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

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5.1 CONCLUSIONS<br />

CHAPTER 5<br />

CONCLUSIONS & SCOPE FOR FUTURE WORK<br />

An improved lumped parameter model is applied to the <strong>transient</strong> <strong>heat</strong> <strong>conduction</strong> <strong>in</strong> a long slab<br />

and long cyl<strong>in</strong>der. Polynomial approximation method is used to predict the <strong>transient</strong> distribution<br />

temperature <strong>of</strong> the slab and tube geometry. Four <strong>different</strong> cases namely, boundary <strong>heat</strong> flux for<br />

both slab and tube and, <strong>heat</strong> generation <strong>in</strong> both slab and tube has been analyzed. Additionally<br />

<strong>different</strong> temperature pr<strong>of</strong>iles have been used to obta<strong>in</strong> solutions for a slab. A unique number,<br />

known as modified Biot number is, obta<strong>in</strong>ed from the <strong>analysis</strong>. It is seen that the modified Biot<br />

number, which is a function <strong>of</strong> Biot number, plays important role <strong>in</strong> the transfer <strong>of</strong> <strong>heat</strong> <strong>in</strong> the<br />

solid. Based on the <strong>analysis</strong> the follow<strong>in</strong>g conclusions have been obta<strong>in</strong>ed.<br />

1. Initially a slab subjected to <strong>heat</strong> flux on one side and convective <strong>heat</strong> transfer on the other<br />

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

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

−Uτ<br />

⎛e + V ⎞<br />

θ = ⎜ ⎟<br />

⎝ U ⎠<br />

B<br />

Q<br />

U = V =<br />

1+<br />

B 1+<br />

B<br />

Where 3 , 3<br />

2. A long cyl<strong>in</strong>der subjected to <strong>heat</strong> flux on one side and convective <strong>heat</strong> transfer on the<br />

other side is considered for the <strong>analysis</strong>. Based on the <strong>analysis</strong>, a solution has been<br />

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

U =<br />

Where ( + B)<br />

−Uτ<br />

⎛e + V ⎞<br />

θ = ⎜ ⎟<br />

⎝ U ⎠<br />

B<br />

4 8<br />

53<br />

V =<br />

Q<br />

4 8<br />

, ( + B)<br />

3. A slab subjected to <strong>heat</strong> generation at one side and convective <strong>heat</strong> transfer on the other<br />

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

obta<strong>in</strong>ed.

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