不同成分和温度下醋酸甲酯与某些选定酮的二元混合物的热力学性质

G. Cookey, Ngozi J. Maduelosi, Edikan A. Udo
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引用次数: 0

摘要

在不同的醋酸甲酯组成(0到1)和温度(25、30、35和40℃)下,对醋酸甲酯与丙酮、丁二酮和戊二酮的二元混合物进行了密度和粘度测量。得到的实验数据与Redlich-Kister多项式方程相关,其中计算了混合物的超摩尔体积(VE)、超粘度(ηE)、黏性流动的超吉布斯激活能(ΔG*E)、拟合系数和标准差。丁烷-2- 1和戊烷-2- 1混合物的ηE值在所有组分和温度下均为正,但随组分和温度的增加而逐渐降低。乙酸甲酯与丙酮的混合物在所有乙酸甲酯组分中均表现为负的过量粘度。观察到负值与温度成正比。乙酸甲酯+丙酮混合体系的VE值在低组分(0-0.4)下呈现正偏差,在高摩尔分数下呈现负偏差。在所研究的组分和温度下,丁烷-2- 1和戊烷-2- 1混合物的过量摩尔体积为负,在0.3组分时最小,随后随着组分的增加而逐渐减少。黏性流动活化的额外吉布斯自由能(ΔG*E)在所有组分和温度下均为正,在0.3组分时达到最大值,超过该值则减小。这些结果是根据溶剂混合物之间相互作用的类型和性质以及分子结构的差异来解释的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Thermodynamic properties of binary mixtures of methyl acetate and some selected ketonesat varying compositions and temperatures
Density and viscosity measurements of binary mixtures of methyl acetate with propanone, butan-2-one and pentan-2-one were carried out at varying compositions (0 to 1) of methyl acetate and temperatures of 25, 30, 35 and 40◦C. The experimental data obtained were correlated with the Redlich-Kister polynomial equation from where excess molar volumes (VE ), excess viscosities (ηE), excess Gibbs free energies of activation for viscous flow (ΔG*E ), fitting coefficients and standard deviations of the mixtures were calculated. The ηE values were positive for mixtures of butan-2-one and pentan-2-one at all compositions and temperatures but gradually decrease with increasing composition and temperature. The mixtures of methyl acetate with propanone showed negative values of excess viscosity at all compositions of methyl acetate. The negative values are observed to be directly proportional to temperature. The values of VE for mixtures of methyl acetate + propanone system display positive deviations at lower compositions (0-0.4) and negative for higher mole fractions. The excess molar volumes of mixtures of butan-2-one and pentan-2-one are negative at the studied compositions and temperatures with a minimum at 0.3 composition and subsequent gradual decrease in negativity with increasing composition. The excess Gibbs free energy of activation for viscous flow (ΔG*E ) are positive at all compositions and temperatures and reaches a maximum at 0.3 composition above which it decreases. These results have been interpreted on the basis of the type and nature of interactions as well as differences in molecular architecture between the solvent mixtures.                
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