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Process Equipment and Plant Design

Process Equipment and Plant Design
Nominal size of a pipe is an indication of its __________ diameter.

Outer
Approximate
Inner
None of these

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Process Equipment and Plant Design
Which of the following factors determine the amount of entrainment in a distillation column?

Plate spacing
All of these
Vapour velocity in the volume between the plates
Depth of liquid above the bubble cap slots

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

12.5 to 18.5
3 to 12.5
4 to 8
L to 3

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Independent of the type of
Disk and ring
Orifice
Segmental

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Heat transfer rate is independent of tube arrangement
Triangular pitch
Diagonal square pitch
Square pitch

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Faulty operating procedures
Failure of equipments
Improper layout of the equipments
Inadequate equipment design

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