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Process Equipment and Plant Design

Process Equipment and Plant Design
Factor of safety (i.e., overdesign factor) in heat transfer equipments is about __________ percent more than the actual/theoretical design factor.

35-40
43961
15-20
30-35

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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
1.25
3.5
2.5

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Process Equipment and Plant Design
Generally, no corrosion allowance in wall thickness of a part is required, if the thickness is more than __________ mm.

20
5
30
10

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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

Minimum
∞
0
1

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

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

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.2-0.5
0.1-0.2
0.4-0.9
1.2-1.5

ANSWER DOWNLOAD EXAMIANS APP
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