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Process Equipment and Plant Design

Process Equipment and Plant Design
In packed absorption tower, onset of flooding usually occurs at a pressure drop of about __________ mm of water column per metre height of packing.

50-75
750-1000
200-250
25-50

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Process Equipment and Plant Design
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.).

Conical
Ellipsoidal
Hemispherical
Dished

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Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

20-40
100-150
1000-1500
43835

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Process Equipment and Plant Design
Le/D for fully open globe value may be around

25
75
300
10

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Process Equipment and Plant Design
The safe distance of habitation from a hazardous chemical plant (TLV of its product < 1000 ppm) should be about __________ kms.

25
5
15
1

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

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

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