Decolorization and Degradation of a Mixture of Industrial Azo Dyes by Anodic Oxidation Using a Ti/Ru0.3Ti0.7O2 (DSA-Cl2) Electrode

被引:15
作者
Sandoval, Miguel A. [1 ,2 ]
Zuniga-Mallea, Nury [1 ]
Espinoza, L. Carolina [1 ]
Vidal, Jorge [1 ]
Jara-Ulloa, Paola [3 ]
Salazar, Ricardo [1 ]
机构
[1] Univ Santiago Chile, Fac Quim & Biol, Lab Electroquim Medio Ambiental, LEQMA,Dept Quim Mat,USACH, Casilla 40,Correo 33, Santiago, Chile
[2] Univ Guanajuato, Dept Ingn Quim, Div Ciencias Nat & Exactas, Noria Alta S-N, Guanajuato 36050, Guanajuato, Mexico
[3] Univ Andres Bello, Lab Electroquim & Superficies Modificadas, Ave Republ 330, Santiago, Chile
来源
CHEMISTRYSELECT | 2019年 / 4卷 / 47期
关键词
anodic oxidation; azo dye; COD removal; decolorization; DSA-Cl-2; anode; ELECTROCHEMICAL DEGRADATION; WASTE-WATER; ACTIVE CHLORINE; PARAMETERS; REMOVAL; PHENOL; ELECTROOXIDATION; BETA-PBO2; EFFLUENT; BEHAVIOR;
D O I
10.1002/slct.201903150
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The electrochemical treatment of wastewaters from the textile industry is a promising alternative for the elimination of organic pollutants. This study approach the decolorization and chemical oxygen demand (COD) removal from synthetic water (0.91 mM Acid Yellow 25 dye - and - 0.42 mM Acid Blue 29 dye), by anodic oxidation (AO) in batch mode using a Ti/Ru0.3Ti0.7O2 (DSA-Cl-2) electrode as anode and an AISI 304 stainless steel plate as cathode. The influence of pH (3, 7 and 10), type of supporting electrolyte (50 mM Na2SO4, 50 mM NaCl and 100 mM NaCl) and applied current density (10 < j < 80 mAcm(-2)) on COD removal and mineralization current efficiency was analyzed. The best AO test in terms of energy consumption was performed at pH 7, 50 mM NaCl and j = 30 mAcm(-2), obtaining a complete decolorization and COD removal. These operating parameters have an energy consumption between 0.41 and 0.82 kWh m(-3). High performance liquid chromatography (HPLC-MS/MS) analyses indicated the presence of several organic intermediates and carboxylic acids.
引用
收藏
页码:13856 / 13866
页数:11
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