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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum plate spacing in most of the pertroleum refinery distillation columns (of dia > 3 ft) is normally __________ inches.

6
18
34
12

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Thick walled vertical
None of these
Thin shperical (e.g. Horton sphere)
Horizontal

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

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

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Process Equipment and Plant Design
In case of a continuous distillation column, increase in reflux ratio may result in the

Lower fixed charges for the column
Greater cost for the reboiler heat supply
All of these
Greater cost for the condenser coolant

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Process Equipment and Plant Design
The ratio of lateral strain to linear strain is termed as the

Shear modulus
Bulk modulus
Modulus of elasticity
Poisson's ratio

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Improper layout of the equipments
Faulty operating procedures
Inadequate equipment design
Failure of equipments

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