Continuous electrochemical treatment of simulated industrial textile wastewater from industrial components in a tubular reactor

被引:58
作者
Korbahti, Bahadir K. [2 ]
Tanyolac, Abdurrahman [1 ]
机构
[1] Hacettepe Univ, Dept Chem Engn, Fac Engn, TR-06800 Ankara, Turkey
[2] Mersin Univ, Dept Chem Engn, Fac Engn, TR-33343 Ciftlikkoy, Mersin, Turkey
关键词
Electrochemical wastewater treatment; Textile wastewater; Tubular reactor; Mass transfer; Energy consumption; ELECTROLYSIS SYSTEM; OXIDATION; DYE; DEGRADATION; ELECTRODES; DETOXIFICATION; HYPOCHLORITE; REMOVAL; PHENOL;
D O I
10.1016/j.jhazmat.2009.05.032
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The continuous electrochemical treatment of industrial textile wastewater in a tubular reactor was investigated. The synthetic wastewater was based on the real process information of pretreatment and dyeing stages of the industrial mercerized and non-mercerized cotton and viscon production. The effects of residence time on chemical oxygen demand (COD), color and turbidity removals and pH change were studied under response surface optimized conditions of 30 degrees C, 25 g/L electrolyte concentration and 3505 mg/LCOD feed concentration with 123.97 mA/cm(2) current density. Increasing residence time resulted in steady profiles of COD and color removals with higher treatment performances. The best column performance was realized at 3 h of residence time as 53.5% and 99.3% for COD and color removals, respectively, at the expense of 193.1 kWh/kg COD with a mass transfer coefficient of 9.47 x 10(-6) m/s. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:771 / 778
页数:8
相关论文
共 42 条
[1]   Electrolytic removal of ammonia from brine wastewater: scale-up, operation and pilot-scale evaluation [J].
Alfafara, CG ;
Kawamori, T ;
Nomura, N ;
Kiuchi, M ;
Matsumura, M .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2004, 79 (03) :291-298
[2]  
COMNINELLIS C, 1995, J APPL ELECTROCHEM, V25, P23
[3]   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
[4]   Paired electrooxidative degradation of phenol with in situ electrogenerated hydrogen peroxide and hypochlorite [J].
Do, JS ;
Yeh, WC .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1996, 26 (06) :673-678
[5]   Electrochemical degradation of C. I. Acid Orange 7 [J].
Fernandes, A ;
Morao, A ;
Magrinho, M ;
Lopes, A ;
Gonçalves, I .
DYES AND PIGMENTS, 2004, 61 (03) :287-296
[6]  
Fogler HS., 1999, ELEMENTS CHEM REACTI
[7]  
Ismail M. I., 1989, ELECTROCHEMICAL REAC
[8]   Olive oil wastewater treatment with the use of an electrolysis system [J].
Israilides, CJ ;
Vlyssides, AG ;
Mourafeti, VN ;
Karvouni, G .
BIORESOURCE TECHNOLOGY, 1997, 61 (02) :163-170
[9]   Treatment of dyeing wastewater with ACF electrodes [J].
Jia, JP ;
Yang, J ;
Liao, J ;
Wang, WH ;
Wang, ZJ .
WATER RESEARCH, 1999, 33 (03) :881-884
[10]   Electrochemical treatment of simulated textile wastewater with industrial components and Levafix Blue CA reactive dye:: Optimization through response surface methodology [J].
Korbahti, Bahadir K. ;
Tanyolac, Abdurrahman .
JOURNAL OF HAZARDOUS MATERIALS, 2008, 151 (2-3) :422-431