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Process Equipment and Plant Design

Process Equipment and Plant Design
What is the slope of the feed line, if the feed to a distillation column is a saturated liquid?

∞
< 1
> 1

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Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

0.08 to 0.12 d
0.02 to 0.05 d
0.5 to 0.6 d
0.2 to 0.5 d

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Process Equipment and Plant Design
To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of

(1.2)2/3
(1.2)3/5
(1.2)3/2
(1.2)5/3

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Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Both A & B
Leads to high tray efficiency
Neither A nor B
Results in higher pressure drop per tray

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Process Equipment and Plant Design
Shell side heat transfer co-efficient in case of square pitch as compared to the triangular pitch under similar condition of fluid flow and tube size is

Twice
Less
More
Same

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Process Equipment and Plant Design
The main purpose of providing stepping on the trays is to

Increase the residence time
Improve the flow condition
Decrease the pressure drop
Facilitate handling of large flow rate of liquid

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