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Process Equipment and Plant Design

Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Both A & B
Layout
Neither A nor B
Pitch

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Process Equipment and Plant Design
Le/D for fully open globe value may be around

300
75
25
10

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Process Equipment and Plant Design
A 'rupture disc' is provided in chemical equipments as an accessory meant for

Relieving excess pressure
Avoiding vortex formation
Creating turbulence
Enhancing mixing rate

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Process Equipment and Plant Design
In distillation columns, bubble caps are held in place over trays by

A hold down bar
Both B and C
Bolts
Rivets

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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 P/A
4 A/P
A/P
√A

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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

D⁵
D
D⁹
D²

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