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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.).

Hemispherical
Dished
Conical
Ellipsoidal

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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
0.5 to 0.6 d
0.02 to 0.05 d

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the shell side cross flow area does not depend upon

Baffle spacing
Pitch
None of these
Clearance

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Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

1.5 to 2.5
5 to 10
0.01 to 1
10 to 20

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

0.95
0.75
0.55
0.85

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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.

24
18
6
34

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