Page 114 - Fundamentals of The Finite Element Method for Heat and Fluid Flow
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STEADY STATE HEAT CONDUCTION IN ONE DIMENSION
106
equation in Equation 4.16. In the plane wall problems considered here, the cross-sectional
area A and convective surface area A s are equal.
The forcing vector can be written as
T T T
{f} e = G[N] d
− q[N] dA s + hT a [N] dA s (4.17)
A s A s
where G is the internal heat generation per unit volume, q is the boundary surface heat flux
and T a is the atmospheric temperature. If G = 0, then there is no heat generation inside
the slab. The no heat flux boundary condition is denoted by q = 0. If neither internal
heat generation nor external heat flux boundary conditions occur, then the finite element
equation for a homogeneous slab (Figure 4.3) with only two nodes becomes
k x A 1 −1 00 T i 0
+ hA = (4.18)
l −1 1 01 T j hT a A
The element equations can now be written for each slab of the composite wall shown
in Figure 4.2 separately and may be assembled. If we assume a discretization as shown in
Figure 4.4, we obtain the following element equations:
Element 1—(Slab 1)
k 1 A k 1 A
−
x 1 x 1 {f} 1 = qA (4.19)
;
k 1 A k 1 A 0
[K] 1 =
−
x 1 x 1
Element 2—(Slab 2)
k 2 A k 2 A
−
x 2 x 2 0
[K] 2 = ; {f} 2 = (4.20)
k 2 A k 2 A 0
−
x 2 x 2
Element 3—(Slab 3)
k 3 A k 3 A
−
x 3 x 3
0
[K] 3 = ; {f} 3 = (4.21)
k 3 A k 3 A hAT a
− + hA
x 3 x 3
1 1 2 2 3 3 4
q h, T a
x 1 x 2 x 3
L
Figure 4.4 Heat conduction through a composite wall subjected to heat convection on one
side and constant heat flux on the other side. Approximation using three linear elements