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Process Equipment and Plant Design

Process Equipment and Plant Design
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is

Minimum
0
1
∞

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the 'tube pitch' is defined as the

Shortest distance between two adj acent tube holes
O.D. of the tube for square pitch
Shortest centre to centre distance between adjacent tubes
None of these

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Process Equipment and Plant Design
Rivets are generally specified by the

Shank diameter
None of these
Head diameter
Overall length

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Process Equipment and Plant Design
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

D²
D⁹
D
D⁵

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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
0.4-0.9
1.2-1.5
0.2-0.5

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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
Low cost
Non-corrosive condensate
High latent heat

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