ELECTROCHEMICAL OXIDATION PROCESS FOR THE TREATMENT OF COKE PLANT WASTE-WATER

被引:35
作者
CHIANG, LC [1 ]
CHANG, JE [1 ]
WEN, TC [1 ]
机构
[1] NATL CHENG KUNG UNIV,DEPT CHEM ENGN,TAINAN,TAIWAN
来源
JOURNAL OF ENVIRONMENTAL SCIENCE AND HEALTH PART A-ENVIRONMENTAL SCIENCE AND ENGINEERING & TOXIC AND HAZARDOUS SUBSTANCE CONTROL | 1995年 / 30卷 / 04期
关键词
ELECTROCHEMICAL OXIDATION PROCESS; COKE-PLANT WASTE-WATER; GOD; TOX; AMMONIUM;
D O I
10.1080/10934529509376231
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Wastewater from a coke plant was treated by using an electrochemical oxidation process. After electrolysis for two hours with a lead dioxide coated titanium anode (PbO2/Ti), COD in the coke plant wastewater was reduced from 2143 mg/L to 226 mg/L and a COD removal efficiency of 89.5% was obtained. In addition, about 760 mg/L ammonium in the wastewater was completely removed simultaneously. These results indicate that electrochemical oxidation process demonstrates an excellent efficacy for the treatment of coke plant wastewater. In this study, anode material, chloride concentration, current density, and pH value were found to have significant influences on both COD removal efficiency and current efficiency in electrochemical oxidation process. Among four anode materials investigated, PbO2/Ti which is inert to the adsorption of phenolic oligomer served the best COD removal efficiency. And, better COD removal efficiencies were obtained as electrolysis experiments were operated under higher current density and chloride concentration. In this study, an indirect oxidation effect of chlorine/hypochlorite generated during electrolysis prays an important role in the removal of pollutants from coke plant wastewater. Consequently, lots of chlorinated byproducts (as TOX) were formed in the beginning of electrolysis, but the derivative TOX can also be removed after electrolysis.
引用
收藏
页码:753 / 771
页数:19
相关论文
共 19 条
[1]  
CHAMBERLIN NS, 1952, SEWAGE IND WASTES, V24, P750
[2]  
Chao Y. M., 1985, 40TH P IND WAST C, P33
[3]   ANODIC-OXIDATION OF PHENOL FOR WASTE-WATER TREATMENT [J].
COMNINELLIS, C ;
PULGARIN, C .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1991, 21 (08) :703-708
[4]  
COMNINELLIS C, 1993, J APPL ELECTROCHEM, V23, P108
[5]   SIMULTANEOUS ELECTROFLOTATION AND DISINFECTION OF SEWAGE [J].
COSTAZ, P ;
MIQUEL, J ;
REINBOLD, M .
WATER RESEARCH, 1983, 17 (03) :255-262
[6]   ANODIC-OXIDATION OF PHENOL FOR WASTEWATER-TREATMENT [J].
DESUCRE, VS ;
WATKINSON, AP .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1981, 59 (01) :52-59
[7]   THE ELECTROCHEMICAL OXIDATION OF AQUEOUS PHENOL AT A GLASSY-CARBON ELECTRODE [J].
GATTRELL, M ;
KIRK, DW .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1990, 68 (06) :997-1003
[8]   SIMULTANEOUS ELECTROCHEMICAL REMOVAL OF COPPER AND CHEMICAL OXYGEN-DEMAND USING A PACKED-BED ELECTRODE CELL [J].
KUSAKABE, K ;
NISHIDA, H ;
MOROOKA, S ;
KATO, Y .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1986, 16 (01) :121-126
[9]  
OEHR K, 1978, J WATER POLLUT CON F, V50, P286
[10]  
OSANTOWSKI R, 1981, 36TH P IND WAST C PU, P168