喹啉
吸附
活性炭
化学
水溶液
吸热过程
弗伦德利希方程
朗缪尔
吡啶
朗缪尔吸附模型
过硫酸铵
过硫酸盐
无机化学
核化学
有机化学
催化作用
聚合物
聚合
作者
Tao Yang,Xuansheng Hu,Peijuan Zhang,Xiaogang Chen,Weiwei Wang,Yanping Wang,Qing Liang,Yingjiu Zhang,Qunce Huang
摘要
Abstract Activated carbon made from agricultural waste (walnut shells) was investigated as a suitable adsorbent for effectively removing quinoline from industrial wastewater. The activated carbon was treated with phosphoric acid and oxidized by ammonium persulfate and its ability to adsorb pyridine and quinoline in aqueous solution was investigated. Kinetic parameters for the adsorption process were determined through pseudo-first-order and pseudo-second-order kinetic models and intraparticle diffusion models. Equilibrium experiments and adsorption isotherms were analyzed using Langmuir and Freundlich adsorption isotherms. After reaching equilibrium, the activated carbon adsorbed quinoline in preference to pyridine: the equilibrium adsorptions from individual aqueous solutions (200 μL L−1) of quinoline and pyridine were 166.907 mg g−1 and 72.165 mg g−1, respectively. Thermodynamic studies of quinoline adsorption were conducted at different temperatures and indicated that quinoline adsorption was an endothermic and spontaneous process. The column-adsorption of quinoline and pyridine was consistent with the Thomas model and the Yoon-Nelson model. The removal efficiency of quinoline reached more than 97% for a velocity of 6 mL min−1 at the initial adsorption stage.
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