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Process Equipment and Plant Design

Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Tall but empty
Thick walled tall
Large horizontal cylindrical
Small

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

Less than
Either more or less (depending upon relative volatility)
More than
Same as

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

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

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Process Equipment and Plant Design
Removable connection of tubes to tube sheet is called

Saddle
Nipple
Ferrule
Socket

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Process Equipment and Plant Design
In packed towers provided with saddle packing, liquid redistributors are positioned at every __________ times column diameter or 6 metres whichever is less.

43959
44119
43864
20-25

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

3.5
1.25
1.75
2.5

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