Bülow Mark, Greive Moritz, Zaitsau Dzmitry H, Verevkin Sergey P, Held Christoph
Laboratory of Thermodynamics, Department of Biochemical and Chemical Engineering, TU Dortmund, Emil-Figge Str. 70, 44277, Dortmund, Germany.
Department of Physical Chemistry, University of Rostock, 18059, Rostock, Germany.
ChemistryOpen. 2021 Feb;10(2):216-226. doi: 10.1002/open.202000258. Epub 2021 Jan 25.
Precursor solubility is a crucial factor in industrial applications, dominating the outcome of reactions and purification steps. The outcome and success of thermodynamic modelling of this industrially important property with equations of states, such as Perturbed-Chain Statistical Associating Fluid Theory (PC-SAFT), vastly depends on the quality of the pure-component parameters. The pure-component parameters for low-volatile compounds such as ionic liquids (ILs) have been commonly estimated using mixture properties, e. g. the osmotic pressure of aqueous solutions. This leads to parameters that depend on the solvent, and transferability to other mixtures often causes poor modeling results. Mixture-independent experimental properties would be a more suitable basis for the parameter estimation offering a way to universal parameter sets. Model parameters for ILs are available in the literature [10.1016/j.fluid.2012.05.029], but they were estimated using pure-IL density data. The present work focuses on a step towards a more universal estimation strategy that includes new experimental vapor-pressure data of the pure IL. ILs exhibit an almost negligible vapor pressure in magnitude of usually 10 Pa even at elevated temperatures. In this work, such vapor-pressure data of a series of 1-ethyl-3-methyl-imidazolium-based [C mim]-ILs with various IL-anions (e. g. tetrafluoroborate [BF ] , hexafluorophosphate [PF ] , bis(trifluoromethylsulfonyl)imide [NTf ] ) were experimentally determined and subsequently used for PC-SAFT parameter estimation. The so-determined parameters were used to predict experimental molecular precursor solubility in ILs and infinitely diluted activity coefficients of various solvents in ILs. The parameters were further compared to modeling results using classical parametrization methods (use of liquid-density data only for the molecular PC-SAFT and the ion-based electrolyte PC-SAFT). As a result, the modeled precursor solubilities using the new approach are much more precise than using the classical parametrization methods, and required binary parameters were found to be much smaller (if needed). In sum, including the pure-component vapor-pressure data of ILs opens the door towards parameter estimation that is not biased by mixture data. This procedure might be suitable also for polymers and for all kind of ionic species but needs extension to ion-specific parametrization in the long term.
前驱体溶解度是工业应用中的一个关键因素,它主导着反应和纯化步骤的结果。使用状态方程(如扰动链统计缔合流体理论(PC-SAFT))对这一具有工业重要性的性质进行热力学建模的结果和成功与否,在很大程度上取决于纯组分参数的质量。对于离子液体(ILs)等低挥发性化合物的纯组分参数,通常使用混合物性质(例如水溶液的渗透压)来估算。这导致参数依赖于溶剂,并且将其转移到其他混合物中时,往往会导致建模结果不佳。与混合物无关的实验性质将是更适合用于参数估计的基础,从而提供一种获得通用参数集的方法。离子液体的模型参数在文献中已有报道[10.1016/j.fluid.2012.05.029],但它们是使用纯离子液体密度数据估算得到的。目前的工作致力于朝着一种更通用的估计策略迈进,该策略包括新的纯离子液体蒸气压实验数据。即使在高温下,离子液体的蒸气压通常也非常小,量级几乎可以忽略不计,通常为10 Pa。在这项工作中,实验测定了一系列基于1-乙基-3-甲基咪唑鎓的[C mim]-离子液体与各种离子液体阴离子(例如四氟硼酸盐[BF ]、六氟磷酸盐[PF ]、双(三氟甲基磺酰)亚胺[NTf ])的蒸气压数据,并随后将其用于PC-SAFT参数估计。如此确定出的参数被用于预测实验中分子前驱体在离子液体中的溶解度以及各种溶剂在离子液体中的无限稀释活度系数。这些参数还进一步与使用经典参数化方法(仅将液体密度数据用于分子PC-SAFT和基于离子的电解质PC-SAFT)的建模结果进行了比较。结果表明,使用新方法建模得到的前驱体溶解度比使用经典参数化方法更为精确,并且发现所需的二元参数要小得多(如果需要的话)。总之,纳入离子液体的纯组分蒸气压数据为不受混合物数据影响的参数估计打开了大门。这个过程可能也适用于聚合物和所有种类的离子物种,但从长远来看需要扩展到特定离子的参数化。