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An experimental study of the viscometric and volumetric properties of octane-pentadecane n-alkane binary and ternary systems at several temperatures.

机译:在几个温度下辛烷-十五烷正构烷烃二元和三元体系的粘度和体积性质的实验研究。

摘要

The viscosities and densities of five ternary C$sb8$-C$sb{15}$ n-alkane liquid systems and their corresponding eight binary subsystems have been measured at 293.15, 298.15, 308.15 and 313.15 K over the entire composition range. The experimental and literature viscosity data were used to test and modify some existing viscosity predictive models. The technique proposed earlier by Asfour et al. (1991) for the prediction of the dependence of viscosities of binary n-alkane systems on composition has been extended to cover ternary mixtures. A pseudo-binary mixture model has been developed in this study to modify the Generalized Corresponding States Principle (GCSP) proposed earlier by Teja and Rice (1981) for either prediction or correlation of the viscosity of liquid mixtures. The proposed modification of the GCSP method has the following advantages for n-alkane liquid mixtures having more than two components: (i) for the prediction of mixture viscosities, it does not require the selection procedure of reference fluids, thus eliminating the possible significant errors resulting from such a selection; (ii) for the correlation of mixture viscosities, it reduces the number of the binary interaction coefficients to one, no matter how many components are in a system. Obviously, this results in substantial cost and time savings. Two equations are proposed in this study as supplements to the original GCSP to make it more efficient; viz. (i) the first equation is concerned with the prediction of the interaction coefficient of the binary n-alkane systems from the pure component properties, (ii) the second equation provides a technique for the appropriate reference fluid selection when the original GCSP method is used for the viscosity prediction of ternary n-alkane liquid systems. Some literature excess property models have also been subjected to testing by using the excess property data calculated from the experimental viscometric and volumetric properties obtained in this study.Dept. of Chemistry and Biochemistry. Paper copy at Leddy Library: Theses u26 Major Papers - Basement, West Bldg. / Call Number: Thesis1992 .W955. Source: Dissertation Abstracts International, Volume: 53-12, Section: B, page: 6430. Supervisor: Abdul-Fattah A. Asfour. Thesis (Ph.D.)--University of Windsor (Canada), 1992.
机译:在整个组成范围内,五个三元C $ sb8 $ -C $ sb {15} $正构烷烃液体系统及其相应的八个二元子系统的粘度和密度已测量为293.15、298.15、308.15和313.15K。实验和文献粘度数据用于测试和修改一些现有的粘度预测模型。先前由Asfour等人提出的技术。 (1991年)为预测二元正构烷烃的粘度对组成的依赖性已扩展到涵盖三元混合物。在这项研究中,已经开发了一种伪二元混合物模型来修改Teja和Rice(1981)较早提出的用于预测或关联液体混合物粘度的广义对应原理(GCSP)。对于具有两种以上成分的正构烷烃液体混合物,建议的GCSP方法改进具有以下优点:(i)用于预测混合物粘度,不需要参比液的选择程序,从而消除了可能的重大误差从这样的选择中得出; (ii)对于混合物粘度的相关性,无论系统中有多少个组件,它都将二元相互作用系数的数量减少为一个。显然,这可以节省大量成本和时间。本研究中提出了两个方程,作为对原始GCSP的补充,以使其更加有效。即(i)第一个方程涉及从纯组分性质预测二元正构烷烃体系的相互作用系数,(ii)第二个方程提供了一种在使用原始GCSP方法时适当选择参考流体的技术用于三元正构烷烃液体系统的粘度预测。还使用从本研究中获得的实验粘度和体积特性计算出的过剩特性数据对一些文献过剩特性模型进行了测试。化学和生物化学系。莱迪图书馆的纸质副本:论文主要论文-西楼地下室。 /电话号码:Thesis1992 .W955。资料来源:国际论文摘要,第53卷,第12节,B,第6430页。主管:Abdul-Fattah A. Asfour。论文(博士学位)-温莎大学(加拿大),1992。

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    Wu Jiangning.;

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