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Process Equipment and Plant Design

Process Equipment and Plant Design
Heat transfer co-efficient for a horizontal condenser as compared to a vertical condenser operating under similar conditions is

Less
About 0.33 times
About 3 times
Same

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Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

6 to 12
3 to 5
4 to 8
2 to 3

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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
Packed
Sieve plate
None of these

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Thick walled vertical
None of these
Horizontal
Thin shperical (e.g. Horton sphere)

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Process Equipment and Plant Design
In a distillation column, bubble caps are located on trays with a pitch of __________ times the outside diameter of the caps.

2.5
1.6 to 2
1.5 to 3
1.3 to 2

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Process Equipment and Plant Design
Needle valves are generally not used for

High pressure throttling service
Smaller sizes of pipe
Very accurate flow control
Very large diameter pipes

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