Iprodione Removal by UV-Light-, Zero-Valent Iron- and Zero-Valent Aluminium-Activated Persulfate Oxidation Processes in Pure Water and Simulated Tertiary Treated Urban Wastewater
The degradation of iprodione (IPR), a once frequently used but recently banned dicarboximide fungicide, by UV-C light-, zero-valent iron- (ZVI), and zero-valent aluminium (ZVA)-activated persulfate (PS) oxidation processes was comparatively studied in distilled (pure) water (DW) and simulated, terti...
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2021-06-01
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author | Bahareh Montazeri Olga Koba-Ucun Idil Arslan-Alaton Tugba Olmez-Hanci |
author_facet | Bahareh Montazeri Olga Koba-Ucun Idil Arslan-Alaton Tugba Olmez-Hanci |
author_sort | Bahareh Montazeri |
collection | DOAJ |
description | The degradation of iprodione (IPR), a once frequently used but recently banned dicarboximide fungicide, by UV-C light-, zero-valent iron- (ZVI), and zero-valent aluminium (ZVA)-activated persulfate (PS) oxidation processes was comparatively studied in distilled (pure) water (DW) and simulated, tertiary treated urban wastewater (SWW). The performance of PS-activated oxidation processes was examined by following IPR (2–10 mg/L) removal, PS (0.01–1.00 mM) consumption, metal ion release (for the two heterogeneous catalytic oxidation processes), dissolved organic carbon (DOC) removal as well as hydroxylated aromatic and low molecular weight aliphatic degradation products. The effect of pH and PS concentrations on IPR removal was examined in DW. While the experiments in DW highlighted the superior performance of UV-C/PS treatment (with 78% DOC removal after 120 min at pH = 6.2), the performance of UV-C/PS treatment decreased sharply (to 24% DOC removal after 120 min at pH = 6.8) in the complex wastewater matrix (in SWW). Complete IPR (in 20 min) and 40% DOC (in 120 min) removals were obtained with ZVI/PS treatment (1 g/L ZVI, 1.5 mM PS, pH = 3.0), which was the most effective oxidation process in SWW. The treatment performance was strongly influenced by the SWW constituents, and UV-C/PS treatment appeared to be the most sensitive to it. |
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issn | 2073-4441 |
language | English |
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spelling | doaj.art-9e6696d329f547218e0a9e24d7e1c1842023-11-22T00:31:47ZengMDPI AGWater2073-44412021-06-011312167910.3390/w13121679Iprodione Removal by UV-Light-, Zero-Valent Iron- and Zero-Valent Aluminium-Activated Persulfate Oxidation Processes in Pure Water and Simulated Tertiary Treated Urban WastewaterBahareh Montazeri0Olga Koba-Ucun1Idil Arslan-Alaton2Tugba Olmez-Hanci3Department of Environmental Engineering, School of Civil Engineering, Ayazaga Campus, Istanbul Technical University, Maslak, Istanbul 34469, TurkeyDepartment of Environmental Engineering, School of Civil Engineering, Ayazaga Campus, Istanbul Technical University, Maslak, Istanbul 34469, TurkeyDepartment of Environmental Engineering, School of Civil Engineering, Ayazaga Campus, Istanbul Technical University, Maslak, Istanbul 34469, TurkeyDepartment of Environmental Engineering, School of Civil Engineering, Ayazaga Campus, Istanbul Technical University, Maslak, Istanbul 34469, TurkeyThe degradation of iprodione (IPR), a once frequently used but recently banned dicarboximide fungicide, by UV-C light-, zero-valent iron- (ZVI), and zero-valent aluminium (ZVA)-activated persulfate (PS) oxidation processes was comparatively studied in distilled (pure) water (DW) and simulated, tertiary treated urban wastewater (SWW). The performance of PS-activated oxidation processes was examined by following IPR (2–10 mg/L) removal, PS (0.01–1.00 mM) consumption, metal ion release (for the two heterogeneous catalytic oxidation processes), dissolved organic carbon (DOC) removal as well as hydroxylated aromatic and low molecular weight aliphatic degradation products. The effect of pH and PS concentrations on IPR removal was examined in DW. While the experiments in DW highlighted the superior performance of UV-C/PS treatment (with 78% DOC removal after 120 min at pH = 6.2), the performance of UV-C/PS treatment decreased sharply (to 24% DOC removal after 120 min at pH = 6.8) in the complex wastewater matrix (in SWW). Complete IPR (in 20 min) and 40% DOC (in 120 min) removals were obtained with ZVI/PS treatment (1 g/L ZVI, 1.5 mM PS, pH = 3.0), which was the most effective oxidation process in SWW. The treatment performance was strongly influenced by the SWW constituents, and UV-C/PS treatment appeared to be the most sensitive to it.https://www.mdpi.com/2073-4441/13/12/1679iprodione removalUV-C-activated persulfatezero-valent iron-activated persulfatezero-valent aluminium-activated persulfateperformance in simulated urban wastewater |
spellingShingle | Bahareh Montazeri Olga Koba-Ucun Idil Arslan-Alaton Tugba Olmez-Hanci Iprodione Removal by UV-Light-, Zero-Valent Iron- and Zero-Valent Aluminium-Activated Persulfate Oxidation Processes in Pure Water and Simulated Tertiary Treated Urban Wastewater Water iprodione removal UV-C-activated persulfate zero-valent iron-activated persulfate zero-valent aluminium-activated persulfate performance in simulated urban wastewater |
title | Iprodione Removal by UV-Light-, Zero-Valent Iron- and Zero-Valent Aluminium-Activated Persulfate Oxidation Processes in Pure Water and Simulated Tertiary Treated Urban Wastewater |
title_full | Iprodione Removal by UV-Light-, Zero-Valent Iron- and Zero-Valent Aluminium-Activated Persulfate Oxidation Processes in Pure Water and Simulated Tertiary Treated Urban Wastewater |
title_fullStr | Iprodione Removal by UV-Light-, Zero-Valent Iron- and Zero-Valent Aluminium-Activated Persulfate Oxidation Processes in Pure Water and Simulated Tertiary Treated Urban Wastewater |
title_full_unstemmed | Iprodione Removal by UV-Light-, Zero-Valent Iron- and Zero-Valent Aluminium-Activated Persulfate Oxidation Processes in Pure Water and Simulated Tertiary Treated Urban Wastewater |
title_short | Iprodione Removal by UV-Light-, Zero-Valent Iron- and Zero-Valent Aluminium-Activated Persulfate Oxidation Processes in Pure Water and Simulated Tertiary Treated Urban Wastewater |
title_sort | iprodione removal by uv light zero valent iron and zero valent aluminium activated persulfate oxidation processes in pure water and simulated tertiary treated urban wastewater |
topic | iprodione removal UV-C-activated persulfate zero-valent iron-activated persulfate zero-valent aluminium-activated persulfate performance in simulated urban wastewater |
url | https://www.mdpi.com/2073-4441/13/12/1679 |
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