TY - JOUR
T1 - Treatment of coking wastewater by aeration assisted electrochemical oxidation process at controlled and uncontrolled initial pH conditions
AU - Iskurt, Cisel
AU - Keyikoglu, Ramazan
AU - Kobya, Mehmet
AU - Khataee, Alireza
N1 - Publisher Copyright:
© 2020 Elsevier B.V.
PY - 2020/10/1
Y1 - 2020/10/1
N2 - The high organic load and toxic content of coking oven wastewater (COW) challenge most of the conventional methods, which focus more on the removal of carbonaceous pollutants and less on the other toxic pollutants such as ammonia. To improve the treatment of COW, which had COD = 6600 mg/L, TOC = 1990 mg/L, SCN−=461 mg/L, NH3-N = 3430 mg/L, phenol = 1452 mg/L, and pH = 9.56, aeration was integrated to the electrochemical oxidation (EO). The effect of initial pH (5–12) and current density (140–700 A/m2) on the performance of the process was assessed. Also, the effect of aeration on the treatment of COW was determined by applying as stand-alone and integrated processes (combined and successive steps). All the experiments were performed both at controlled (pH was kept constant) and uncontrolled (pH was not adjusted) conditions. By applying the pseudo-first-order kinetic model, the contribution of aeration to the removal kinetics of the pollutants was clarified. The combined process of aeration/EO achieved 99.8% COD, 92.3% TOC, 100% NH3-N, 100% SCN−, and 100% phenol removal efficiencies. The total cost of the process, including electrical energy and chemical consumption, was determined as 52.10 $/m3 and 8.60 $/kg COD.
AB - The high organic load and toxic content of coking oven wastewater (COW) challenge most of the conventional methods, which focus more on the removal of carbonaceous pollutants and less on the other toxic pollutants such as ammonia. To improve the treatment of COW, which had COD = 6600 mg/L, TOC = 1990 mg/L, SCN−=461 mg/L, NH3-N = 3430 mg/L, phenol = 1452 mg/L, and pH = 9.56, aeration was integrated to the electrochemical oxidation (EO). The effect of initial pH (5–12) and current density (140–700 A/m2) on the performance of the process was assessed. Also, the effect of aeration on the treatment of COW was determined by applying as stand-alone and integrated processes (combined and successive steps). All the experiments were performed both at controlled (pH was kept constant) and uncontrolled (pH was not adjusted) conditions. By applying the pseudo-first-order kinetic model, the contribution of aeration to the removal kinetics of the pollutants was clarified. The combined process of aeration/EO achieved 99.8% COD, 92.3% TOC, 100% NH3-N, 100% SCN−, and 100% phenol removal efficiencies. The total cost of the process, including electrical energy and chemical consumption, was determined as 52.10 $/m3 and 8.60 $/kg COD.
KW - Ammonia removal
KW - Boron-doped diamond
KW - Coking wastewater
KW - Electrochemical oxidation
KW - Operation cost
UR - http://www.scopus.com/inward/record.url?scp=85084362700&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2020.117043
DO - 10.1016/j.seppur.2020.117043
M3 - Article
AN - SCOPUS:85084362700
SN - 1383-5866
VL - 248
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 117043
ER -