Laboratory of Separation and Reaction Engineering - Associate Laboratory LSRE/LCM, Faculdade de Engenharia, Universidade do Porto, Rua Dr. Roberto Frias, 4200-465 Porto, Portugal.
J Phys Chem B. 2013 Aug 29;117(34):9980-95. doi: 10.1021/jp404864c. Epub 2013 Aug 16.
Biorefining processes using ionic liquids (ILs) require proper solubility data of biomass-based compounds in ILs, as well as an appropriate thermodynamic approach for the modeling of such data. Carbohydrates and their derivatives such as sugar alcohols represent a class of compounds that could play an important role in biorefining. Thus, in this work, the pure IL density and solubility of xylitol and sorbitol in five different ILs were measured between 288 and 339 K. The ILs under consideration were 1-ethyl-3-methylimidazolium dicyanamide, 1-butyl-3-methylimidazolium dicyanamide ([bmim][DCA]), Aliquat dicyanamide, trihexyltetradecylphosphonium dicyanamide, and 1-ethyl-3-methylimidazolium trifluoroacetate. Comparison with the literature data was performed, showing good agreement. With the exception of [bmim][DCA], the solubility of these sugar alcohols in the other ILs is presented for the first time. The measured data as well as previously published solubility data of glucose and fructose in these ILs were modeled by means of PC-SAFT using a molecular-based associative approach for ILs. PC-SAFT was used in this work as it has shown to be applicable to model the solubility of xylitol and sorbitol in ILs (Paduszyński; et al. J. Phys. Chem. B 2013, 117, 7034-7046). For this purpose, three pure IL parameters were fitted to pure IL densities, activity coefficients of 1-propanol at infinite dilution in ILs, and/or xylitol solubility in ILs. This approach allows accurate modeling of the pure IL data and the mixture data with only one binary interaction parameter k(ij) between sugar and the IL or sugar alcohol and the IL. In cases where only the pure IL density and activity coefficients of 1-propanol at infinite dilution in ILs were used for the IL parameter estimation, the solubility of the sugars and sugar alcohols in the ILs could be predicted (k(ij) = 0 between sugar and the IL or sugar alcohol and the IL) with reasonable accuracy.
使用离子液体(ILs)的生物炼制过程需要生物质基化合物在 ILs 中的适当溶解度数据,以及用于此类数据建模的适当热力学方法。碳水化合物及其衍生物(如糖醇)代表一类可能在生物炼制中发挥重要作用的化合物。因此,在这项工作中,在 288 至 339 K 之间测量了木糖醇和山梨糖醇在五种不同 IL 中的纯 IL 密度和溶解度。所考虑的 IL 是 1-乙基-3-甲基咪唑二氰胺、1-丁基-3-甲基咪唑二氰胺([bmim][DCA])、Aliquat 二氰胺、三己基十四烷基磷酸二氰胺和 1-乙基-3-甲基咪唑三氟乙酸盐。与文献数据进行了比较,结果表明吻合良好。除了[bmim][DCA]之外,这些糖醇在其他 IL 中的溶解度也是首次呈现。使用基于分子的缔合方法,通过 PC-SAFT 使用纯 IL 密度、IL 中无限稀释的 1-丙醇的活度系数和/或 IL 中木糖醇的溶解度对测量数据以及之前在这些 IL 中葡萄糖和果糖的溶解度数据进行了建模。在这项工作中使用了 PC-SAFT,因为它已被证明适用于模型 IL 中木糖醇和山梨糖醇的溶解度(Paduszyński;等人,J. Phys. Chem. B 2013,117,7034-7046)。为此,将三个纯 IL 参数拟合到纯 IL 密度、IL 中无限稀释的 1-丙醇的活度系数和/或 IL 中木糖醇的溶解度。这种方法允许仅使用一个二元相互作用参数 k(ij)(糖与 IL 或糖醇与 IL 之间)对纯 IL 数据和混合物数据进行准确建模。在仅使用 IL 参数估计的纯 IL 密度和 IL 中无限稀释的 1-丙醇的活度系数的情况下,可以以合理的精度预测糖和糖醇在 IL 中的溶解度(k(ij)=0 之间糖与 IL 或糖醇与 IL)。