Degradation of thiocyanate by electrochemical oxidation process in coke oven wastewater: Role of operative parameters and mechanistic study

• Published in: Chemosphere (Oxford) 2020-09, Vol.255, p.127014-127014, Article 127014
• Main Authors: Turan, Ayşenur, Keyikoglu, Ramazan, Kobya, Mehmet, Khataee, Alireza
• Format: Article
• Language: English
• Subjects: Boron-doped diamond; Coke oven wastewater; Electrochemical oxidation; Operation cost; Thiocyanate removal
• ISSN: 0045-6535; 1879-1298
• DOI: 10.1016/j.chemosphere.2020.127014

This study presents the removal of thiocyanate (SCN−) from coke oven wastewater by the electrooxidation (EO) process. Initially, the performances boron-doped diamond (BDD) and different DSA (Dimensionally stable anode) electrodes including Ti/IrO2, Ti/IrO2−RuO2, and Ti/IrO2−RuO2−TiO2 in SCN− removal were compared. BDD anode outperformed the Ti−based mixed metal oxide (MMO) anodes achieving 96.51% SCN− removal efficiency. The most favorable conditions for the removal of SCN− using BDD anode were determined as follows: pH = 9, current density = 43.10 A m−2, and the electrolyte concentration (Na2SO4) = 2.5 g L−1. The strong role of ⦁OH in the removal of SCN− was confirmed by the addition of radical quenching agents. The evolution of the intermediates as a result of the EO of SCN− was determined. Under the determined conditions, the EO process could remove 84.13% of SCN− and 94.67% of phenol from a real coke oven wastewater, which was comparable to that of the simulated solution. The electrical energy consumption cost of the process to remove 1 kg of SCN− was calculated as 0.208 US $. Overall, the study showed the EO using BDD anode is a cost-effective method for the removal of SCN− from a coke oven wastewater. [Display omitted] •Electrochemical oxidation was used for the degradation of SCN−.•BDD anode showed superior performance compared to DSA electrodes.•The effect of the main operational parameters was investigated.•The cost of the process to remove 1 kg of SCN− was 0.208 US $.