Study of pre-treatment of quinoline in aqueous solution using activated carbon made from low-cost agricultural waste (walnut shells) modified with ammonium persulfate

被引:7
|
作者
Yang, Tao [1 ,2 ]
Hu, Xuansheng [3 ]
Zhang, Peijuan [1 ]
Chen, Xiaogang [2 ]
Wang, Weiwei [1 ]
Wang, Yanping [1 ]
Liang, Qiuxia [1 ]
Zhang, Yingjiu [2 ]
Huang, Qunce [1 ]
机构
[1] Zhengzhou Univ, Sch Phys & Engn, Henan Prov Key Lab Ion Beam Bioengn, Zhengzhou 450052, Henan, Peoples R China
[2] Zhengzhou Univ, Sch Phys & Engn, Minist Educ, Key Lab Mat Phys, Zhengzhou 450052, Henan, Peoples R China
[3] Shangluo Univ, Coll Biol Pharm & Food Engn, Shangluo 726000, Peoples R China
关键词
activated carbon; ammonium persulfate oxidation; column-adsorption process; equilibrium studies; kinetic parameters; quinoline; ADSORPTION; CESIUM; EQUILIBRIUM; REMOVAL; BIOSORBENT; BAGASSE;
D O I
10.2166/wst.2019.206
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
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 mu L 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.
引用
收藏
页码:2086 / 2094
页数:9
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