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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

18
6
24
34

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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
D²
D⁹
D

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Process Equipment and Plant Design
In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

Aa = Sa
1.2 Aa = 1.2 Sa
Aa = 1.5 Sa
Sa = 1.5 Aa

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

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Process Equipment and Plant Design
Wall thickness of schedule 40 pipe as compared to that of schedule 80 pipe is

Same
Cither A or B; depends upon the I.D. of the pipe
Less
More

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Process Equipment and Plant Design
Joint efficiency (J) for a seamless pipe is

1.2
< 0.5
1
0.85

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