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Process Equipment and Plant Design

Process Equipment and Plant Design
In a distillation column, the minimum residence time for liquid in the downspout is about __________ seconds.

1
80
180
8

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Process Equipment and Plant Design
Baffles may be eliminated for

Large diameter tanks
None of these
Low viscosity liquids (< 200 poise)
High viscosity liquids (> 600 poise)

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Process Equipment and Plant Design
The LMTD correction factor (FT) is applied in __________ heat exchangers.

1-1 cocurrent
All of these
All multipass
Double pipe

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

All of these
Back trapping
Gas blowing beneath cap skit
Maldistribution of gas

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Process Equipment and Plant Design
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

D²
D⁹
D⁵
D

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

4
2
1/2
8

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