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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

0.8
0.95
0.55
0.99

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Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

Less than arithmetic mean value
More than geometric mean value
More than arithmetic mean value
Both B & C

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

1.75
2.5
1.25
3.5

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Process Equipment and Plant Design
Typical static submergence for bubble cap plate column operating at atmospheric pressure may be around

5"
0.5"
50% of the plate spacing
2.5"

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Process Equipment and Plant Design
Low pressure steam (with saturation temperature between 105 to 120°C) is usually used in the vacuum evaporators, which normally employ a vacuum of about __________ mm Hg (referred to a 760 mm mercury barometer).

750
250
450
650

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Process Equipment and Plant Design
Baffle width is normally taken as __________ times the tank diameter.

0.45-0.6
0.4-0.5
0.1-0.12
0.2-0.45

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