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Heat Transfer

Heat Transfer
Nusselt number for full developed, laminar, constant property flow in a pipe at uniform heat flux is

4.364
18
83
0.72

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Heat Transfer
In case of __________ boiling, the liquid temperature is below the saturation temperature and the boiling takes place in the vicinity of the heated surface.

Saturated
Nucleate
Local
Pool

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Heat Transfer
Heat transfer in the laminar sublayer in case of a liquid flowing through a pipe, is mostly by

Eddies current
Conduction
Convection
None of these

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

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

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Heat Transfer
The non-dimensional temperature gradient in a liquid at the wall of a pipe is the

Nusselt number
Schmidt number
Heat flux
Prandtl number

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Heat Transfer
Increasing the liquor level in the evaporator results in the

increase in liquor film co-efficient
decreased capacity
increased true temperature drop
decreased effect of hydrostatic head

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