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Heat Transfer

Heat Transfer
Reynold's analogy states that

Nst α f
NRe α f
Nst α NRe
NNu α f

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Heat Transfer
The Fourier number (defined as a.t/L²) is used in the analysis of problem involving heat transfer by

Natural convection
Steady state conduction
Forced convection
Transient conduction

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Heat Transfer
A composite flat wall of a furnace is made of two materials 'A' and 'B'. The thermal conductivity of 'A' is twice of that of material 'B', while the thickness of layer of 'A' is half that of B. If the temperature at the two sides of the wall are 400 and 1200°K, then the temperature drop (in °K) across the layer of material 'A' is

160
133
125
150

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Heat Transfer
In an extended surface heat exchanger, fluid having lower co-efficient

Flows through the tube
Should not be used as it gives very high pressure drop
Flows outside the tubes
Can flow either inside or outside the tubes

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Heat Transfer
Analogy between mass and heat transfer is not applicable in case of

Both B and C
Same velocity profile or equal eddy diffusivities
Viscous heating or chemical reaction
Thermal or pressure mass diffusion

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Heat Transfer
In a shell and tube heat exchanger, the shell side fluid velocity can not be changed by changing the

No. of baffles
Tube diameter
Tube pitch
Tube layout

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MORE MCQ ON Heat Transfer

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