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Process Equipment and Plant Design

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

Ultimate stress
Elastic limit
Yield stress
Breaking stress

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering branch) would be

More than that for Tee (used as elbow, entering run)
Both B and C
Around 90
Less than that for Tee (used as elbow, entering run)

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Process Equipment and Plant Design
The distance between the centre of a rivet hole to the nearest edge of the plate is called

None of these
Margin
Pitch
Back pitch

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Process Equipment and Plant Design
Ratio of tube length to shell diameter for a shell and tube heat exchanger is

8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers
Both B & C
4 : 1 to 8 : 1 for liquid-liquid exchanger
< 4 : 1 for gas-gas exchangers

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

Less than
More than
Same as
Either more or less (depending upon relative volatility)

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Process Equipment and Plant Design
Floating head heat exchangers are used for the

Cases where temperature difference between the shell and the tubes is more (>50°C)
Heat transfer between corrosive fluids
Counter-current heat transfer systems
Co-current heat transfer systems

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