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Adsorption kinetics of polyethylene glycol from aqueous solution onto activated carbon

机译:聚乙二醇从水溶液到活性炭的吸附动力学

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The adsorption equilibrium and kinetics of polyethylene glycol (PEG) in three aqueous systems were examined in this study. Langmuir isotherm was used to satisfactorily predict the adsorption capacity of PEG on activated carbon F-400 and applied to the investigation of adsorption kinetics. The surface diffusion, pore diffusion, and branched pore kinetics models successfully described the adsorption behavior of PEG on F-400 in the completely stirred tank reactor. The pore diffusion coefficients obtained from the pore diffusion model were compared with those computed by the experimental data of the short fixed-bed reactor combined with the assumption of non-hindered pore diffusion. In addition, the effects of initial concentrations of PEG and the relative importance of external and internal mass transfers for the adsorption were also taken into account and discussed in this study.
机译:在这项研究中检查了聚乙二醇(PEG)在三种水性体系中的吸附平衡和动力学。 Langmuir等温线用于令人满意地预测PEG在活性炭F-400上的吸附容量,并用于吸附动力学研究。表面扩散,孔扩散和分支孔动力学模型成功地描述了PEG在F-400上在完全搅拌釜反应器中的吸附行为。将通过孔隙扩散模型获得的孔隙扩散系数与通过短固定床反应器的实验数据结合无阻碍孔隙扩散的假设所计算出的孔隙扩散系数进行了比较。此外,本研究还考虑了PEG初始浓度的影响以及外部和内部质量转移对吸附的相对重要性。

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