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Process Equipment and Plant Design

Process Equipment and Plant Design
Pressure drop (Δp) and the superficial gas mass velocity (G) in case of packed absorption tower operating in the preloading range are related as

Δp = 1/G0.6
Δp = G
Δp = G2
Δp = G0.5

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Process Equipment and Plant Design
The thermal stress in a metallic bar does not depend upon the

Both A & B
Changes in temperature
Cross-sectional area
Neither A nor B

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Process Equipment and Plant Design
Multiple blade paddle agitator is used for mixing high viscosity liquids/paste in which the paddle diameter is commonly 0.8 times the tank diameter. However, the width of the blade is in the range of __________ times the paddle diameter.

0.3 to 0.5
0.5 to 0.6
0.1 to 0.25
0.65 to 0.80

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Process Equipment and Plant Design
The ideal size of round bubble caps to be used in industrial distillation column having a diameter of 3-6 metres is __________ cms.

5
7.5
50
15

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Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

1.25-1.50 times
One-fourth of
Less than
2.5 times

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Process Equipment and Plant Design
Vertical vessels are not supported by

Columns
Brackets
Saddles
Skirts

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