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Mass Transfer

Mass Transfer
The value of L/mG ratio for economical absorption operation ranges from

2.5 to 3.5
0.8 to 1.2
0.5 to 0.8
1.25 to 2.0

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Mass Transfer
Total reflux in a distillation operation requires minimum

Reboiler load
All of these
Condenser load
Number of plates

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Mass Transfer
Fenske-Underwood equation used for calculating the minimum number of theoretical plates in distillation column is valid for

Constant molal overflow
Constant relative volatility
All of these
Total reflux

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Mass Transfer
Air initially at 101. 3 kPa and 40°C and with a relative humidity of 50%, is cooled at constant pressure to 30°C. The cooled air has a

Higher dew point
Higher absolute (specific) humidity
Higher wet bulb temperature
Higher relative humidity

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Mass Transfer
In a binary distillation column, if the feed contains 40 mole % vapour, the q line will have a slope of

1.5
-1.5
0.6
-0.6

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Mass Transfer
For a binary mixture with low relative volatility, continuous rectification to get pure products will require

Small cross-section column
Less number of trays
Low reflux ratio
High reflux ratio

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MORE MCQ ON Mass Transfer

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