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Qian J, Atallah Al-Asad H, Parniske J, Brandl A, Degenhardt M, Morck T. Influence of effluent particles and particle-bound micropollutants on the removal of micropollutants and UVA 254 in wastewater effluent ozonation. ECOTOXICOLOGY AND ENVIRONMENTAL SAFETY 2024; 270:115915. [PMID: 38194809 DOI: 10.1016/j.ecoenv.2023.115915] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 09/30/2023] [Revised: 12/23/2023] [Accepted: 12/28/2023] [Indexed: 01/11/2024]
Abstract
This study systematically investigated the influence of effluent particles and activated sludge (AS) particles on the removal of micropollutants via wastewater effluent ozonation within typical effluent total suspended solids (TSS) concentrations. A series of batch experiments revealed that particle concentrations up to 30 mg/L had a minor impact on the removal of organic micropollutants (OMPs) in the aqueous phase. Moreover, the reduction of UV absorbance at 254 nm (UVA254) was negatively correlated to the level of particle concentration at ozone doses higher than 0.5 gO3/gDOC. It indicates that UVA254 abatement was more sensitive to the presence of particles compared to OMP removal. Organic micropollutants (OMPs) sorbed on effluent particles and sludge particles were extracted before and after ozonation. OMP sorption in effluent particles was 2-5 times higher than that in sludge particles. During the ozonation of raw secondary effluent, particle-bound micropollutants were removed comparably to the micropollutants in the aqueous phase. This suggests that the boundary layer surrounding the particle didn't affect the removal of OMPs in the particle phase. Furthermore, the removal of existing OMPs (irbesartan, sulfamethoxazole, and metoprolol) in the effluent was used to assess the ozone and •OH exposure. In water samples with and without particles, the elimination of OMPs could be reliably predicted (R² > 0.95) by calculated ozone and •OH exposures.
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Affiliation(s)
- Jueying Qian
- University of Kassel, Chair of Urban Water Engineering, Kurt-Wolters-Street 3, 34125 Kassel, Germany
| | - Hana Atallah Al-Asad
- University of Kassel, Chair of Urban Water Engineering, Kurt-Wolters-Street 3, 34125 Kassel, Germany
| | - Janna Parniske
- University of Kassel, Chair of Urban Water Engineering, Kurt-Wolters-Street 3, 34125 Kassel, Germany
| | - Andrea Brandl
- University of Kassel, Chair of Urban Water Engineering, Kurt-Wolters-Street 3, 34125 Kassel, Germany
| | - Monika Degenhardt
- University of Kassel, Chair of Urban Water Engineering, Kurt-Wolters-Street 3, 34125 Kassel, Germany
| | - Tobias Morck
- University of Kassel, Chair of Urban Water Engineering, Kurt-Wolters-Street 3, 34125 Kassel, Germany.
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Falås P, Juárez R, Dell LA, Fransson S, Karlsson S, Cimbritz M. Microbial bromate reduction following ozonation of bromide-rich wastewater in coastal areas. THE SCIENCE OF THE TOTAL ENVIRONMENT 2022; 841:156694. [PMID: 35714740 DOI: 10.1016/j.scitotenv.2022.156694] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 02/13/2022] [Revised: 06/08/2022] [Accepted: 06/10/2022] [Indexed: 06/15/2023]
Abstract
Ozonation of wastewater can reduce the release of organic micropollutants, but may result in the formation of undesirable by-products, such as bromate from bromide. Bromide is one of the most abundant ions in seawater, the primary precursor of bromate during ozonation, and the end product in microbial bromate reduction. Investigations were carried out to compare the concentration of bromide in wastewater in coastal and non-coastal catchment areas, to monitor bromate formation during ozonation, and to assess the potential for subsequent bromate reduction with denitrifying carriers. Higher bromide concentrations were systematically observed in wastewater from coastal catchment areas (0.2-2 mg Br-/L) than in wastewater from non-coastal areas (0.06-0.2 mg Br-/L), resulting in elevated formation of bromate during ozonation. Subsequent investigations of bromate reduction in contact with denitrifying carriers from two full-scale moving bed biofilm reactors (MBBRs) showed that 80 % of the bromate formed during ozonation could be reduced to bromide in 60 min with first-order rate constants of 0.3-0.8 L/(gbiomass·h). Flow-through experiments with denitrifying carriers also showed that combined reduction of bromate and nitrate could be achieved below a concentration of 2 mg NOx--N/L. These findings indicate that bromide-rich wastewater is more likely to be of concern when using ozonation in coastal than in non-coastal areas, and that bromate and nitrate reduction can be combined in a single biofilm reactor.
