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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the baffles on shell side is primarily provided for

Fixing the tubes
Creating turbulence
Reducing scale deposition
Increasing pressure drop

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

Chain
Zig-zag
Diamond
None of these

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Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A liquid phase catalytic reactor
Pot type reactor
A liquid phase reactor
A vapor phase reactor

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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
In shell and tube heat exchangers, straight tie rods are used to

None of these
Hold baffle in space
Fix the tubes in position
Account for thermal strain

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