Hot wastewater of a heat recovery system is flowing through a concrete conduct (k = 1.4 W/m-K) of square cross section. The flow section of the duct is 40 cm x 40 cm, and the thickness of the wall is 10 cm as shown in figure (next page). The average temperature of the hot water in the conduct is T, = 300°C. The conduct is %3D losing heat from its outer surface to the ambient air at T = 12°C by convection %3D with a heat transfer coefficient of h 35 W/m2 K. Using the finite difference %3D method with Ax = Ay = 5 cm and taking full advantage of symmetry: a) obtain the finite difference formulation of this problem for steady two- dimensional heat transfer. b) determine the temperatures at the nodal points of a cross section. c) evaluate the rate of heat loss for a 1-m-long section of the conduct.

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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Chapter10: Heat Exchangers
Section: Chapter Questions
Problem 10.28P
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Hot wastewater of a heat recovery system is flowing through a concrete conduct
(k = 1.4 W/m-K) of square cross section. The flow section of the duct is 40 cm x 40
%3D
cm, and the thickness of the wall is 10 cm as shown in figure (next page). The
average temperature of the hot water in the conduct is T, = 300°C. The conduct is
%3D
losing heat from its outer surface to the ambient air at T 12°C by convection
with a heat transfer coefficient of h = 35 W/m2 K. Using the finite difference
%3D
method with Ar Ay 5 cm and taking full advantage of symmetry:
a) obtain the finite difference formulation of this problem for steady two-
dimensional heat transfer.
b) determine the temperatures at the nodal points of a cross section.
c) evaluate the rate of heat loss for a 1-m-long section of the conduct.
Transcribed Image Text:Hot wastewater of a heat recovery system is flowing through a concrete conduct (k = 1.4 W/m-K) of square cross section. The flow section of the duct is 40 cm x 40 %3D cm, and the thickness of the wall is 10 cm as shown in figure (next page). The average temperature of the hot water in the conduct is T, = 300°C. The conduct is %3D losing heat from its outer surface to the ambient air at T 12°C by convection with a heat transfer coefficient of h = 35 W/m2 K. Using the finite difference %3D method with Ar Ay 5 cm and taking full advantage of symmetry: a) obtain the finite difference formulation of this problem for steady two- dimensional heat transfer. b) determine the temperatures at the nodal points of a cross section. c) evaluate the rate of heat loss for a 1-m-long section of the conduct.
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