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Process Equipment and Plant Design

Process Equipment and Plant Design
At equal mass velocities, the values of film co-efficients for gases as compared to that for liquids are generally.

Lower
Unpredictable
Same
Higher

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Process Equipment and Plant Design
For high pressure process equipments/vessels, the connected nozzle should be

Welded
Screwed
Flanged
Brazed

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Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

D
0.5 d
2 d
0.75 d

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Process Equipment and Plant Design
__________ closure is the weakest enclosure for cylindrical vessels.

Torispherical
Elliptical
Hemispherical
Conical or flat plate

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Double pipe heat exchanger
Multipass shell and tube heat exchanger
Fouling fluids
Counter flow of hot and cold fluids

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

Bubble cap plate
Sieve plate
Packed
None of these

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