Mass Transfer
For water-ethanol system, the minimum reflux ratio

Cannot be computed
Is computed from the intercept of the operating line
Is the optimum reflux ratio
Is computed from the slope of the upper operating line that is tangent to the equilibrium curve

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Mass Transfer
Inside the distillation column, the

None of these
Driving force for the vapour flow is the pressure drop
Liquids are not always at their bubble points
Pressure increases gradually from bottom to the top of the column

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