Example: Multilayer cylindrical thermal resistance network Steam at T= 320 °C flows in a cast iron pipe [k = 80 W/ m.°C] whose inner and outer diameter are D, = 5 cm and D, = 5.5 cm, respectively. The pipe is covered with a 3 cm thick glass wool insulation [k = 0.05 W/ m.°C]. Heat is lost to the surroundings at T, radiation, with a combined heat transfer coefficient of h, = 18 W/m2. °C. Taking the heat transfer coefficient inside the pipe to be h, = 60 W/m2 K, determine the rate of heat loss from the steam per unit length of the pipe. Also determine the temperature drop across the pipe shell and the insulation. Assumptions: Steady state and one dimensional heat transfer. Solution: Taking L = 1 m, the areas of the surfaces exposed to convection are: %3D = 5°C by natural convection and %3D %3D %3D

Structural Analysis
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ISBN:9781337630931
Author:KASSIMALI, Aslam.
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Chapter2: Loads On Structures
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Example: Multilayer cylindrical thermal resistance network
Steam at T = 320 °C flows in a cast iron pipe [k = 80 W/
m.°C] whose inner and outer diameter are D, = 5 cm and D,
= 5.5 cm, respectively. The pipe is covered with a 3 cm thick
glass wool insulation [k = 0.05 W/ m.°C]. Heat is lost to the
surroundings at T, 5°C by natural convection and
radiation, with a combined heat transfer coefficient of h,
18 W/m2. °C. Taking the heat transfer coefficient inside the
pipe to be h, = 60 W/m2 K, determine the rate of heat loss
from the steam per unit length of the pipe. Also determine the
temperature drop across the pipe shell and the insulation.
Assumptions: Steady state and one dimensional heat transfer.
Solution: Taking L 1 m, the areas of the surfaces exposed to
convection are:
%3D
%3D
%3D
Transcribed Image Text:Example: Multilayer cylindrical thermal resistance network Steam at T = 320 °C flows in a cast iron pipe [k = 80 W/ m.°C] whose inner and outer diameter are D, = 5 cm and D, = 5.5 cm, respectively. The pipe is covered with a 3 cm thick glass wool insulation [k = 0.05 W/ m.°C]. Heat is lost to the surroundings at T, 5°C by natural convection and radiation, with a combined heat transfer coefficient of h, 18 W/m2. °C. Taking the heat transfer coefficient inside the pipe to be h, = 60 W/m2 K, determine the rate of heat loss from the steam per unit length of the pipe. Also determine the temperature drop across the pipe shell and the insulation. Assumptions: Steady state and one dimensional heat transfer. Solution: Taking L 1 m, the areas of the surfaces exposed to convection are: %3D %3D %3D
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