There is no heat loss to surrounding, so
For ideal gases and in compressible fluids
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(8) |
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(9) |
Heat balance over a length of heat exchanger
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(10) |
is an overall coefficient for heat flow path consisting of a series of thermal resistances such tha
Here and are convective thermal resistance and is thermal resistance of the wall of thickness and of thermal conductivity due to conduction. Re-arrangement of equations 9 and 10 gives
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(12) |
And
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(13) |
|