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Heat Transfer

Heat Transfer
Reynold's analogy states that

Nst α f
NNu α f
NRe α f
Nst α NRe

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Heat Transfer
The advantage of using a 1 - 2 shell and tube heat exchanger over a 1 - 1 shell and tube heat exchanger is

Lower shell side pressure drop
Higher tube side heat transfer co-efficient
Lower tube side pressure drop
Higher shell side heat transfer co-efficient

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Heat Transfer
Prandtl number is the reciprocal of

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

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

Schmidt number
Prandtl number
Heat flux
Nusselt number

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Heat Transfer
Which of the following has the lowest Prandtl number?

Dilute H₂SO₄
Transformer oil
Molten sodium (a coolant used in fast breeder reactor)
Water

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Heat Transfer
It is not preferable to use superheated steam in evaporators, because of its very

low film co-efficient
high temperature
high pressure
none of the listed here

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