Three distillation schemes for separating an equimolar, constant relative volatility $ABC$ mixture into nearly pure components are shown. The usual simplifying assumptions such as constant molal overflow, negligible heat loss, ideal trays are valid. All the schemes are designed for minimum total reboiler duty. Given ... of total reboiler duty is $I, II, III$ $III, I, II$ $II,I, III$ $III, II, I$
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Feb 24, 2019
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Arjun
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