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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

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

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

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

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Be fabricated very easily
Withstand higher pressure for a given metallic shell thickness
Be supported very easily
Be designed without wind load considerations

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Process Equipment and Plant Design
for couplings and unions would be

350
Negligible
200
60

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

3 to 12.5
4 to 8
L to 3
12.5 to 18.5

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Process Equipment and Plant Design
Scale up problem in design based on the similarity concept takes into account __________ similarity.

All of these
Geometrical
Dynamic
Kinematic

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