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Equilibrium Solubilities of Iso-eicosane in Supercritical Carbon Dioxide

机译:异二十烷在超临界二氧化碳中的平衡溶解度

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摘要

To develop the separation process using supercritical (sc) CO2 regeneration of waste lubricating oil, the equilibrium solubilities of iso-eicosane in the binary iso-eicosane-supercritical CO2 system were obtained at 313.2 K, 328.2 K 343.2 K, and 358.2 K under pressures ranging from 7.24 MPa to 14.68 MPa. The solubilities of this component increased with a pressure increase, whereas they decreased with temperature increase. The Chrastil equation and Adachi and Lu equation were used correlate the solubility behavior of iso-eicosane in supercritical CO2, which revealed that both equations are in good agreement with the experimental data. Since the AARD values of the Chrastil equation range froth 0.42 % to 4.99 % and the AARD values of Adachi and Lu equation range from 0.16 % to 1.70 %, it was shown that the Adachi and Lu models better agreement with the experimental data.
机译:为了开发利用废润滑油的超临界(sc)CO2再生进行分离的方法,在压力下分别在313.2 K,328.2 K,343.2 K和358.2 K下获得了二异二十烷-超临界CO2系统中异二十烷的平衡溶解度。范围为7.24 MPa至14.68 MPa。该组分的溶解度随着压力的增加而增加,而随着温度的升高而降低。利用Chrastil方程,Adachi和Lu方程将异二十烷在超临界CO2中的溶解行为联系起来,表明这两个方程与实验数据吻合良好。由于Chrastil方程的AARD值介于0.42%至4.99%之间,而Adachi和Lu方程的AARD值介于0.16%至1.70%之间,因此表明Adachi和Lu模型与实验数据更好地吻合。

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