1. A high temperature steam line is covered with two successive layers of insulation. The layer in contact with the pipe is 1 ½ in. thickness of asbestos for which k is 0.08 Btu/hr .ft.°F. The asbestos is covered with a 1-in thickness if magnesia insulation, which has a value of 0.04. The internal pipe diameter is 2.90 in., the pipe wall thickness is 0.30 in. and k for the pipe is 26 Btu/hr.ft.°F. The steam temperature is 800°F, and the internal surface film coefficient is 40 Btu/hr . ft².°F , while the ambient outer temperature is 100 °F and the outer surface film coefficient is 1.2. Calculate (a) the value of U based upon the external area of magnesia covering, (b) the heat loss from the steam for a length of 180 feet of pipe, Btu/hr.

Elements Of Electromagnetics
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ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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1. A high temperature steam line is covered with two successive
layers of insulation. The layer in contact with the pipe is 1 ½ in.
thickness of asbestos for which k is 0.08 Btu/hr.ft.°F. The
asbestos is covered with a 1-in thickness if magnesia insulation,
which has a value of 0.04. The internal pipe diameter is 2.90 in., the
pipe wall thickness is 0.30 in. and k for the pipe is 26 Btu/hr.ft. °F.
The steam temperature is 800°F, and the internal surface film
coefficient is 40 Btu/hr.ft2.°F , while the ambient outer
temperature is 100 °F and the outer surface film coefficient is 1.2.
Calculate (a) the value of U based upon the external area of
magnesia covering, (b) the heat loss from the steam for a length of
180 feet of pipe, Btu/hr.
Transcribed Image Text:1. A high temperature steam line is covered with two successive layers of insulation. The layer in contact with the pipe is 1 ½ in. thickness of asbestos for which k is 0.08 Btu/hr.ft.°F. The asbestos is covered with a 1-in thickness if magnesia insulation, which has a value of 0.04. The internal pipe diameter is 2.90 in., the pipe wall thickness is 0.30 in. and k for the pipe is 26 Btu/hr.ft. °F. The steam temperature is 800°F, and the internal surface film coefficient is 40 Btu/hr.ft2.°F , while the ambient outer temperature is 100 °F and the outer surface film coefficient is 1.2. Calculate (a) the value of U based upon the external area of magnesia covering, (b) the heat loss from the steam for a length of 180 feet of pipe, Btu/hr.
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