Mathematical model analysis of Fenton oxidation of landfill leachate

被引:29
|
作者
Wu, Yanyu [1 ,3 ]
Zhou, Shaoqi [1 ,2 ,3 ]
Zheng, Ke [1 ,3 ]
Ye, Xiuya [1 ,3 ]
Qin, Fanghui [1 ,3 ]
机构
[1] S China Univ Technol, Coll Environm Sci & Engn, Guangzhou Higher Educ Mega Ctr, Guangzhou 510006, Guangdong, Peoples R China
[2] S China Univ Technol, State Key Lab Subtrop Bldg Sci, Guangzhou 510641, Guangdong, Peoples R China
[3] S China Univ Technol, Key Lab Environm Protect & Ecoremediat, Guangdong Regular Higher Educ Inst, Guangzhou Higher Educ Mega Ctr, Guangzhou 510006, Guangdong, Peoples R China
关键词
WASTE-WATER TREATMENT; HYDROGEN-PEROXIDE; REVERSE-OSMOSIS; CHEMICAL OXIDATION; REACTION-KINETICS; ACTIVATED-SLUDGE; REAGENT; RADICALS; DEGRADATION; REMOVAL;
D O I
10.1016/j.wasman.2010.09.016
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The treatment of concentrated landfill leachate rejected from reverse osmosis (RO) with Fenton process was studied, and the system model was developed through the examination of reaction kinetics. The leachate is typically non-biodegradable with low BOD5/COD ratio 0.01. The oxidation reactions of Fenton process was found to be a two-stage process, where a fast initial reaction (H2O2/Fe2+) was followed by a much slower one (H2O2/Fe3+). A simple and more accurate mathematics model based on COD and TOC removals has been derived successfully to describe the two-stage reaction kinetics. The two corresponding parameters involved in this model have been identified as the initial reaction rate and the maximum oxidation removal efficiency, respectively. It was found to be very useful for evaluating the performance of Fenton system and/or for process design using the two parameters under different experimental conditions. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:468 / 474
页数:7
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