TY - JOUR
T1 - Degradation of thiocyanate by electrochemical oxidation process in coke oven wastewater
T2 - Role of operative parameters and mechanistic study
AU - Turan, Ayşenur
AU - Keyikoglu, Ramazan
AU - Kobya, Mehmet
AU - Khataee, Alireza
N1 - Publisher Copyright:
© 2020 Elsevier Ltd
PY - 2020/9
Y1 - 2020/9
N2 - 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.
AB - 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.
KW - Boron-doped diamond
KW - Coke oven wastewater
KW - Electrochemical oxidation
KW - Operation cost
KW - Thiocyanate removal
UR - http://www.scopus.com/inward/record.url?scp=85084473503&partnerID=8YFLogxK
U2 - 10.1016/j.chemosphere.2020.127014
DO - 10.1016/j.chemosphere.2020.127014
M3 - Article
C2 - 32679632
AN - SCOPUS:85084473503
SN - 0045-6535
VL - 255
JO - Chemosphere
JF - Chemosphere
M1 - 127014
ER -