Electrochemical Oxidation of Bromothymol Blue: Application to Textile Industrial Wastewater Treatment

被引:0
|
作者
Maamar, Malak [1 ]
Naimi, Imen [1 ]
Mkadem, Yassine [2 ]
Souissi, Nebil [1 ]
Bellakhal, Nizar [1 ]
机构
[1] Inst Natl Sci Appl & Technol, Ctr Urbain Nord, Unite Rech Catalyse Electrochim Nanomat & Leurs A, Tunis, Tunisia
[2] Univ Libre Tunis, Dept Genie Chim, Tunis 1002, Tunisia
关键词
Bromothymol blue; electrochemical oxidation; electro-Fenton process; mineralization; textile industrial wastewater; ELECTRO-FENTON DEGRADATION; ACID ORANGE 7; AQUEOUS-MEDIUM; HYDROXYL RADICALS; REMOVAL; DYE; DECOLORIZATION; MINERALIZATION; DECOMPOSITION; IMPROVEMENT;
D O I
10.1515/jaots-2015-0113
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In this study, electrochemical oxidation of Bromothymol blue (BTB) was studied in an aqueous medium (pH = 3) by electro-Fenton process (EFP). This chemical compound belongs to the family of sulfone phthalein, widely used for dyeing in the textile industry. EFP generates in a catalytic way hydroxyl radicals (. OH) which are powerful oxidant species (E-0 (center dot OH/H2O) = 2.8 V/NHE) used for the oxidation of organic pollutants. The kinetics of BTB degradation and the mineralization efficiency of its process are investigated through the effect of some operating parameters. The value of 300 mA as applied current, Fe2+ as a catalyst with a concentration of 0.2 mM and a temperature of 40 degrees C are found to be the optimum operating parameters. The reaction kinetic follows a pseudo-first order with an absolute rate constant of 3.36 x 10(10) M(-1)s(-1). The efficiency of EFP is confirmed by the decrease of the molecule concentration during the treatment until its total disappearing. The chemical oxygen demand (COD) analyses indicate after 6 h a mineralization degree of 94% for the BTB synthetic solution, 91% for the effluent provided from a small Tunisian textile industry and 41% for the wastewater provided from a medium one. The energy consumption per unit COD mass (ECCOD) of the EFP is determined for the treatment of BTB synthetic solution and for the two real effluents. Concerning the BTB synthetic solution, the energetic cost is equal to 1.02 kWh (g COD)(-1) at the beginning of the electrolysis and it has decreased to reach 0.30 kWh (g COD)(-1) after 6 h. For the first effluent, the energy consumption rises from 1.20 to 0.36 kWh (g COD)(-1). An opposite phenomenon is observed for the second effluent.
引用
收藏
页码:105 / 113
页数:9
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