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Heat Transfer

Heat Transfer
Natural convection is characterised by

Prandtl number
Peclet number
Reynolds number
Grashhoff number

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Heat Transfer
Steam side heat transfer co-efficient in an evaporator is in the range of __________ kcal/hr.m²°C.

100-500
5000-15000
1000-1500
18537

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Heat Transfer
Viscosity of gases __________ with increase in temperature.

Decrease slowly
Increase slowly
Increase very rapidly
Remain unaffected

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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 layout
Tube pitch

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Heat Transfer
Critical value of the __________ number governs the transition from laminar to turbulent flow in free convection heat transfer.

Both A & B
Grashoff
Prandtl & Grashoff
Reynolds

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Heat Transfer
Boiling point elevation of a solution of NaOH

Increases rapidly with temperature rise
Is almost independent of temperature
Is almost independent of pressure
Both B and C

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