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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

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

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

(d1 + d2)/d2
D1/(d1 + d2)
(d1 + d2)/d1
D2/(d1 + d2)

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Process Equipment and Plant Design
Which of the following packing materials provides for maximum mass transfer?

Raschig rings
Cross-partition rings
All of these
Lessig rings

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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.

Disk and ring
Orifice
Segmental
Independent of the type of

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Process Equipment and Plant Design
Stage efficiency for packed tower varies with the

All of these
Fluid rates and fluid properties
Type & size of packing
Operating pressure and column diameter

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Process Equipment and Plant Design
At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

Decreases
May increase or decrease depending upon the solubility of the gas in the liquid
Remains same
Increases

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