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首页> 外文期刊>Fluid Phase Equilibria >Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 6. Total pressure data and G(E) for binary and ternary mixtures containing 1, 1-dimethlethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K
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Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 6. Total pressure data and G(E) for binary and ternary mixtures containing 1, 1-dimethlethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K

机译:汽油中辛烷增强添加剂的蒸气液平衡 - 6.含有1,1-二甲乙基甲基醚(MTBE),甲醇和正己烷的二元和三元混合物的总压力数据和G(e),313.15k

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摘要

Experimental isothermal P-x data at T = 313.15 K for the binary systems 1,1-dimethylethyl methyl ether (MTBE) + n-hexane and methanol + n-hexane, and the ternary system MTBE + methanol + n-hexane are reported. Data reduction by Barker's method provides correlations for G(E) using the Margules equation for the binary systems and the Wohl expansion for the ternary system. Wilson, NRTL and UNIQUAC models have been applied successfully to both the binary and the ternary systems. Moreover, we compare the experimental results for these binary mixtures to the prediction of the UNIFAC (Dortmund) model. Experimental results have been compared to predictions for the ternary system obtained from the Wilson, NRTL, UNIQUAC and UNIFAC models; for the ternary system, the UNIFAC predictions seem poor. The presence of azeotropes in the binary systems has been studied. (C) 2003 Elsevier B.V. All rights reserved. [References: 45]
机译:报道,T = 313.15K的实验等温P-X数据1,1-二甲基乙基甲基醚(MTBE)+正己烷和甲醇+正己烷,并报告三元体系MTBE +甲醇+正己烷。 Barker方法的数据减少提供了使用用于二元系统的Margules方程和三元系统的WOHL扩展的G(e)的相关性。 Wilson,NRTL和Uniquac模型已成功应用于二进制和三元系统。 此外,我们将这些二元混合物的实验结果与Unifac(多特蒙德)模型的预测进行了比较。 将实验结果与从威尔逊,NRTL,Uniquac和Unifac模型中获得的三元系统的预测进行了比较; 对于三元制度,统一性的预测似乎差。 研究了二元系统中的共沸存在。 (c)2003 Elsevier B.V.保留所有权利。 [参考:45]

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