Adsorption rate of phenol from aqueous solution onto organobentonite: Surface diffusion and kinetic models

被引:108
作者
Ocampo-Perez, Raul [1 ]
Leyva-Ramos, Roberto [1 ]
Mendoza-Barron, Jovita [1 ]
Guerrero-Coronado, Rosa M. [1 ]
机构
[1] Univ Autonoma San Luis Potosi, Fac Ciencias Quim, Ctr Invest & Estudios Posgrad, San Luis Potosi Slp 78210, Mexico
关键词
Adsorption; Diffusion; Kinetics; Mass transfer; Organobentonite; Phenol; GRANULAR ACTIVATED CARBON; PHASE ADSORPTION; HEAVY-METALS; SORPTION; REMOVAL; COEFFICIENTS; BENTONITE; SINGLE;
D O I
10.1016/j.jcis.2011.08.032
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The concentration decay curves for the adsorption of phenol on organobentonite were obtained in an agitated tank batch adsorber. The experimental adsorption rate data were interpreted with diffusional models as well as first-order, second-order and Langmuir kinetic models. The surface diffusion model adjusted the data quite well, revealing that the overall rate of adsorption was controlled by surface diffusion. Furthermore, the surface diffusion coefficient increased raising the mass of phenol adsorbed at equilibrium and was independent of the particle diameter in the range 0.042-0.0126 cm. It was demonstrated that the overall rate of adsorption was essentially not affected by the external mass transfer. The second-order and the Langmuir kinetic models fitted the experimental data quite well; however, the kinetic constants of both models varied without any physical meaning while increasing the particle size and the mass of phenol adsorbed at equilibrium. (C) 2011 Elsevier Inc. All rights reserved.
引用
收藏
页码:195 / 204
页数:10
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