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analysis of transient heat conduction in different geometries - ethesis ...

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a + 2a<br />

=−Bθ<br />

1 2<br />

Subtract<strong>in</strong>g the equation (3.30) from (3.29) we get<br />

a<br />

2<br />

Bθ − Q<br />

=<br />

2 1<br />

( ε − )<br />

Substitut<strong>in</strong>g the value at equation (3.30) we have<br />

Us<strong>in</strong>g second boundary conditions we have<br />

( 1)<br />

( )<br />

25<br />

(3.33)<br />

(3.34)<br />

−Bθ ε − − Bθ −Q<br />

a1<br />

=<br />

ε − 1<br />

(3.35)<br />

⎛a1+ 2a2<br />

⎞<br />

a0 = −⎜ ⎟−a1−a2<br />

⎝ B ⎠ (3.36)<br />

Thus substitut<strong>in</strong>g the value <strong>of</strong> and at yhe expression <strong>of</strong> we get the follow<strong>in</strong>g value<br />

a<br />

0<br />

( − ) + B ( − ) + ( B −Q)<br />

2( ε −1)<br />

2θ ε 1 2 θ ε 1 θ<br />

=<br />

We may write the average temperature equation as<br />

Where m=1 for cyl<strong>in</strong>derical co-ord<strong>in</strong>ate<br />

Thus the above equation may be written as<br />

1<br />

m<br />

x dx<br />

mε θ = ∫ θ<br />

Substitut<strong>in</strong>g the value <strong>of</strong> and <strong>in</strong>tegrat<strong>in</strong>g equation (3.35) we get<br />

1<br />

(3.37)<br />

θ = ∫ θxdx<br />

ε<br />

(3.38)<br />

2 2 3 4<br />

⎛a0 a1 a2 ⎞ ⎛a0εa1εa1ε a2ε<br />

⎞<br />

θ = ⎜ + + ⎟−<br />

⎜ + + + ⎟<br />

⎝ 2 3 4 ⎠ ⎝ 2 2 3 4 ⎠ (3.39)<br />

is the ratio <strong>of</strong> <strong>in</strong>side diameter and outside diameter <strong>of</strong> the cyl<strong>in</strong>der<br />

2 2 3 4<br />

⎛a0εa1ε a1ε a2ε<br />

⎞<br />

⎜ + + + ⎟=<br />

0<br />

⎝ 2 2 3 4 ⎠ (3.40)<br />

Thus consider<strong>in</strong>g ε = 0 and substitut<strong>in</strong>g the value <strong>of</strong><br />

a0, a1, a 2 at equation (3.40) we get the<br />

value <strong>of</strong> θ as

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