Application of response surface methodology to the advanced treatment of biologically stabilized landfill leachate using Fenton's reagent

被引:74
|
作者
Li, Huosheng [1 ]
Zhou, Shaoqi [1 ,2 ,3 ]
Sun, Yanbo [1 ]
Lv, Jiang [4 ]
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, Peoples R China
[3] S China Univ Technol, Key Lab Environm Protect & Ecoremediat, Guangzhou Higher Educ Mega Ctr, Guangdong Regular Higher Educ Inst, Guangzhou 510006, Guangdong, Peoples R China
[4] S China Univ Technol, Coll Civil Engn & Transportat, Guangzhou 510640, Peoples R China
关键词
WASTE-WATER; EXPERIMENTAL-DESIGN; MILL EFFLUENT; OXIDATION; OPTIMIZATION; DEGRADATION; REMOVAL; DYE; COAGULATION; ORGANICS;
D O I
10.1016/j.wasman.2010.03.036
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A Fenton process that uses FeCl2 as the alternative catalyst was employed to deal with the biologically treated landfill leachate. Data obtained revealed that this Fenton process can provide an equivalent pollutant removal as the Fenton process that uses FeSO4 as catalyst. Central composite design (CCD) and response surface methodology (RSM) were applied to evaluate and optimize the four key factors, namely initial pH, Fe(II) dosage ([Fe2+]), H2O2/Fe(II) mole ratio ([H2O2]/[Fe2+] ratio) and reaction time, which affect the performance of the Fenton treatment. Chemical oxygen demand (COD) and color were selected as response variables. This approach provided statistically significant quadratic models, which were adequate to predict responses and to carry out optimization under the conditions studied. It was demonstrated that the interaction between initial pH and [H2O2]/[Fe2+] ratio has a significant effect on the COD removal, while the interaction between [H2O2]/[Fe2+] ratio and reaction time shows a large impact on color removal. The optimal conditions were found to be initial pH 5.9, [Fe2+] = 9.60 mmol/L, [H2O2]/ [Fe2+] ratio = 2.38, reaction time = 5.52 h. Under this optimal scheme, the COD and color in the effluent were reduced to 159 mg/L and 25 degrees, respectively, with an increase of BOD5/COD ratio from 0.05 to 0.21. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2122 / 2129
页数:8
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