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- W2057485222 abstract "Isobaric (101.32 kPa) liquid-vapour equilibrium data for the system 1-butanol + ethanol + 2-methoxy-2-methylpropane (MTBE) were determined and fitted with Wilson, NRTL and UNIQUAC equations, and their prediction by various group contribution methods (ASOG and modified and unmodified UNIFAC methods) was examined. The NRTL equation was used to calculate, by simulation, the influence of plate number and entrainer/feed flow ratio on the quantity and composition of the distillate afforded by extractive distillation of azeotropic MTBE + ethanol using 1-butanol as the entrainer. The quantity of distillate and its MTBE content both increased with plate number, and the quantity of distillate also increased with entrainer/feed flow rate ratio. Des données d'équilibre liquide-vapeur isobares (101,32 kPa) pour le système 1-butanol + éthanol + 2-méthoxy-2-méthylpropane (MTBE) ont été déterminées et calées aux équations de Wilson, NRTL et UNIQUAC, et leur prédiction par diverses méthodes de contribution des groupes (ASOG et méthodes UNIFAC modifiées et non modifiées) a été examinée. On a employé l'equation NRTL afin de calculer, par simulation, l'influence du nombre de plateaux et du rapport écoulement d'entrainement/écoulement d'alimentation sur la quantité et la composition du distillat permise par la distillation extractive de MTBE azéotrope + éthanol à l'aide de l-butanol come agent d'entraînement. La quantité de distillat et sa teneur en MTBE augmentent toutes deux avec le nombre de plateaux, et la quantité de distillat augmente également avec le rapport écoulement d'entraînement/écoulement d'alimentation." @default.
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- W2057485222 date "1999-12-01" @default.
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- W2057485222 title "Extractive distillation of 2-methoxy-2-methylpropane + ethanol using 1-butanol as entrainer: Equilibria and simulation" @default.
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- W2057485222 doi "https://doi.org/10.1002/cjce.5450770608" @default.
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