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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...

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Autores principales: Arslan-Alaton, Idil, Olmez-Hanci, Tugba, Genç, Bora, Dursun, Duygu
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Frontiers Media S.A. 2013
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(·).
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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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