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Heat Transfer

Heat Transfer
Prandtl and Reynold's analogies are identical for Prandtl number value of

1
0.5
5

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Heat Transfer
For a liquid in laminar flow through a very long tube, when the exit fluid temperature approaches the wall temperature, the equation to be used is

Nu = Gz
Nu = 2Gz0.5
Nu = Gz
Nu = 0.023 Re0.8 . Pr0.4

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Heat Transfer
The actual temperature drop across the heating surface in an evaporator depends on the

Depth of liquid over heating surface
Pressure difference between steam chest and vapour space
Feed
All of these

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Heat Transfer
With increase in porosity, the thermal conductivity of a solid substance

Increases
May increase or decrease; depends on the solid
Remains unchanged
Decreases

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Heat Transfer
Heat flux through several resistances in series in analogous to the current flowing through several.

resistances in parallel
none of the listed here
resistances in series
capacitors in series

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Heat Transfer
Corrosiveness of steam condensate is due to the presence of

Neither A nor B
Dissolved O₂
CO₂
Both A & B

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