首页> 外文期刊>The Journal of Chemical Thermodynamics >Isothermal (liquid + liquid) equilibrium data at T = 313.15 K and isobaric (vapor + liquid + liquid) equilibrium data at 101.3 kPa for the ternary system (water + 1-butanol + p-xylene)
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Isothermal (liquid + liquid) equilibrium data at T = 313.15 K and isobaric (vapor + liquid + liquid) equilibrium data at 101.3 kPa for the ternary system (water + 1-butanol + p-xylene)

机译:三元体系(水+ 1-丁醇+对二甲苯)的等温(液体+液体)平衡数据为T = 313.15 K,等压(蒸气+液体+液体)平衡数据为101.3 kPa

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摘要

The (vapor + liquid), (liquid + liquid) and (vapor + liquid + liquid) equilibria of the ternary system (water + 1-butanol + p-xylene) have been determined. (Water + 1-butanol + p-xylene) is a type 2 heterogeneous ternary system with partially miscible (water + 1-butanol) and (water + p-xylene) pairs. By contrast, (1-butanol + p-xylene) is totally miscible under atmospheric conditions. This paper examines the (vapor + liquid) equilibrium in both heterogeneous and homogeneous regions at 101.3 kPa of pressure. (Liquid + liquid) equilibrium data at T = 313.15 K have also been determined, and for comparison, the obtained experimental data have been calculated by means of several thermodynamic models: UNIQUAC, UNIFAC and NRTL. Some discrepancies were found between the (vapor + liquid + liquid) correlations; however, the models reproduced the (liquid + liquid) equilibrium data well. The obtained data reveal a ternary heterogeneous azeotrope with mole fraction composition: 0.686 water, 0.146 1-butanol and 0.168 p-xylene.
机译:确定了三元体系(水+ 1-丁醇+对二甲苯)的(蒸气+液体),(液体+液体)和(蒸气+液体+液体)平衡。 (水+ 1-丁醇+对二甲苯)是2型异质三元体系,具有部分互溶的(水+ 1-丁醇)和(水+对二甲苯)对。相反,(1-丁醇+对二甲苯)在大气条件下是完全可混溶的。本文研究了在101.3 kPa压力下非均质和均质区域中的(蒸汽+液体)平衡。还确定了T = 313.15 K时的(液体+液体)平衡数据,并且为了进行比较,还通过几种热力学模型(UNIQUAC,UNIFAC和NRTL)计算了获得的实验数据。在(蒸气+液体+液体)相关性之间发现了一些差异。但是,这些模型很好地再现了(液体+液体)平衡数据。获得的数据揭示了具有摩尔分数组成的三元均相共沸物:0.686水,0.146 1-丁醇和0.168对二甲苯。

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