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Process Equipment and Plant Design

Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.55
0.95
0.99
0.8

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Process Equipment and Plant Design
The main purpose of providing stepping on the trays is to

Improve the flow condition
Decrease the pressure drop
Facilitate handling of large flow rate of liquid
Increase the residence time

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Process Equipment and Plant Design
Bubble cap plate column is

A continuous contactor
A differential stage contactor
Used only for distillation, not for absorption
A finite stage contactor

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Process Equipment and Plant Design
Lap joints are preferred for plates having thickness __________ mm.

> 5
43961
< 12.5
> 3

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Process Equipment and Plant Design
Which of the following material is seldom used for pressure vessel construction?

Mild steel
Semi-killed steel
Killed steel
Rimmed still

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Process Equipment and Plant Design
__________ closure is the weakest enclosure for cylindrical vessels.

Elliptical
Torispherical
Conical or flat plate
Hemispherical

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