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Process Equipment and Plant Design

Process Equipment and Plant Design
In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

Aa = Sa
Sa = 1.5 Aa
1.2 Aa = 1.2 Sa
Aa = 1.5 Sa

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Process Equipment and Plant Design
The retention time of material in a rotary dryer depends upon its

All of these
Rpm
Flights arrangement
Slope & length

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Process Equipment and Plant Design
The units of Young's modulus of elasticity and __________ are the same.

None of these
Stress
Modular ratio
Strain

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Cross
Reverse
Split
Cascade

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Process Equipment and Plant Design
Pressure drop due to pipe fittings can be estimated by the equation, ΔP/p = 4f.Le/D.V2/2gc, where, Le = equivalent length of straight pipeline which will incur the same frictional loss as the fitting and D = diameter of the fitting. The value of Le/D (dimensionless) for 45° elbow and 180° close return bends would be respectively around

5 and 10
45 and 75
300 and 500
180 and 300

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Process Equipment and Plant Design
The optimum size ratio for two mixed reactors in series depends on the kinetics of the reaction and the conversion level. For reaction orders more than one, the

Smaller reactor should come first
None of these
Larger reactor should come first
Equal sized reactors are the best

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