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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of down take area to cross-sectional area of the tube, for calendria type evaporator ranges from

1 to 1.5
1.5 to 2
0.5 to 1
2 to 2.5

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Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

2.5 times
1.25-1.50 times
One-fourth of
Less than

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Process Equipment and Plant Design
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

1.5 to 2
10 to 15
5 to 10
2.5 to 5

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Triangular pitch
Heat transfer rate is independent of tube arrangement
Diagonal square pitch
Square pitch

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Process Equipment and Plant Design
In inclined long tube vertical evaporators, the tubes are inclined at an angle of

90°
15°
45°
60°

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Process Equipment and Plant Design
Vertical storage vessels are never supported by __________ support.

Lug
Bracket
Skirt
Saddle

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