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Heat Transfer

Heat Transfer
Minimum recommended baffle spacing in a shell and tube heat exchanger is about (where, D = shell diameter)

0.5 D
0.3 D
0.2 D
0.4 D

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Heat Transfer
Log mean temperature difference (LMTD) cannot be used, if

none of the listed here
heat transfer co-efficient over the entire heat exchanger is not constant
the heat capacity is not constant and there is a phase change.
there exists an unsteady state

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

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

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Heat Transfer
Maximum water velocity in tubes of a 1-2 shell and tube heat exchanger may be around __________ metres/second.

20
30
1
10

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Heat Transfer
Multiple effect evaporation is generally recommended, when the

Evaporation on small scale is to be done
Corrosive liquids are to be concentrated
Fuel is cheaply available
Large scale evaporation of liquor is needed

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Heat Transfer
Prandtl number is the reciprocal of

Thermal diffusivity/Momentum diffusivity
Thermal diffusivity x Mass diffusivity
Thermal diffusivity x Momentum
Mass diffusivity x Momentum diffusivity

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