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Adsorption and Ozonation Kinetic Model for Phenolic Wastewater Treatment 被引量:13

Adsorption and Ozonation Kinetic Model for Phenolic Wastewater Treatment
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摘要 三分阶段执行使流体化的床反应堆被用来为酉分的废水处理调查吸附和氧化的联合效果。包含 10 mgssion 电子显微镜学(TEM ) 和表面形态学分析(SEM ) 的水的答案,表面酸(NH3-TPD ) , reducibility 性质(TPR ) , X 光检查精力散分光计(版本) 和 thermogravimetric 分析(TG/DTG ) 。Al/La 合成 mesoporous 材料与 n (艾尔) 被综合:n (La ) 70:1.0, 80 ? 楤慳癤湡慴敧? A three phase fluidized bed reactor was used to investigate the combined effect of adsorption and oxidation for phenolic wastewater treatment.Aqueous solutions containing 10 mg·L 1of phenol and ozone were continuously fed co-currently as upward flow into the reactor at constant flow rate of 2 and 1 L·min 1,respectively.The phenolic treatment results in seven cases were compared:(a)O3 only,(b)fresh granular activated carbon(GAC),(c) 1st reused GAC,(d)2nd reused GAC,(e)fresh GAC enhanced with O3,(f)1st reused GAC enhanced with O3,and (g)2nd reused GAC enhanced with O3.The phenolic wastewater was re-circulated through the reactor and its concentration was measured with respect to time.The experimental results revealed that the phenolic degradation using GAC enhanced with O3 provided the best result.The effect of adsorption by activated carbon was stronger than the effect of oxidation by ozone.Fresh GAC could adsorb phenol better than reused GAC.All cases of adsorption on GAC followed the Langmuir isotherm and displayed pseudo second order adsorption kinetics.Finally,a differential equation for the fluidized bed reactor model was used to describe the phenol concentration with respect to time for GAC enhanced with O3.The calculated results agree reasonably well with the experimental results.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2011年第1期76-82,共7页 中国化学工程学报(英文版)
基金 Supported by the National Nanotechnology Center(NANOTEC)(601003) the National Science and Technology Development Agency(NSTDA)
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