A batch distillation system with a still pot and one equilibrium stage (two equilibrium contacts total) distills
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A batch distillation system with a still pot and one equilibrium stage (two equilibrium contacts total) distills a feed that is \(10.0 \mathrm{~mol} \%\) water and \(90.0 \mathrm{~mol} \% \mathrm{n}\)-butanol (see Table \(8-5\) for VLE data). \(\mathrm{p}=1.0 \mathrm{~atm}\). The charge is \(4.0 \mathrm{kmoles}\). The final still concentration is \(2.0 \mathrm{~mol} \%\) water. The system has a total condenser, and the reflux is a saturated liquid. \(\mathrm{L} / \mathrm{D}=\) \(1 / 2\). Find the final number of moles in the still pot and the average concentration of distillate.
Table 8-5
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Separation Process Engineering Includes Mass Transfer Analysis
ISBN: 9780137468041
5th Edition
Authors: Phillip Wankat
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