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Correlating and predicting the solubilities of polycyclic aromatic hydrocarbons in supercritical fluids using the compressed gas model and the reference solubilities

机译:使用压缩气体模型和参考溶解度关联并预测多环芳烃在超临界流体中的溶解度

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The solubilities of some polycyclic aromatic hydrocarbons (PAHs) in supercritical fluids were correlated and predicted using the compressed gas model and the reference solubilities. By introducing the reference solubilities, the compressed gas models combined with Peng-Robinson equation of state, Carnahan-Starling-van der Waals hard sphere equation of state and van der Waals one-parameter mixing rules can yield the overall averages of the average absolute relative deviations (AARDs) of 7.45% and 8.16% in solubility correlation for PAHs in supercritical fluids, respectively, which are much less than the values obtained using the compressed gas model combined with the corresponding equation of state and the sublimation pressures of the solutes. By introducing the reference solubilities, the calculated solubilities are not sensitive to the binary interaction parameters and the solubilities of PAHs in the corresponding supercritical fluid can be predicted with a specific binary interaction parameter. When using reference solubilities in the compressed gas model, the two equations of state provide comparable average AARDs in solubility prediction for PAHs in supercritical fluids, which are 14.00% and 14.19%, respectively. The introduction of reference solubilities into the compressed gas model provides a feasible and simple solubility prediction method for the compounds in supercritical fluids without using their sublimation pressures. Moreover, combined with the reference solubilities and the compressed gas model, the hard sphere equation of state provides a more simple method to predict the solubilities of solutes in supercritical fluids with only their solid molar volumes.
机译:使用压缩气体模型和参考溶解度对超临界流体中某些多环芳烃(PAH)的溶解度进行关联和预测。通过引入参考溶解度,压缩气体模型与Peng-Robinson状态方程,Carnahan-Starling-van der Waals硬球状态方程和van der Waals一参数混合规则相结合,可以得出平均绝对相对湿度的总体平均值。 PAHs在超临界流体中的溶解度相关性的偏差(AARDs)分别为7.45%和8.16%,这远小于使用压缩气体模型结合相应的状态方程和溶质的升华压力获得的值。通过引入参考溶解度,计算出的溶解度对二元相互作用参数不敏感,并且可以通过特定的二元相互作用参数预测相应超临界流体中PAH的溶解度。在压缩气体模型中使用参考溶解度时,两个状态方程在超临界流体中PAH的溶解度预测中提供了可比较的平均AARD,分别为14.00%和14.19%。将参考溶解度引入压缩气体模型为超临界流体中的化合物提供了一种可行且简单的溶解度预测方法,而无需使用其升华压力。此外,结合参考溶解度和压缩气体模型,硬球状态方程提供了一种更简单的方法来预测仅具有固体摩尔体积的超临界流体中溶质的溶解度。

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