Consider steady heat transfer in an L-shaped solid body whose cross section is given in Figure 5-26. The thermal conductivity of the body is k = 15 W/m · °C, and heat is generated in the body at a rate of g. = 2 x 106 W/m3. The left surface of the body is insulated, and the bottom surface is maintained at a uniform temperature of 90°C. The entire top surface is subjected to convection to ambient air at Too= 25°C with a convection coefficient of h= 80 W/m2 °C, and the right surface is subjected to heat flux at a uniform rate of q''R = 5000 W/m2. The nodal network of the problem consists of 15 equally spaced nodes with Ax=Ay=1.2 cm. Five of the nodes are at the bottom surface, and thus their temperatures are known. Obtain the finite difference equations at the remaining nine nodes and determine the nodal temperatures by solving them. Convection h, To -3+34 Ay Ay 1 4 10 2 5 3 6 12! 7 13 Ax= Ay=1 8 9 ÅR 14 15 90°C -Ax+Ax+Ax+AxAx- X

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Chapter2: Steady Heat Conduction
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EXAMPLE
Consider steady heat transfer in an L-shaped solid body whose cross section is
given in Figure 5–26. The thermal conductivity of the body is k = 15 W/m.
°C, and heat is generated in the body at a rate of g. = 2 × 106 W/m3. The left
surface of the body is insulated, and the bottom surface is maintained at a
uniform temperature of 90°C. The entire top surface is subjected to convection
to ambient air at Too= 25°C with a convection coefficient of h= 80 W/m2 . °C,
and the right surface is subjected to heat flux at a uniform rate of q'R = 5000
W/m2. The nodal network of the problem consists of 15 equally spaced nodes
with Ax=Ay =1.2 cm. Five of the nodes are at the bottom surface, and thus their
temperatures are known. Obtain the finite difference equations at the
remaining nine nodes and determine the nodal temperatures by solving them.
Convection
h, To
3
Ay
Ay
↓
2
5
Ax=Ay=1
6 789 R
10 |11| 12 13 14 15
tarta
90°C
Ax+AxAxAxAx+
FIGURE 5-26
Schematic for Example 5–3 and
the nodal network (the boundaries
of volume elements of the nodes are
indicated by dashed lines).
X
Transcribed Image Text:EXAMPLE Consider steady heat transfer in an L-shaped solid body whose cross section is given in Figure 5–26. The thermal conductivity of the body is k = 15 W/m. °C, and heat is generated in the body at a rate of g. = 2 × 106 W/m3. The left surface of the body is insulated, and the bottom surface is maintained at a uniform temperature of 90°C. The entire top surface is subjected to convection to ambient air at Too= 25°C with a convection coefficient of h= 80 W/m2 . °C, and the right surface is subjected to heat flux at a uniform rate of q'R = 5000 W/m2. The nodal network of the problem consists of 15 equally spaced nodes with Ax=Ay =1.2 cm. Five of the nodes are at the bottom surface, and thus their temperatures are known. Obtain the finite difference equations at the remaining nine nodes and determine the nodal temperatures by solving them. Convection h, To 3 Ay Ay ↓ 2 5 Ax=Ay=1 6 789 R 10 |11| 12 13 14 15 tarta 90°C Ax+AxAxAxAx+ FIGURE 5-26 Schematic for Example 5–3 and the nodal network (the boundaries of volume elements of the nodes are indicated by dashed lines). X
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