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Process Equipment and Plant Design

Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Neither A nor B
Both A & B
Layout
Pitch

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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?

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

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Process Equipment and Plant Design
The minimum baffle height should be

Twice the tank diameter
Equal to the impeller diameter
3/4 of the tank height
Twice the impeller diameter

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Process Equipment and Plant Design
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.).

Ellipsoidal
Conical
Dished
Hemispherical

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Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

1000-1500
100-150
20-40
43835

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Process Equipment and Plant Design
Which of the following efficiencies can be greater than 100%?

Murphree plate efficiency
Point efficiency
None of these
Overall plate efficiency

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