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

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Process Equipment and Plant Design
Rivets are generally specified by the

None of these
Shank diameter
Overall length
Head diameter

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Process Equipment and Plant Design
__________ tray arrangement is recommended for distillation column having diameter upto 4 ft.

Split flow
Cross flow
Radial flow
Cascade

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Process Equipment and Plant Design
The optimum size ratio for two mixed reactors in series depends on the kinetics of the reaction and the conversion level. For reaction orders more than one, the

Larger reactor should come first
Equal sized reactors are the best
Smaller reactor should come first
None of these

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Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

√d
D
√(2πd)
√(2d)

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Process Equipment and Plant Design
A minimum clearance of about __________ mm is maintained between the distillation column wall and the bubble cap.

76
19
95
38

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