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首页> 外文期刊>The Journal of Chemical Thermodynamics >Thermodynamic properties of (an ester plus an alkane). XVIII. Experimental H-m(E) and V-m(E) values for (an alkyl butanoate plus an alkane) at T=318.15 K
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Thermodynamic properties of (an ester plus an alkane). XVIII. Experimental H-m(E) and V-m(E) values for (an alkyl butanoate plus an alkane) at T=318.15 K

机译:(酯加烷烃)的热力学性质。十八。 (丁酸烷基酯和烷烃)在T = 318.15 K时的实验H-m(E)和V-m(E)值

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This work presents the experimental values of H-m(E) and V-m(E) obtained at a temperature of 318.15 K and atmospheric pressure for a group of 24 binary mixtures comprised of the first four alkyl butanoates (methyl to butyl) with six odd alkanes, from heptane to hep tadecane. All the mixtures are endothermic, and present a regular increase in H-m(E) with the molecular weight of the saturated hydrocarbon, while, for a same alkane, the enthalpic effects diminish with increasing alcoholic chain of the butanoate. The variation in V-m(E) occurs in the same direction. In this paper the structural behaviour of these systems and the influence of temperature on excess properties are analysed. Experimental data are correlated with a suitable polynomial equation which is given as a function of concentration and temperature, that permits a simultaneous correlation to be established with other properties of the mixture, such as (vapour + liquid) equilibria; and acceptable results are obtained. Finally, an estimation of H-m(E) is made with two known versions of the UNIFAC model. In the version by Dang and Tassios [J. Dang, D.P. Tassios, Ind. Eng. Chem. Process Des. Dev. 25 (1986) 22-31.], a method is proposed that considers the interaction parameters as a function of the butanoate alkanolic chain. The estimations obtained for H-m(E) are good. (c) 2007 Elsevier Ltd. All rights reserved.
机译:这项工作提出了在318.15 K的温度和大气压下,由前四种烷基丁酸酯(甲基至丁基)与六种奇数烷烃组成的24种二元混合物的Hm(E)和Vm(E)的实验值。从庚烷到庚烷。所有混合物都是吸热的,并且随着饱和烃分子量的增加,H-m(E)呈规律性增加,而对于相同的烷烃,随着丁酸酯的醇链增加,焓效应减弱。 V-m(E)的变化方向相同。在本文中,分析了这些系统的结构行为以及温度对过量性能的影响。实验数据与合适的多项式方程式相关,该方程式是浓度和温度的函数,可以同时与混合物的其他性质(如(蒸气+液体)平衡)建立相关性。并获得可接受的结果。最后,使用两个已知版本的UNIFAC模型对H-m(E)进行估算。在Dang和Tassios的版本中[J.邓D.P.塔西奥斯(印第安纳州)化学流程设计。开发人员25(1986)22-31。]中,提出了一种考虑相互作用参数作为丁酸酯链的函数的方法。 H-m(E)获得的估计值很好。 (c)2007 Elsevier Ltd.保留所有权利。

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