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Process Equipment and Plant Design

Process Equipment and Plant Design
In case of bubble cap distillation column of diameter greater than 1.2 metres, the cap diameter is roughly about __________ cms.

20
35
30
10

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Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Skirts
Columns
Saddles

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Process Equipment and Plant Design
Frame thickness in the plate and frame filter press is normally in the range of __________ inches.

1 to 12
0.25 to 4
1 to 5
0.25 to 8

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

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

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Process Equipment and Plant Design
Minimum baffle spacing recommended in a shell and tube heat exchanger is equal to

25 cms
5 cms
40% of the I.D. of the shell
I.D. of the shell

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Process Equipment and Plant Design
Stage efficiency for packed tower varies with the

All of these
Operating pressure and column diameter
Fluid rates and fluid properties
Type & size of packing

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