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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffle width is normally taken as __________ times the tank diameter.

0.4-0.5
0.2-0.45
0.45-0.6
0.1-0.12

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Process Equipment and Plant Design
Bubble cap plate column is

A continuous contactor
A finite stage contactor
Used only for distillation, not for absorption
A differential stage contactor

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Process Equipment and Plant Design
Back-trapping in a distillation column results due to

High gas velocity
Excessive liquid gradient over the tray
Low reflux ratio
Low gas velocity

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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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Process Equipment and Plant Design
The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

4 A/P
4 P/A
A/P
√A

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Process Equipment and Plant Design
Steam economy is defined as the amount of evaporation per unit amount of steam used, while the capacity is the total evaporation obtained per hour. Use of multiple effect in evaporation

Increases economy
Does not affect the capacity
Increases capacity
Both B & C

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