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Heat Transfer

Heat Transfer
For what value of Prandtl number, St = f/2?

2
1.5
> 1
1

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Heat Transfer
Prandtl number is the reciprocal of

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

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Heat Transfer
What is the steam economy in case of a single effect evaporator system?

< 1
>1
0.1
1

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Heat Transfer
Fouling factor for a heat exchanger is given by (where, U₁ = heat transfer co-efficient of dirty surface U₂ = heat transfer co-efficient of clean surface)

1/U₂ - 1/U₁
U₁ - U₂
1/U₁ - 1/U₂
U₂ - U₁

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Heat Transfer
The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe, where the wall heat flux is constant, is

2.36
Dependent on NRe only
120.36
4.36

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Heat Transfer
__________ heat exchanger is the most suitable, when the temperature of shell side fluid is much higher than that of tube side.

Three pass, fixed tube sheet
None of these
U-tube
Single pass, fixed tube sheet

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