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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

2 to 3
6 to 12
4 to 8
3 to 5

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

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

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Process Equipment and Plant Design
Which of the following factors determine the amount of entrainment in a distillation column?

Depth of liquid above the bubble cap slots
All of these
Plate spacing
Vapour velocity in the volume between the plates

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Process Equipment and Plant Design
For identical situation, condensing film coefficient in case of a horizontal condenser is almost __________ the value expected in case of vertical condenser.

Thrice
Twice
Five times
Half

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Independent of the type of
Segmental
Orifice
Disk and ring

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Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Thick spherical
Tall vertical
Thick walled vertical
Horizontal cylinderical

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