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

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U =<br />

θ =<br />

Where ( + B)<br />

54<br />

− τU<br />

e + V<br />

U<br />

B<br />

4 8<br />

V =<br />

G<br />

, ( 1 3 ) B +<br />

4. A long cyl<strong>in</strong>der subjected to <strong>heat</strong> generation at one side and convective <strong>heat</strong> transfer on<br />

the other side is considered for the <strong>analysis</strong>. Based on the <strong>analysis</strong> a closed form solution<br />

has been obta<strong>in</strong>ed.<br />

θ =<br />

− τU<br />

e + V<br />

⎛<br />

2B<br />

⎞<br />

G<br />

U = ⎜ ⎟ V =<br />

⎜1+ B ⎟<br />

Where ⎝ 4 ⎠ ( 1+<br />

B )<br />

, 4<br />

5. Based on the <strong>analysis</strong> a unique parameter known as modified Boit number obta<strong>in</strong>ed from<br />

the <strong>analysis</strong> and is shown <strong>in</strong> Table 2 and 3. With higher value <strong>of</strong> <strong>heat</strong> source parameter,<br />

the temperature <strong>in</strong>side the tube does not vary with time. However at lower values <strong>of</strong> <strong>heat</strong><br />

source parameters, the temperature decreases with <strong>in</strong>crease <strong>of</strong> time. With lower value <strong>of</strong><br />

Biot numbers, the temperature <strong>in</strong>side the tube does not vary with time. For higher value<br />

<strong>of</strong> Biot numbers, the temperature decreases with the <strong>in</strong>crease <strong>of</strong> time.<br />

5.2 SCOPE FOR FURTHER WORK<br />

1. Polynomial approximation method can be used to obta<strong>in</strong> solution <strong>of</strong> more complex<br />

problem <strong>in</strong>volv<strong>in</strong>g variable properties and variable <strong>heat</strong> transfer coefficients, radiation at<br />

the surface <strong>of</strong> the slab.<br />

2. Other approximation method, such as Heat Balance Integral method, Biots variation<br />

method can be used to obta<strong>in</strong> the solution for various complex <strong>heat</strong> transfer problems.<br />

3. Efforts can be made to analyze two dimensional unsteady problems by employ<strong>in</strong>g various<br />

approximate methods.<br />

U

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