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Process Equipment and Plant Design

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

Sieve plate
Packed
Bubble cap plate
None of these

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Process Equipment and Plant Design
In actual operation of distillation column, the vapour is not distributed uniformly among the bubble caps, primarily because of the

Small downcomer liquid seal
Lower skirt clearance
Lower static submergence
Liquid gradient on the tray

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering branch) would be

Both B and C
Around 90
More than that for Tee (used as elbow, entering run)
Less than that for Tee (used as elbow, entering run)

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

May increase or decrease depending upon the plate spacing
Increases
Remains same
Decreases

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Process Equipment and Plant Design
__________ dished head is the strongest of all.

Torispherical
None of these
Hemispherical
Elliptical

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

Large horizontal
Small horizontal
Tall vertical
Thick walled

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