Advanced landfill leachate biochemical effluent treatment using Fe-Mn/AC activates O3/Na2S2O8 process: process optimization, wastewater quality analysis, and activator characterization

被引:15
|
作者
Liu, Zhanmeng [1 ]
Pan, Liang [1 ]
Hu, Fengping [1 ]
Hu, Yunqi [1 ]
机构
[1] East China Jiao Tong Univ, Sch Civil Engn & Architecture, 808 East Shuanggang Rd, Nanchang 330013, Jiangxi, Peoples R China
关键词
Activator characterization; Fe-Mn; AC; Leachate biochemical effluent; Reusability; Sulfate radical oxidation; Spectrum analysis; ADVANCED OXIDATION; CATALYTIC OZONATION; ORGANIC-MATTER; BISPHENOL-A; PERSULFATE; DEGRADATION; REMOVAL; FENTON; CONTAMINANTS; KINETICS;
D O I
10.1007/s11356-020-08046-2
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A novel catalyst of Fe-Mn/AC was prepared and used as a heterogeneous catalyst to activate O-3/Na2S2O8 for landfill leachate biochemical effluent treatment. The experimental results indicated that the highest COD (84%) and color (98%) removal was obtained at Fe-Mn/AC dosage 1.2 g/L, O-3 concentration 1.2 g/L, Na2S2O8 dosage 6 g/L, initial pH 10, and reaction time 100 min. Three-dimensional and excitation emission matrix (3D-EEM) fluorescence spectrometry, Fourier transform infrared spectroscopy (FTIR), and gas chromatography mass spectrometry (GC/MS) of wastewater samples before and after treatment demonstrated that the leachate biochemical effluent contained a large amount of humic and fulvic acid organic compounds. After treatment with this coupling system, both the pollution level of dissolved organic matter (DOM) and the fluorescence intensity declined. The micro morphology of Fe-Mn/AC was characterized using scanning X-ray diffraction patterns (XRD), electron microscope spectra (SEM), X-ray photoelectron spectroscopy (XPS), and Fourier transform infrared (FTIR) spectroscopy. It can be concluded that the microscopic morphology of the catalyst is porous. The main active components are amorphous MnO2 and multivalent iron oxides. Furthermore, the Fe-Mn/AC catalyst showed great reusability; the removal efficiency of COD was only reduced from 84% to 79% at the fourth reaction. Moreover, the COD removal efficiency could recover to 81% after catalyst regeneration.
引用
收藏
页码:15337 / 15349
页数:13
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