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Process Equipment and Plant Design

Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

0.2 to 0.5 d
0.08 to 0.12 d
0.02 to 0.05 d
0.5 to 0.6 d

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

5.5
30.5
45.5
12.5

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Process Equipment and Plant Design
To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of

(1.2)3/2
(1.2)2/3
(1.2)3/5
(1.2)5/3

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

Lug
Saddle
Skirt
Bracket

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Process Equipment and Plant Design
for couplings and unions would be

200
60
Negligible
350

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Process Equipment and Plant Design
Baffles are provided in a shell and tube heat exchanger to increase the turbulence and velocity of the shell side fluid. Which of the following shaped baffles does not fall in the category of transverse baffle?

Disk type baffle
Segmental baffle
Helical type baffle
Flat plate extending across the wall

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