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Process Equipment and Plant Design

Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Leads to high tray efficiency
Both A & B
Results in higher pressure drop per tray
Neither A nor B

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Process Equipment and Plant Design
Flanges are connected to pipes by

Screwing
Brazing
All of these
Welding

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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
Bracket supports are the most suitable for supporting __________ vessels.

None of these
Thick walled vertical
Thin shperical (e.g. Horton sphere)
Horizontal

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Process Equipment and Plant Design
__________ heat exchanger is also known as 'hair pin type' exchanger,

Plate type
Double pipe
Regenerative
Finned

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Remains constant
Increases linearly
Decreases very rapidly
Increases very rapidly

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