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Process Equipment and Plant Design

Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

30.5
45.5
12.5
5.5

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

D²
1/D
1/D²
1/D⁵

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Process Equipment and Plant Design
In shell and tube heat exchangers, straight tie rods are used to

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

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Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Columns
Skirts
Saddles

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Process Equipment and Plant Design
Which of the following is not a graphical method (but is an analytical method) for the calculation of theoretical number of stages in case of continuous binary distillation?

McCabe-Thiele's method
Sorel-Lewis method
None of these
Ponchon-Savarit method

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Process Equipment and Plant Design
In a thin cylindrical shell, the hoop stress is __________ stress.

Compressive
Longitudinal
Radial
Circumferential tensile

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