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

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Dimensionless time θ<br />

1.0<br />

0.8<br />

0.6<br />

0.4<br />

0.2<br />

Exact solution<br />

PAM<br />

CLSA<br />

Exact solution<br />

Polynomial approximation method<br />

classical lumped system<br />

Dimensionless temperature τ<br />

51<br />

B=10<br />

Fig 4.11 Comparison <strong>of</strong> solutions <strong>of</strong> PAM, CLSA and Exact solution for a slab hav<strong>in</strong>g <strong>in</strong>ternal<br />

<strong>heat</strong> generation<br />

4.4 TABULATION<br />

Table 4.1 Comparison <strong>of</strong> solutions <strong>of</strong> average temperature obta<strong>in</strong>ed from <strong>different</strong> <strong>heat</strong><br />

<strong>conduction</strong> problems<br />

Average<br />

temperature<br />

θ<br />

Slab with <strong>heat</strong> flux Slab with <strong>heat</strong><br />

generation<br />

−Uτ<br />

⎛e + V ⎞<br />

θ = ⎜ ⎟<br />

⎝ U ⎠<br />

B<br />

U =<br />

1+<br />

B<br />

Where 3 ,<br />

Q<br />

V =<br />

1+<br />

B<br />

3<br />

− τU<br />

e + V<br />

θ =<br />

Where<br />

U<br />

U =<br />

B<br />

1+<br />

B<br />

3<br />

V =<br />

( )<br />

G<br />

( 1 ) B +<br />

3<br />

,<br />

Tube with <strong>heat</strong><br />

flux<br />

−Uτ<br />

⎛e + V ⎞<br />

θ = ⎜ ⎟<br />

⎝ U ⎠<br />

Where<br />

B<br />

U =<br />

( 4+ B)<br />

8<br />

,<br />

Q<br />

V =<br />

4+ B 8<br />

( )<br />

1<br />

Tube with <strong>heat</strong><br />

generation<br />

− τU<br />

e + V<br />

θ =<br />

U<br />

Where<br />

⎛<br />

2B<br />

⎞<br />

U = ⎜ ⎟<br />

⎜1+ B ⎟<br />

⎝ 4 ⎠ ,<br />

G<br />

V =<br />

( 1+<br />

B<br />

4)

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