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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

>1
< 1
Equal to the order of reaction
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

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

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Process Equipment and Plant Design
At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

Increases
Decreases
Remains same
May increase or decrease depending upon the solubility of the gas in the liquid

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the shell side cross flow area does not depend upon

None of these
Clearance
Pitch
Baffle spacing

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Process Equipment and Plant Design
Reflux ratio variation in a distillation column is between

Zero and one
Zero and infinity
None of these
Minimum and infinity

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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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