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Process Equipment and Plant Design

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

Dished
Hemispherical
Ellipsoidal
Conical

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Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

15000
2500
7500
1250

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

D2/(d1 + d2)
D1/(d1 + d2)
(d1 + d2)/d2
(d1 + d2)/d1

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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.

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

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Process Equipment and Plant Design
Which of the following material is seldom used for pressure vessel construction?

Mild steel
Killed steel
Rimmed still
Semi-killed steel

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Process Equipment and Plant Design
A claming section before the liquid flows into the downcomer is privided to

Permit release of entrained vapour in the liquid
Cool the liquid before it flows down
Ensure better vapour-liquid contact
Reduce the discharge fluctuation

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