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首页> 外文期刊>Physics and Chemistry of Liquids >Ternary liquid-liquid equilibria for mixtures of (ethanol plus toluene plus n-decane)
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Ternary liquid-liquid equilibria for mixtures of (ethanol plus toluene plus n-decane)

机译:(乙醇+甲苯+正癸烷)混合物的三元液-液平衡

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摘要

The data on the liquid-liquid equilibrium in (ethanol+toluene+n-decane) have been measured at three temperatures 298.15, 303.15 and 313.15 K and ambient pressure. Gas liquid chromatography has been employed, to determine the composition of the substances in liquid phases. The measured tie-line data are presented. The experimental ternary liquid-liquid equilibrium data have been correlated, using the Universal quasi chemical (UNIQUAC) and non-random tow-liquid (NRTL) activity coefficient models to obtain the binary interaction parameters of these components. Both the UNIQUAC and NRTL models, satisfactorily predict the equilibrium corn posit ions. The partition coefficients and the selectivity factor of the toluene extraction From n-decane mixtures were calculated and presented.
机译:在(乙醇+甲苯+正癸烷)中的液-液平衡数据已在三个温度298.15、303.15和313.15 K以及环境压力下进行了测量。已采用气相色谱法测定液相中物质的组成。显示了测得的联络线数据。使用通用准化学(UNIQUAC)和非随机拖液(NRTL)活度系数模型对实验三元液-液平衡数据进行了关联,以获得这些组分的二元相互作用参数。 UNIQUAC和NRTL模型都可以令人满意地预测平衡的玉米正离子。计算并给出了正癸烷混合物中甲苯萃取的分配系数和选择性因子。

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