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Process Equipment and Plant Design

Process Equipment and Plant Design
Hazards associated with the relief valve leakage for extremely hazardous material storage can be taken care of by providing

Rupture diaphragm
Dikes
Surge chamber
None of these

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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)

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

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Process Equipment and Plant Design
In a distillation column, bubble caps are located on trays with a pitch of __________ times the outside diameter of the caps.

2.5
1.6 to 2
1.3 to 2
1.5 to 3

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Process Equipment and Plant Design
What is the value of 'q' for saturated vapor feed to a distillation column ?(where q = fraction of the feed stream that is liquid.)

1
> 1

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Upper limit of the vapour velocity
Hole diameter of the seive tray
Lower limit of vapour velocity
Height of the plate spacing

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Process Equipment and Plant Design
Which of the following factors affect the pressure drop in a co-current gas-liquid absorption packed tower?

Size, shape, orientation and surface of the packing particles
All of these
Density and viscosity of fluids
Fluid flow rates

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