner surface temperature of pipe is T1-53°C. If there is no heat generation in the pipe material, calculate the outer surface temperature of the pipe T(r2), in °C, by considering steady one-dimensional heat transfer and constant thermal conductivity.

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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Heat mass transfer
A long pipe carries hot water and loses heat by convection to the surrounding air at Too-16
°C and h=20 W/(m2°C). The pipe has a thermal conductivity of k=1.7 W/(m°C), inner radius
of r1=0.2 m and outer radius of r2=0.22 m. Assume that the inner surface temperature of
pipe is T1=53°C. If there is no heat generation in the pipe material, calculate the outer
surface temperature of the pipe T(r2), in °C, by considering steady one-dimensional heat
transfer and constant thermal conductivity.
h, To
I2
Transcribed Image Text:A long pipe carries hot water and loses heat by convection to the surrounding air at Too-16 °C and h=20 W/(m2°C). The pipe has a thermal conductivity of k=1.7 W/(m°C), inner radius of r1=0.2 m and outer radius of r2=0.22 m. Assume that the inner surface temperature of pipe is T1=53°C. If there is no heat generation in the pipe material, calculate the outer surface temperature of the pipe T(r2), in °C, by considering steady one-dimensional heat transfer and constant thermal conductivity. h, To I2
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