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chemical engineering process equipment and plant design
1. Smoker's equation for the calculation of number of equilibrium stages in a continuous binary distillation column is used, when the
(A): feed is not at its bubble point.
(B): number of equilibrium stages in only stripping section is to be calculated.
(C): number of equilibrium stages required is likely to be very small.
(D): relative volatility is close to one (e.g., separation of close boiling isomers).
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