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Process Equipment and Plant Design

Process Equipment and Plant Design
In chemical process equipments, the conical bottom heads used, usually has an apex angle of

20°
60°
80°
40°

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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 a double pipe concentric heat exchanger, the equivalent diameter of annulus for heat transfer would be (where, D₁ and D₂ are I.D. of inner and outer pipes)

(D₂² - D₁²)/D₁²
D₂ - D₁
(D₂² - D₁²)/D₂²
None of these

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Process Equipment and Plant Design
Smaller sized packings are generally dumped to the packed columns, and the large ones of size greater than __________ mm are stacked individually, which provides better control over bed porosity and offers lower gas pressure drop.

50
150
25
75

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

D²
1/D⁵
1/D²
1/D

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G0.2
G0.8
G1.5
G0.5

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