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Heat Transfer

Heat Transfer
Open pan evaporators are preferred to be used, when the solution to be concentrated is

Scaling
Highly viscous
Corrosive
Salty

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Heat Transfer
Shell side pressure drop in a shell and tube heat exchanger does not depend upon the

Viscosity, density & mass velocity of shell side fluid
None of these
Tube diameter & pitch
Baffle spacing & shell diameter

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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

Steady state conduction
Transient conduction
Forced convection
Natural convection

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Heat Transfer
The purpose of floating head in a heat exchanger is to

Facilitate its lengthening, if needed
Avoid buckling of tubes
Provide support for tubes
Decrease the pressure drop

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Heat Transfer
The radiation heat flux from a heating element at a temperature of 800°C, in a furnace maintained at 300°C is 8 kW/m². The flux, when the element temperature is increased to 1000°C for the same furnace temperature is

12.0 kW/m²
11.2 kW/m²
14.6 kW/m²
16.5 kW/m²

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Heat Transfer
Extremely large or small volumes of fluids are generally best routed through the shell side of a shell and tube heat exchanger, because of the

Less corrosion problems
High heat transfer co-efficient
Flexibility possible in the baffle arrangement
Low pressure drop

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MORE MCQ ON Heat Transfer

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