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Process Equipment and Plant Design

Process Equipment and Plant Design
Movement of pipeline caused by thermal expansion is taken care by providing

Expansion joint
Changes in its direction
Change in the shape of pipeline
All of these

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Process Equipment and Plant Design
Ratio of tube length to shell diameter for a shell and tube heat exchanger is

4 : 1 to 8 : 1 for liquid-liquid exchanger
< 4 : 1 for gas-gas exchangers
Both B & C
8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers

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Process Equipment and Plant Design
The buckling tendency of compression members is always in the direction of the

Axis of the load
Perpendicular to the axis of the load
None of these
Least radius of gyration

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

Decreases
Remains same
Increases
May increase or decrease depending upon the plate spacing

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Process Equipment and Plant Design
In which of the following evaporators, steam is fed inside the tube while the liquor is outside the tube?

Horizontal tube evaporator
Long tube vertical evaporator
None of these
Short tube vertical evaporator

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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
Less than
More than
Either more or less (depending upon relative volatility)

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