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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum baffle height should be

Twice the impeller diameter
3/4 of the tank height
Twice the tank diameter
Equal to the impeller diameter

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Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.95
0.55
0.85
0.75

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Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

45.5
30.5
5.5
12.5

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Process Equipment and Plant Design
The optimum size ratio for two mixed reactors in series depends on the kinetics of the reaction and the conversion level. For reaction orders more than one, the

Larger reactor should come first
None of these
Equal sized reactors are the best
Smaller reactor should come first

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Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

6
24
18
34

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

U-bend
Floating head tube sheet
Either A or B
Neither A nor B

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