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Competitive adsorption equilibrium modeling of volatile organic compound (VOC) and water vapor onto activated carbon

机译:挥发性有机化合物(VOC)和水蒸气挥发性碳的竞争性吸附平衡建模

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摘要

In this study, the Potential theory-based Manes method was used to describe competitive multicomponent adsorption of VOC and water vapor onto activated carbon. The thermodynamically consistent method was extended to water-miscible VOCs using a Raoult's law-like relation. The method uses as input the pure single-component adsorption isotherms, which were obtained from the modified Dubinin-Radushkevich (MDR) model for VOCs and the Qi-Hay-Rood (QHR) model for water vapor. The MDR model was applicable for the studied VOCs (2-propanol, acetone, n-butanol, toluene, 1,2,4-trimethylbenzene) with an overall r(2) value of 0.998. The QHR isotherm provided a good description for water vapor adsorption on activated carbon with 0.999 r(2) value. Experimental validation tests revealed that the multicomponent adsorption isotherm model predicted the VOC adsorption capacity during competitive adsorption with water vapor with an overall mean relative absolute error (MRAE) of 1.9% for non-polar VOCs and 5.2% for polar VOCs. These results are encouraging, as they indicate a good agreement between modeled and experimental results. Hence, the model can potentially be integrated with dynamic adsorption models to optimize adsorber design and operation or model adsorption kinetics.
机译:在该研究中,用于将VOC和水蒸气的竞争多组分吸附在活性炭中来描述竞争性的多组分吸附。热力学一致的方法使用Raoul的类似法律关系扩展到水混溶VOC。该方法用作输入纯单组分吸附等温,从用于水蒸气的VOCS和QI-Hay-Rood(QHR)模型的改性的Dubinin-Radushkevich(MDR)模型中获得。 MDR模型适用于研究的VOC(2-丙醇,丙酮,正丁醇,甲苯,1,2,4-三甲基苯),其总R(2)值为0.998。 QHR等温机提供了良好的描述,用于对活性炭的水蒸气吸附,0.999 r(2)值。实验验证试验显示,多组分吸附等温线模型预测了在竞争吸附过程中的VOC吸附能力,水蒸气,对于非极性VOC的总体平均相对绝对误差(MRAE)为1.9%,极性VOC的5.2%。这些结果令人鼓舞,因为它们表明建模和实验结果之间的良好一致性。因此,该模型可能与动态吸附模型集成,以优化吸附器设计和操作或模型吸附动力学。

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