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Process Equipment and Plant Design

Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

√(2d)
√(2πd)
D
√d

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large reflux ratio
Low gas velocity
Resistance offered to flow of liquids by caps & risers and the flow of gas
Large plate spacing

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Process Equipment and Plant Design
Rivets are generally specified by the

Overall length
Head diameter
None of these
Shank diameter

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Horizontal
None of these
Thin shperical (e.g. Horton sphere)
Thick walled vertical

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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.

30
35
10
20

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Process Equipment and Plant Design
In a __________ rivetted joint, the rivets in the various rows are opposite to each other.

Diamond
Chain
Zig-zag
None of these

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