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Process Equipment and Plant Design

Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Results in higher pressure drop per tray
Leads to high tray efficiency
Neither A nor B
Both A & B

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the 'tube pitch' is defined as the

None of these
Shortest centre to centre distance between adjacent tubes
Shortest distance between two adj acent tube holes
O.D. of the tube for square pitch

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Process Equipment and Plant Design
Maximum allowable vapour velocity in a bubble cap tower is determined by the

None of these
Vapour density
Entrainment considerations
Diameter of the column

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Process Equipment and Plant Design
A shell may by termed as thin if its thickness to diameter ratio is less than 0.1. The factor which can be neglected in the calculation of membrane stresses is

Shear
Bending
Elongation
Deformation

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G0.2
G0.5
G0.8
G1.5

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

Cross
Split
Cascade
Reverse

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