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Affiliation(s)
- Per Falås
- Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden.
| | - Rubén Juárez
- Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden; Sweden Water Research AB, Ideon Science Park, Scheelevägen 15, SE-223 70 Lund, Sweden
| | - Lauren A Dell
- Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden
| | - Sandra Fransson
- Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden
| | - Stina Karlsson
- Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden; Sweden Water Research AB, Ideon Science Park, Scheelevägen 15, SE-223 70 Lund, Sweden
| | - Michael Cimbritz
- Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden
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Abromaitis V, Svaikauskaite J, Sulciute A, Sinkeviciute D, Zmuidzinaviciene N, Misevicius S, Tichonovas M, Urniezaite I, Jankunaite D, Urbonavicius M, Varnagiris S, Dzingeleviciene R, Baranauskis K, Martuzevicius D. Ozone-enhanced TiO 2 nanotube arrays for the removal of COVID-19 aided antibiotic ciprofloxacin from water: Process implications and toxicological evaluation. JOURNAL OF ENVIRONMENTAL MANAGEMENT 2022; 318:115515. [PMID: 35949077 DOI: 10.1016/j.jenvman.2022.115515] [Citation(s) in RCA: 8] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 01/25/2022] [Revised: 05/25/2022] [Accepted: 06/10/2022] [Indexed: 06/15/2023]
Abstract
The purpose of this study was to evaluate the performance of synthesized TiO2 nanotube arrays (NTAs) for the removal of the COVID-19 aided antibiotic ciprofloxacin (CIP) and the textile dye methylene blue (MB) from model wastewater. Synthesis of TiO2 NTAs showed that anodization potential and calcination temperatures directly influence nanotube formation. The increased anodization potential from 10 to 40 V resulted in the development of larger porous nanotubes with a diameter of 36-170 nm, while the collapse of the tubular structure was registered at the highest applied potential. Furthermore, it was found that the 500 °C calcination temperature was the most prominent for the formation of the most photocatalytically active TiO2 NTAs, due to the optimal anatase/rutile ratio of 4.60. The degradation of both model compounds was achieved with all synthesized TiO2 NTAs; however, the most photocatalytically active NTA sample was produced at 30 V and 500 °C. Compared to photocatalysis, CIP degradation was greatly enhanced by 5-25 times when ozone was introduced to the photocatalytic cell (rates 0.4-4.2 × 10-1 min-1 versus 0.07-0.2 × 10-1 min-1). This resulted in the formation of CIP degradation by-products, with different mass-to-charge ratios from [M+H]+ 346 to 273 m/z. Even though the CIP degradation pathway is rather complex, three main mechanisms, decarboxylation, hydroxylation reaction, and piperazine ring cleavage, were proposed and explained. Furthermore, treated samples were placed in contact with the crustaceans Daphnia magna. It was found that 100% mortality was achieved when approximately 60% of the remaining TOC was present in the samples, indicating that toxic degradation by-products were formed.
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Affiliation(s)
- V Abromaitis
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania.
| | - J Svaikauskaite
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
| | - A Sulciute
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
| | - D Sinkeviciute
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
| | - N Zmuidzinaviciene
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
| | - S Misevicius
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
| | - M Tichonovas
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
| | - I Urniezaite
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
| | - D Jankunaite
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
| | - M Urbonavicius
- Lithuanian Energy Institute, Breslaujos st. 3, LT-44403, Kaunas, Lithuania
| | - S Varnagiris
- Lithuanian Energy Institute, Breslaujos st. 3, LT-44403, Kaunas, Lithuania
| | - R Dzingeleviciene
- Marine Research Institute, Klaipeda University, Universiteto av. 17, LT-92294, Klaipeda, Lithuania
| | - K Baranauskis
- Marine Research Institute, Klaipeda University, Universiteto av. 17, LT-92294, Klaipeda, Lithuania
| | - D Martuzevicius
- Kaunas University of Technology, Chemical Faculty of Technology, Radvilenu st. 19, LT-50254, Kaunas, Lithuania
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