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Process Equipment and Plant Design

Process Equipment and Plant Design
Steam is preferred to be used as a heating medium in heat exchangers, because of its

Low cost
High film co-efficient
Non-corrosive condensate
High latent heat

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Process Equipment and Plant Design
Baffle width is normally taken as __________ times the tank diameter.

0.1-0.12
0.2-0.45
0.4-0.5
0.45-0.6

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Process Equipment and Plant Design
The safe distance of habitation from a hazardous chemical plant (TLV of its product < 1000 ppm) should be about __________ kms.

25
15
1
5

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Process Equipment and Plant Design
Two iron pipes of the same nominal diameter but different schedule numbers will have the same

Outside diameter
Wall thickness
None of these
Inside diameter

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

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Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Saddles
Skirts
Columns

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