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Heat Transfer

Heat Transfer
In a liquid-liquid heat exchanger, for the same process temperature, the ratio of the LMTD in parallel flow to the LMTD in counter flow is always

> 1
< 1
1
∞

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Heat Transfer
Thickness of thermal boundary layer is more compared to that of hydrodynamic boundary layer, when the value of Prandtl number is

1
> 5
< 1
> 1

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Heat Transfer
Prandtl and Reynolds analogy are same, when Prandtl number is

0.5
1
1.5
> 2

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Heat Transfer
Kirchoff's law is applicable to

Monochromatic radiation only
Total radiation only
Only volumes and not to surfaces
Both A and B

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Heat Transfer
The thickness of condensate layer in filmwise condensation depends on the

Liquid flow rate from the surface
Surface configuration
Condensation rate
All of these

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Heat Transfer
For the same heat load and mass flow rate in the tube side of a shell and tube heat exchanger, one may use multipass on the tube side, because it

Decreases the pressure drop
Decreases the outlet temperature of cooling medium
Increases the overall heat transfer coefficient
None of these

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