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Process Equipment and Plant Design

Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

1.2-1.5
0.2-0.5
0.4-0.9
0.1-0.2

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Process Equipment and Plant Design
Power required for agitation depends upon the

Height & properties of the liquid
Size of agitator & the tank
Agitator type & speed of agitation
All of these

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Process Equipment and Plant Design
Length to diameter ratio of most rotary driers is in the range of

4 to 10
20 to 30
1 to 2
10 to 20

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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
For identical situation, condensing film coefficient in case of a horizontal condenser is almost __________ the value expected in case of vertical condenser.

Thrice
Twice
Five times
Half

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Process Equipment and Plant Design
The optimum size ratio for two mixed reactors in series depends on the kinetics of the reaction and the conversion level. For reaction orders more than one, the

Smaller reactor should come first
Larger reactor should come first
Equal sized reactors are the best
None of these

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