首页> 外文期刊>Fluid Phase Equilibria >Behaviour of butyl ether as entrainer for the extractive distillation of the azeotropic mixture propanone + diisopropyl ether. Isobaric VLE data of the azeotropic components with the entrainer
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Behaviour of butyl ether as entrainer for the extractive distillation of the azeotropic mixture propanone + diisopropyl ether. Isobaric VLE data of the azeotropic components with the entrainer

机译:丁醚作为共沸混合物丙酮+二异丙醚萃取蒸馏的夹带剂的行为。夹带剂共沸组分的等压VLE数据

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摘要

The behaviour of butyl ether as entrainer in extractive distillation for the rupture of the propanone + diisopropyl ether azeotropic mixture is investigated. The vapor-liquid equilibrium of each component with butyl ether has been carried out at 101.3 kPa in order to check the absence of azeotropes. Neither system showed an azeotrope. Thermodynamic consistency of the experimental data was good. The activity coefficients were correlated by means of the van Laar, Wilson, NRTL and UNIQUAC equations. UNIFAC prediction has been also used. As a final part, an experiment of extractive distillation was carried out and a composition of 0.990 in mole fraction of acetone, 0.001 of diisopropyl ether and 0.009 of butyl ether resulted in the head of the column. In conclusion, butyl ether is an excellent solvent for the rupture of the studied azeotropic mixture.
机译:研究了丁醚作为夹带剂在萃取蒸馏中破坏丙酮与二异丙醚共沸混合物的行为。为了检查不存在共沸物,已经在101.3kPa下进行了各组分与丁醚的气液平衡。两种系统均未显示出共沸物。实验数据的热力学一致性很好。活性系数通过van Laar,Wilson,NRTL和UNIQUAC方程进行关联。还使用了UNIFAC预测。最后,进行了萃取蒸馏的实验,在塔的顶部得到了0.990(摩尔)丙酮,0.001(二异丙醚)和0.009(丁醚)的组成。总之,丁基醚是研究共沸混合物破裂的极好溶剂。

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