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Process Equipment and Plant Design

Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

1
2
3.5
5.5

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

Less than
Same as
Either more or less (depending upon relative volatility)
More than

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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.

3.5
2.5
1.75
1.25

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Process Equipment and Plant Design
The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

Equal to the order of reaction
< 1
>1
1

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Process Equipment and Plant Design
Speed of industrial paddle agitator ranges from __________ rpm.

500 to 750
1 to 5
1000 to 2000
20 to 100

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Process Equipment and Plant Design
Frame thickness in the plate and frame filter press is normally in the range of __________ inches.

0.25 to 8
1 to 5
1 to 12
0.25 to 4

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