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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

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

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Process Equipment and Plant Design
In actual operation of a bubble cap distillation tower, the __________ at the bottom of the tower is more than that at the top of the tower.

All of these
Pressure and temperature
Molal flow rate of vapour
Vapour molecular weight

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Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

None of these
Tall but empty
Tall (say 30 metres), but is full of liquid
Short (< 2 m) and housed indoor

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Process Equipment and Plant Design
The testing pressure of storage tanks and pressure vessels designed as per Indian standard codes should be about __________ times.the design pressure.

1.5 to 2
4 to 5
>5
3 to 4

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Process Equipment and Plant Design
In seive plate column, holes are drilled or punched in sizes ranging from 2.5 to 12 mm (5 mm being widely used). The hole pitch is normally __________ times the hole diameter to give the required hole area.

10 to 15
2.5 to 4.0
5 to 10
0.5 to 1.5

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Remains constant
Decreases very rapidly
Increases linearly
Increases very rapidly

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