Study of COD and turbidity removal from real oxide-CMP wastewater by iron electrocoagulation and the evaluation of specific energy consumption

被引:75
作者
Chou, Wei-Lung [1 ]
Wang, Chih-Ta [2 ]
Chang, Shih-Yu [1 ]
机构
[1] Hungkuang Univ, Dept Safety Hlth & Environm Engn, Taichung 433, Taiwan
[2] Chung Hwa Univ Med Technol, Dept Safety Hlth & Environm Engn, Tainan 717, Taiwan
关键词
Electrocoagulation; Wastewater treatment; COD removal; Chemical mechanical polishing (CMP); Turbidity removal; Specific energy consumption; MECHANICAL POLISHING WASTE; PHOSPHATE REMOVAL; ALUMINUM; DECOLORIZATION; PERFORMANCES; PARTICLES; BIPOLAR;
D O I
10.1016/j.jhazmat.2009.02.163
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study explores the feasibility of reducing COD and turbidity from real oxide chemical mechanical polishing (oxide-CMP) wastewater. Based on the dynamic characteristics of batch electrocoagulation, three operating stages (lag. reactive, and stabilizing) are proposed to identify the relationships among the zeta potential of the silica particles, solution turbidity, and the corresponding mean particle size. Experiment results show that the silica particles were destabilized and settled at the critical electrolysis time, which was estimated to be about 12 min under an applied voltage of 20 V and a supporting electrolyte of 200 mg/L The corresponding turbidity removal occurred mostly during the reactive stage. The process variables, including applied voltage and electrolyte concentration, were investigated in terms of COD removal efficiency and turbidity removal. In addition, the effects of applied voltage and supporting electrolyte on COD removal efficiency and specific energy consumption were evaluated. Under the optimum balance, satisfactory removal efficiency and relatively low energy consumption were obtained. The optimum electrolyte concentration and applied voltage were found to be 200 mg/L NaCl and 20V, respectively. Under the optimum conditions, COD and turbidity decreased by more than 90% and 98% in real oxide-CMP wastewater, respectively. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:1200 / 1207
页数:8
相关论文
共 45 条
[1]  
[Anonymous], 1992, STAND METH EX WAT WA
[2]   Treatment of alumina and silica chemical mechanical polishing waste by electrodecantation and electrocoagulation [J].
Belongia, BM ;
Haworth, PD ;
Baygents, JC ;
Raghavan, S .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1999, 146 (11) :4124-4130
[3]  
Benefield L.D., 1982, PROCESS CHEM WATER W
[4]   Electrocoagulation of cutting oil emulsions using aluminium plate electrodes [J].
Bensadok, K. ;
Benammar, S. ;
Lapicque, F. ;
Nezzal, G. .
JOURNAL OF HAZARDOUS MATERIALS, 2008, 152 (01) :423-430
[5]  
Browne S, 1999, MICRO, V17, P77
[6]   Separation of pollutants from restaurant wastewater by electrocoagulation [J].
Chen, XM ;
Chen, GH ;
Yue, PL .
SEPARATION AND PURIFICATION TECHNOLOGY, 2000, 19 (1-2) :65-76
[7]  
Corlett G, 2000, SOLID STATE TECHNOL, V43, P201
[8]   Decolorization of CI Acid Yellow 23 solution by electrocoagulation process: Investigation of operational parameters and evaluation of specific electrical energy consumption (SEEC) [J].
Daneshvar, N. ;
Khataee, A. R. ;
Ghadim, A. R. Amani ;
Rasoulifard, M. H. .
JOURNAL OF HAZARDOUS MATERIALS, 2007, 148 (03) :566-572
[9]   Decolorization of basic dye solutions by electrocoagulation: An investigation of the effect of operational parameters [J].
Daneshvar, N ;
Oladegaragoze, A ;
Djafarzadeh, N .
JOURNAL OF HAZARDOUS MATERIALS, 2006, 129 (1-3) :116-122
[10]   Electrocoagulation for removal of silica nano-particles from chemical-mechanical-planarization wastewater [J].
Den, W ;
Huang, CP .
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 2005, 254 (1-3) :81-89