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Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation
This study explored the potential use of a sulfate radical (SO(·−)(4))-based photochemical oxidation process to treat the commercial nonionic surfactant octylphenol polyethoxylate (OPPE) Triton™ X-45. For this purpose, the effect of initial S(2)O(2−)(8) (0–5.0 mM) and OPPE (10–100 mg/L) concentratio...
Autores principales: | , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Frontiers Media S.A.
2013
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3982581/ https://www.ncbi.nlm.nih.gov/pubmed/24790933 http://dx.doi.org/10.3389/fchem.2013.00004 |
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author | Arslan-Alaton, Idil Olmez-Hanci, Tugba Genç, Bora Dursun, Duygu |
author_facet | Arslan-Alaton, Idil Olmez-Hanci, Tugba Genç, Bora Dursun, Duygu |
author_sort | Arslan-Alaton, Idil |
collection | PubMed |
description | This study explored the potential use of a sulfate radical (SO(·−)(4))-based photochemical oxidation process to treat the commercial nonionic surfactant octylphenol polyethoxylate (OPPE) Triton™ X-45. For this purpose, the effect of initial S(2)O(2−)(8) (0–5.0 mM) and OPPE (10–100 mg/L) concentrations on OPPE and its organic carbon content (TOC) removal were investigated at an initial reaction pH of 6.5. Results indicated that very fast OPPE degradation (100%) accompanied with high TOC abatement rates (90%) could be achieved for 10 and 20 mg/L aqueous OPPE at elevated S(2)O(2−)(8) concentrations (≥2.5 mM). S(2)O(2−)(8)/UV-C treatment was still capable of complete OPPE removal up to an initial concentration of 40 mg/L in the presence of 2.5 mM S(2)O(2−)(8). On the other hand, TOC removal efficiencies dropped down to only 40% under the same reaction conditions. S(2)O(2−)(8)/UV-C oxidation of OPPE was also compared with the relatively well-known and established H(2)O(2)/UV-C oxidation process. Treatment results showed that the performance of S(2)O(2−)(8)/UV-C was comparable to that of H(2)O(2)/UV-C oxidation for the degradation and mineralization of OPPE. In order to elucidate the relative reactivity and selectivity of SO(·−)(4) and HO(·), bimolecular reaction rate coefficients of OPPE with SO(·−)(4) and HO(·) were determined by employing competition kinetics with aqueous phenol (47 μM) selected as the reference compound. The pseudo-first-order abatement rate coefficient obtained for OPPE during S(2)O(2−)(8)/UV-C oxidation (0.044 min(−1)) was found to be significantly lower than that calculated for phenol (0.397 min(−1)). In the case of H(2)O(2)/UV-C oxidation however, similar pseudo-first-order abatement rate coefficients were obtained for both OPPE (0.087 min(−1)) and phenol (0.140 min(−1)). From the kinetic study, second-order reaction rate coefficients for OPPE with SO(·−)(4) and HO(·) were determined as 9.8 × 10(8) M(−1) s(−1) and 4.1 × 10(9) M(−1) s(−1), respectively. The kinetic study also revealed that the selectivity of SO(·−)(4) was found to be significantly higher than that of HO(·). |
format | Online Article Text |
id | pubmed-3982581 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2013 |
publisher | Frontiers Media S.A. |
record_format | MEDLINE/PubMed |
spelling | pubmed-39825812014-04-30 Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation Arslan-Alaton, Idil Olmez-Hanci, Tugba Genç, Bora Dursun, Duygu Front Chem Chemistry This study explored the potential use of a sulfate radical (SO(·−)(4))-based photochemical oxidation process to treat the commercial nonionic surfactant octylphenol polyethoxylate (OPPE) Triton™ X-45. For this purpose, the effect of initial S(2)O(2−)(8) (0–5.0 mM) and OPPE (10–100 mg/L) concentrations on OPPE and its organic carbon content (TOC) removal were investigated at an initial reaction pH of 6.5. Results indicated that very fast OPPE degradation (100%) accompanied with high TOC abatement rates (90%) could be achieved for 10 and 20 mg/L aqueous OPPE at elevated S(2)O(2−)(8) concentrations (≥2.5 mM). S(2)O(2−)(8)/UV-C treatment was still capable of complete OPPE removal up to an initial concentration of 40 mg/L in the presence of 2.5 mM S(2)O(2−)(8). On the other hand, TOC removal efficiencies dropped down to only 40% under the same reaction conditions. S(2)O(2−)(8)/UV-C oxidation of OPPE was also compared with the relatively well-known and established H(2)O(2)/UV-C oxidation process. Treatment results showed that the performance of S(2)O(2−)(8)/UV-C was comparable to that of H(2)O(2)/UV-C oxidation for the degradation and mineralization of OPPE. In order to elucidate the relative reactivity and selectivity of SO(·−)(4) and HO(·), bimolecular reaction rate coefficients of OPPE with SO(·−)(4) and HO(·) were determined by employing competition kinetics with aqueous phenol (47 μM) selected as the reference compound. The pseudo-first-order abatement rate coefficient obtained for OPPE during S(2)O(2−)(8)/UV-C oxidation (0.044 min(−1)) was found to be significantly lower than that calculated for phenol (0.397 min(−1)). In the case of H(2)O(2)/UV-C oxidation however, similar pseudo-first-order abatement rate coefficients were obtained for both OPPE (0.087 min(−1)) and phenol (0.140 min(−1)). From the kinetic study, second-order reaction rate coefficients for OPPE with SO(·−)(4) and HO(·) were determined as 9.8 × 10(8) M(−1) s(−1) and 4.1 × 10(9) M(−1) s(−1), respectively. The kinetic study also revealed that the selectivity of SO(·−)(4) was found to be significantly higher than that of HO(·). Frontiers Media S.A. 2013-03-20 /pmc/articles/PMC3982581/ /pubmed/24790933 http://dx.doi.org/10.3389/fchem.2013.00004 Text en Copyright © 2013 Arslan-Alaton, Olmez-Hanci, Genç and Dursun. http://creativecommons.org/licenses/by/3.0/ This is an open-access article distributed under the terms of the Creative Commons Attribution License, which permits use, distribution and reproduction in other forums, provided the original authors and source are credited and subject to any copyright notices concerning any third-party graphics etc. |
spellingShingle | Chemistry Arslan-Alaton, Idil Olmez-Hanci, Tugba Genç, Bora Dursun, Duygu Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation |
title | Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation |
title_full | Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation |
title_fullStr | Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation |
title_full_unstemmed | Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation |
title_short | Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation |
title_sort | advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate triton™ x-45 by the persulfate/uv-c process: effect of operating parameters and kinetic evaluation |
topic | Chemistry |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3982581/ https://www.ncbi.nlm.nih.gov/pubmed/24790933 http://dx.doi.org/10.3389/fchem.2013.00004 |
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