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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

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

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Process Equipment and Plant Design
Baffles may be eliminated for

Low viscosity liquids (< 200 poise)
Large diameter tanks
High viscosity liquids (> 600 poise)
None of these

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Process Equipment and Plant Design
In distillation columns, bubble caps are held in place over trays by

Both B and C
Rivets
Bolts
A hold down bar

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Process Equipment and Plant Design
The necessary wall thickness for a metallic storage vessel is a function of the

All of these
Diameter of the vessel
Ultimate tensile strength (or yield point) of the material and operating temperature
Operating pressure and welding/joint efficiency

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Increases linearly
Remains constant
Decreases very rapidly
Increases very rapidly

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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.

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

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