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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of down take area to cross-sectional area of the tube, for calendria type evaporator ranges from

1 to 1.5
0.5 to 1
2 to 2.5
1.5 to 2

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

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Process Equipment and Plant Design
The main purpose of providing stepping on the trays is to

Improve the flow condition
Increase the residence time
Decrease the pressure drop
Facilitate handling of large flow rate of liquid

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

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

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the minimum shell thickness for carbon steel (inclusive of corrosion allowance) depends on shell diameter and is in the range of __________ mm.

43895
44183
44058
43962

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