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Process Equipment and Plant Design

Process Equipment and Plant Design
Normally, the length to diameter ratio of rotary dryers varies form 4 to 10 and for its economic operation, the number of transfer units (NTU) for such dryers varies from

1.5-2.5
3.5-5.5
44119
7.5-10.0

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Process Equipment and Plant Design
An adequate clearance between the tray and the shell wall of a distillation column is provided to

Avoid back-trapping
Drain the liquid from the tray when the unit is not in operation
Allow for thermal expansion and facilitate installation
None of these

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

Density of the fluid
None of these
Total cost considerations (pumping cost plus fixed cost of the pipe)
Viscosity of the fluid

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Process Equipment and Plant Design
To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of

(1.2)5/3
(1.2)3/5
(1.2)2/3
(1.2)3/2

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Lower limit of vapour velocity
Height of the plate spacing
Upper limit of the vapour velocity
Hole diameter of the seive tray

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Process Equipment and Plant Design
Which of the following is used to set the diameter of the distillation column?

Length of straight rectangular weir on cross-flow tray
Allowable vapour velocity
Number of theorectical plates
Static submergence

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