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Process Equipment and Plant Design

Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.60-0.90
0.75-0.85
0.15-030
0.5-0.65

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Process Equipment and Plant Design
A minimum clearance of about __________ mm is maintained between the distillation column wall and the bubble cap.

76
19
38
95

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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.).

Hemispherical
Dished
Conical
Ellipsoidal

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

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

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Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

1
3.5
2
5.5

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Process Equipment and Plant Design
What is the minimum recommended ligament for square pitch arrangement in case of heat exchangers?

6.5 cms
6.5 mm
Equal to tube O.D
Equal to tube I.D

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