<p>In this study, the treatability of a chemical industry wastewater by coagulation-flocculation pretreatment followed by persulfate oxidation process was investigated. In pretreatment, iron chloride (FeCl<sub>3</sub>), aluminum sulfate (Al<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub>) and polyaluminum chloride (PAC) coagulants were tested at different pH and dose conditions, and the best COD and TOC removal efficiency was obtained with FeCl<sub>3</sub> at pH 7 and 1750&#xa0;mg/L dose. After coagulation-flocculation, UV (UVA, UVB, UVC) and heat (50–90&#xa0;°C) activated persulfate oxidation processes were applied to the wastewater and their performances were compared. The highest removal efficiency in UV activation was achieved with UVC, and a total of 89.8% COD and 84.6% TOC removal was obtained. In heat activation, as the temperature increased, the removal efficiency increased, and 91.9% and 95.8% COD and 86.1% and 91.6% TOC removal was achieved at 70&#xa0;°C and 90&#xa0;°C, respectively. However, the increase in removal was limited after 70&#xa0;°C and the cost increased significantly. According to the cost analysis, oxidation studies conducted at 70&#xa0;°C were determined to be the most suitable option in terms of removal efficiency and cost. As a result, it was revealed that chemical industry wastewater can be effectively treated with UV or heat-activated persulfate oxidation processes after coagulation-flocculation pretreatment.</p>

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Treatment of chemical industry wastewater by persulfate oxidation after coagulation-flocculation: performance and cost analysis of UV and heat activation

  • Cankut Oğur,
  • Deniz İzlen Çifçi,
  • Elçin Güneş,
  • Yalçın Güneş

摘要

In this study, the treatability of a chemical industry wastewater by coagulation-flocculation pretreatment followed by persulfate oxidation process was investigated. In pretreatment, iron chloride (FeCl3), aluminum sulfate (Al2(SO4)3) and polyaluminum chloride (PAC) coagulants were tested at different pH and dose conditions, and the best COD and TOC removal efficiency was obtained with FeCl3 at pH 7 and 1750 mg/L dose. After coagulation-flocculation, UV (UVA, UVB, UVC) and heat (50–90 °C) activated persulfate oxidation processes were applied to the wastewater and their performances were compared. The highest removal efficiency in UV activation was achieved with UVC, and a total of 89.8% COD and 84.6% TOC removal was obtained. In heat activation, as the temperature increased, the removal efficiency increased, and 91.9% and 95.8% COD and 86.1% and 91.6% TOC removal was achieved at 70 °C and 90 °C, respectively. However, the increase in removal was limited after 70 °C and the cost increased significantly. According to the cost analysis, oxidation studies conducted at 70 °C were determined to be the most suitable option in terms of removal efficiency and cost. As a result, it was revealed that chemical industry wastewater can be effectively treated with UV or heat-activated persulfate oxidation processes after coagulation-flocculation pretreatment.