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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the overall heat transfer co-efficient is proportional to the tube side (volumetric flow rate)0.8. This is valid, only when the ratio of the tube side film resistance to the total resistance is almost equal to

2
∞
20.8
1

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Process Equipment and Plant Design
The ratio of linear stress to linear strain is termed as the

Modulus of rigidity
Bulk modulus
Modulus of elasticity
None of these

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Process Equipment and Plant Design
What is the slope of the operating line in the stripping section of a distillation column?

?
> 1
< 1

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Process Equipment and Plant Design
In a shell and tube heat exchanger having triangular pitch, the shell side equivalent diameter is given by

(p² - πd²/4)/πd
4(0.86p² - πd²/4)/πd
(4p² - πd²/4)/πd
4(0.86p² - πd²)/πd

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Process Equipment and Plant Design
An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

An increase in relatived volatility for rectification columns
An increase in liquid viscosity
Decrease in gas solubility for absorbers
All of these

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