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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

10000
1000
5000
3000

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Process Equipment and Plant Design
For a 25 mm hole drilled in plates to be rivetted, the shank diameter of the rivet should be __________ mm.

25
23
27
26

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Process Equipment and Plant Design
Bubble cap plate column is

Used only for distillation, not for absorption
A finite stage contactor
A differential stage contactor
A continuous contactor

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Reverse
Split
Cascade
Cross

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.1-0.2
1.2-1.5
0.4-0.9
0.2-0.5

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Process Equipment and Plant Design
Which of the following efficiencies can be greater than 100%?

Overall plate efficiency
Murphree plate efficiency
None of these
Point efficiency

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