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Process Equipment and Plant Design

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

0.55
0.95
0.85
0.75

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Process Equipment and Plant Design
Le/D for fully open globe value may be around

300
25
10
75

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Process Equipment and Plant Design
The minimum baffle height should be

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

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Process Equipment and Plant Design
The thickness of segmental baffles (25 -35% cut truncated plates usually) is generally __________ the tube wall thickness.

Twice
Equal to
Four times
Half

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Process Equipment and Plant Design
In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)

4(P² - πd²/4)/πd
Πd/4P²
(P² - πd²/4)/πd
4P²/πd

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Process Equipment and Plant Design
The normal range of velocity of water in pipes is __________ m/sec.

1-2
15-30
0.1-0.5
10-50

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