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