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Process Equipment and Plant Design

Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of

3000
10000
1000
5000

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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
Maximum allowable vapour velocity in a bubble cap tower is determined by the

Entrainment considerations
Vapour density
Diameter of the column
None of these

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Tall vertical
Thick walled
Large horizontal
Small horizontal

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

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

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Process Equipment and Plant Design
Cylinderical shell thickness of rotary drier is generally __________ mm.

43990
43864
44180
18-22

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