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Process Equipment and Plant Design

Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Large horizontal cylindrical
Tall but empty
Small
Thick walled tall

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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
None of these
Clearance
Pitch

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Much more than that for fully open globe valves
Around 7
Both B and C
Much less (say 2% than that for fully open globe valves)

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Process Equipment and Plant Design
In a shell and tube heat exchanger having triangular pitch, the shell side equivalent diameter is given by

4(0.86p² - πd²/4)/πd
(p² - πd²/4)/πd
4(0.86p² - πd²)/πd
(4p² - πd²/4)/πd

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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.

18
6
34
24

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Process Equipment and Plant Design
The maximum liquid gradient over a tray must not exceed

Half the tray spacing
0.5" -1.25"
5"
2"-3.5"

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