In: Mechanical Engineering
A 2 in schedule 40 pipe insulated with 1 in of 85% magnesia is carrying a fluid at 800°F. The insulated pipe passes through a room at 80°F, and the outside surface of the magnesia is at 100°F. Please calculate
The total heat loss per linear foot of pipe (in Btu/h),
The temperature of the inside wall of the pipe (in *F), and
The heat transfer coefficient between the fluid inside the pipe and the inside pipe wall (in Btu/h?ft2?F°).
The outside heat transfer coefficient is 10 Btu/h?ft2?F°.
Given,
2 in schedule 40 pipe
Therefore
Do = 2.375 in
Di = 2.067 in
t = 0.154 in
Insulation thickness, ti = 1 in
For 85% magnesia, thermal conductivity, km = 0.07 W/mK
We will use notations with respect to figure.
r1 = 1.0335 in = 0.0262509 m
r2 = 1.1875 in = 0.0301625 m
r3 = 2.1875 in = 0.0555625 m
km = 0.07 W/mK
ho = 10 Btu/h ft2oF = 56.744 W/m2K
T1 | 800 F | 426.667 C |
T2 | Unknown (to be found out 'T') | - |
T3 | Unknown | - |
T4 | 100 F | 37.7778 C |
T5 | 80 F | 26.6667 C |
Considering only the surface exposed to atmosphere,
For unit length,
Assuming the material of pipe as steel
ks = 19 W/mK
Now to find the temperature of inner surface of pipe,
For the inner surface of pipe,