Application of modified bentonite granulated electrodes for advanced treatment of pulp and paper mill wastewater in three-dimensional electrode system

被引:51
作者
Chu, Huanqing [1 ]
Wang, Zhen [1 ,2 ]
Liu, Yu [1 ]
机构
[1] Key Lab Pulp & Paper Sci & Technol, Jinan, Shandong, Peoples R China
[2] Shandong Univ, Qilu Univ Technol, Key Lab Cleaner Prod & Ind Waste Recycling & Reso, Jinan, Shandong, Peoples R China
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2016年 / 4卷 / 02期
关键词
Modified bentonite; 3-D electrode system; Pulp and paper wastewater; Discharge standard;
D O I
10.1016/j.jece.2016.02.017
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Two types of granular electrodes (cetyl trimethyl ammonium bromide modified bentonite (CTAB-bent) and hydroxy-aluminum pillared organic bentonite (OH-Al-CTAB-bent)) were prepared and form a three-dimensional (3-D) electrode system with general electrode plates to dispose the pulp and paper secondary wastewater deeply of paper mills. Then XRD, FTIR and SEM spectroscopy analysis were applied to characterize the feature of the electrodes. The removal efficiency of the chemical oxygen demand (COD) and color of the effluent after treatment was investigated. It was found that the removal efficiency of COD and color depended on the reaction time, current density, amount of granular electrode, the airflow and the run times. The results proved that the 3-D electrode system exhibited high efficiency in the removal of COD and color. Under the optimum conditions, the COD could be degraded from initial 256 mg/L to 40 mg/L, that was, 84.3% of COD were removed. And the removal efficiency of color could reach 93%. So the secondary wastewater treated advanced could meet the discharge standard (GB3544-2008). Finally, the possible reaction mechanism of organic pollutants degradation in 3-D electrode system was expatiated. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1810 / 1817
页数:8
相关论文
共 37 条
[1]   Adsorptive removal of tannin from aqueous solutions by cationic surfactant-modified bentonite clay [J].
Anirudhan, T. S. ;
Ramachandran, M. .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2006, 299 (01) :116-124
[2]  
Backhurst J.R., 1969, J ELECTROCHEM SOC, V116
[3]   Electrochemical degradation of 1,2-dichloroethane (DCA) in a synthetic groundwater medium using stainless-steel electrodes [J].
Bejankiwar, R ;
Lalman, JA ;
Seth, R ;
Biswas, N .
WATER RESEARCH, 2005, 39 (19) :4715-4724
[4]  
BERUBE PR, 2001, WATER ENVIRON RES, V73, P1
[5]   Effect of contact resistance between particles on the current distribution in a packed bed electrode [J].
Bockris, JO ;
Kim, J .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1997, 27 (08) :890-901
[6]   Mineralization of 2,4-D by advanced electrochemical oxidation processes [J].
Brillas, E ;
Calpe, JC ;
Casado, J .
WATER RESEARCH, 2000, 34 (08) :2253-2262
[7]  
BROWN CJ, 1994, J APPL ELECTROCHEM, V24, P95
[8]   Coupling of anodic and cathodic reactions for phenol electro-oxidation using three-dimensional electrodes [J].
Fockedey, E ;
Van Lierde, A .
WATER RESEARCH, 2002, 36 (16) :4169-4175
[9]   Study of catalyzed ozonation for advanced treatment of pulp and paper mill effluents [J].
Fontanier, V ;
Farines, V ;
Albet, J ;
Baig, S ;
Molinier, J .
WATER RESEARCH, 2006, 40 (02) :303-310
[10]   Electrochemical approaches to environmental problems in the process industry [J].
Jüttner, K ;
Galla, U ;
Schmieder, H .
ELECTROCHIMICA ACTA, 2000, 45 (15-16) :2575-2594