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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is

∞
1
Minimum
0

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

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

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Process Equipment and Plant Design
The stress developed in a material without any permanent set is called the

Yield stress
Ultimate stress
Breaking stress
Elastic limit

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Process Equipment and Plant Design
Which of the following lengths of heat exchanger tubes are normally not used in practice?

0.5 metre
10 metres
2.5 metres
6 metres

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Process Equipment and Plant Design
Hold up of material in a operating rotary drier is in the range of

0.25 to 0.50
0.8 to 0.9
0.05 to 0.15
0.5 to 0.8

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