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Process Equipment and Plant Design

Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Large horizontal
Thick walled
Tall vertical
Small horizontal

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

30.5
12.5
45.5
5.5

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G1.5
G0.8
G0.2
G0.5

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Process Equipment and Plant Design
Shortest distance between two tubes is

Called tube clearance
Called tube pitch
More in case of triangular pitch as compared to square pitch of tube layout
None of these

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Process Equipment and Plant Design
What is the slope of the feed line, if the feed to a distillation column is a saturated liquid?

< 1
∞
> 1

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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)

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

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