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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

18
34
6
24

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

Same as
Either more or less (depending upon relative volatility)
More than
Less than

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Process Equipment and Plant Design
Baffle spacing is generally __________ the I.D. of the shell.

More than
Not less than one fifth of
Both B and C
Not greater than

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Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Large diameter tanks
All of these
Small diameter tanks
Small diameter tall tanks

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

Inner
None of these
Outer
Approximate

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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

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

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