Adsorption Kinetics of Fluroxypyr Herbicide in Aqueous Solution onto Granular Activated Carbon

被引:0
|
作者
Maria Pastrana-Martinez, Luisa [2 ]
Victoria Lopez-Ramon, Maria [2 ]
Moreno-Castilla, Carlos [3 ]
Joly, Jean-Pierre [1 ]
Perrard, Alain [1 ]
Morlay, Catherine [1 ]
机构
[1] Univ Lyon, CNRS, UMR IRCELYON 5256, Villeurbanne, France
[2] Univ Jaen, Dept Quim Inorgan & Organ, Fac Ciencias Expt, Jaen, Spain
[3] Univ Granada, Fac Ciencias, Dept Quim Inorgan, E-18071 Granada, Spain
来源
SEPARATION SCIENCE AND TECHNOLOGY | 2011年 / 46卷 / 10期
关键词
activated carbon; adsorption kinetics; fluroxypyr; herbicide; SURFACE-DIFFUSION MODEL; BATCH REACTOR SOLUTIONS; ORGANIC-COMPOUNDS; REMOVAL; DYE; EQUILIBRIUM; DESIGN; WATER;
D O I
10.1080/01496395.2011.572573
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Fluroxypyr is a widely used herbicide whose presence in natural waters has prompted research into its removal by adsorption. This article reports a kinetics study of fluroxypyr adsorption on a commercial activated carbon. The experimental study used a micro differential column batch reactor operated at three solution flow rates and two initial fluroxypyr concentrations, establishing a differential regime in order to obtain correct experimental data. Initial rates at zero coverage permitted the external transfer coefficient k(L) to be calculated. Internal surface diffusion coefficients D-S were determined by using the Homogeneous Surface Diffusion Model running the FAST software and taking advantage of tabulated user-oriented solutions. This model satisfactorily fits the experimental data. DS values were 2.5 x 10(-14) and 4.2 x 10(-14) m(2) s(-1) for initial concentrations of 30 and 50 mg/L, respectively. These values were confirmed by experiments in a widely used shaken batch reactor with a determined kL value.
引用
收藏
页码:1582 / 1590
页数:9
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