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Process Equipment and Plant Design

Process Equipment and Plant Design
For turbine agitator, the impeller diameter is about

0.3 to 0.5 d
0.95 d
0.1 to 0.2 d
0.65 to 0.85 d

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Process Equipment and Plant Design
Normal screwed fittings are used for pipes upto a diameter of __________ inches.

3
5
7
1.5

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

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Process Equipment and Plant Design
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is

1
∞
Minimum
0

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Thick walled vertical
Thin shperical (e.g. Horton sphere)
Horizontal
None of these

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Multipass shell and tube heat exchanger
Double pipe heat exchanger
Counter flow of hot and cold fluids
Fouling fluids

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