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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.

Packed
Bubble cap plate
Sieve plate
None of these

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Process Equipment and Plant Design
Corrosion allowance in the design of pressure vessel/chemical equipment is not necessary, if

Both B & C
Wall thickness is > 30 mm
Material of construction is high alloy steel
Plain carbon steel and cast iron parts are used

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Process Equipment and Plant Design
The dust collection efficiency of electrostatic precipitator increases with increase in the

Neither A nor B
Gas flow rate
Both A & B
Electrode area

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Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

Less
More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein
Same
More

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

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

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Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Skirts
Columns
Saddles

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