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Process Equipment and Plant Design

Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the shell side cross flow area does not depend upon

None of these
Clearance
Baffle spacing
Pitch

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Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

Less than
2.5 times
1.25-1.50 times
One-fourth of

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Process Equipment and Plant Design
The LMTD correction factor (FT) is applied in __________ heat exchangers.

Double pipe
1-1 cocurrent
All multipass
All 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 vapor phase reactor
A liquid phase reactor
A liquid phase catalytic reactor
Pot type reactor

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Process Equipment and Plant Design
With increase in the reflux ratio for a fixed production from a continuous binary distillation column, the __________ decreases.

Fixed charges initially
Running cost of steam for reboiler
Vapour & liquid load both
Running cost of cooling water for condenser

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Process Equipment and Plant Design
__________ dished head is the strongest of all.

None of these
Hemispherical
Elliptical
Torispherical

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