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Process Equipment and Plant Design

Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

< 30
> 7 < 15
< 7
> 20 < 50

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

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

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Much more than that for fully open globe valves
Much less (say 2% than that for fully open globe valves)
Both B and C
Around 7

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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/D²
1/D
1/D⁵

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Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

2
1
3.5
5.5

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Process Equipment and Plant Design
Which of the following is the most common type of baffle used in industrial shell and tube heat exchanger?

25% cut segmental baffle
75% cut segmental baffle
Orifice baffle
Disk and doughnut baffle

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