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首页> 外文期刊>Fluid Phase Equilibria >Correlation and prediction of the solubilities of solid n-alkanes in supercritical carbon dioxide using the Carnahan-Starling-van der Waals model with a density-dependent parameter
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Correlation and prediction of the solubilities of solid n-alkanes in supercritical carbon dioxide using the Carnahan-Starling-van der Waals model with a density-dependent parameter

机译:使用密度依赖参数的Carnahan-Starling-van der Waals模型对超临界二氧化碳中固体正构烷烃的溶解度进行关联和预测

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In this paper, the solubilities of some solid n-alkanes in supercritical carbon dioxide were correlated and predicted using the Carnahan-Starling-van der Waals model with a density-dependent parameter of a _(12). It was found that the parameter values of a _(12) for solid n-alkanes in CO _2 at different temperatures are equal at the crossover pressure of 24MPa, and a _(12) can be correlated with carbon number of the corresponding solid n-alkanes. At a given temperature, the linear fit of parameters a _(12) versus the density of the solvent was used for solubility correlation, resulting in an average absolute average relative deviation of 11.82%, which is comparable with that of the Peng-Robinson equation of state combined with the van der Waals two-parameter mixing rule model. The regressed slope m and intercept n of the linear fit can also be correlated with the carbon number of solid n-alkanes. The solubilities of solid n-alkanes can be predicted with a _(12) at the crossover pressure and slope m or with intercept n and slope m.
机译:本文使用密度依赖参数为_(12)的Carnahan-Starling-van der Waals模型对某些固体正构烷烃在超临界二氧化碳中的溶解度进行关联和预测。发现在24MPa的交越压力下,CO_2中不同温度下固态n-烷烃的_(12)的参数值在24MPa的交越压力下相等,并且_(12)与相应的固态n的碳数相关-烷烃。在给定温度下,使用参数a _(12)对溶剂密度的线性拟合进行溶解度相关,得出的平均绝对平均相对偏差为11.82%,与Peng-Robinson方程相当状态与范德华两参数混合规则模型相结合。线性拟合的回归斜率m和截距n也可以与固体正构烷烃的碳原子数相关。固体正构烷烃的溶解度可以在交叉压力和斜率m处用_(12)或在截距n和斜率m处进行预测。

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