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Process Equipment and Plant Design

Process Equipment and Plant Design
Heat transfer co-efficient for a horizontal condenser as compared to a vertical condenser operating under similar conditions is

About 0.33 times
About 3 times
Same
Less

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Process Equipment and Plant Design
Bubble cap plate column is

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

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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 is preferred to be used as a heating medium in heat exchangers, because of its

Low cost
High latent heat
Non-corrosive condensate
High film co-efficient

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Process Equipment and Plant Design
The distance between the centre of a rivet hole to the nearest edge of the plate is called

Margin
Back pitch
Pitch
None of these

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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
D
D⁹
D⁵

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