Xinxin Qin , Xinyue Liu , Yi He , Yichun Zhu , Zuwen Liu , Wentao Li , Mengkai Li , Zhimin Qiang , Junfeng Lian
{"title":"UV/H2O2降解磺胺的动力学建模:ROH的推导、UV建模及应用","authors":"Xinxin Qin , Xinyue Liu , Yi He , Yichun Zhu , Zuwen Liu , Wentao Li , Mengkai Li , Zhimin Qiang , Junfeng Lian","doi":"10.1016/j.chemosphere.2024.143836","DOIUrl":null,"url":null,"abstract":"<div><div>Eight sulfonamide (SA) antibiotics were effectively degraded using a UV/H<sub>2</sub>O<sub>2</sub> process in a quasi-collimated beam apparatus, utilizing optimized fluence quantification. Fluence-based rate constants (<em>k</em><em>k</em>'<sub>SA</sub>) for the UV/H<sub>2</sub>O<sub>2</sub> process were established. A curve-fitting method, derived from <em>R</em><sub>OH,UV</sub> modeling, was developed for the UV/H<sub>2</sub>O<sub>2</sub> process to quantitatively assess the impact of critical factors, including water quality and direct UV photolysis. It was observed that <em>k</em>'<sub>SA</sub> values approached a limiting value as initial H<sub>2</sub>O<sub>2</sub> concentration increased. The specific second-order rate constants for <sup>•</sup>OH reactions with neutral and anionic SA species were determined to be within (2.2–5.7) × 10⁹ M⁻<sup>1</sup> s⁻<sup>1</sup>, showing minimal variation among species. For the eight SAs studied, <em>k</em>'<sub>SA</sub> values were calculated from 3.9 × 10⁻⁴ to 6.0 × 10⁻<sup>2</sup> cm<sup>2</sup> mJ⁻<sup>1</sup> across a typical pH range of 6.5–9.5. Direct UV photolysis was notably significant in SA degradation, particularly for sulfisoxazole, contributing at least 35%. An energy cost equation was formulated to evaluate the cost-effectiveness of SA degradation by UV/H<sub>2</sub>O<sub>2</sub> and optimize operational parameters. This model, validated in real water scenarios, shows promise for predicting SA removal in UV/H<sub>2</sub>O<sub>2</sub> processes. The developed curve-fitting method, pH-independent and accounting for both direct photolysis and OH radical reactions, is apt for modeling mixed-contaminant degradation in UV/H<sub>2</sub>O<sub>2</sub> processes, simplifying calculations in <em>R</em><sub>OH,UV</sub> modeling.</div></div>","PeriodicalId":276,"journal":{"name":"Chemosphere","volume":"369 ","pages":"Article 143836"},"PeriodicalIF":8.1000,"publicationDate":"2024-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Kinetic modeling of sulfonamide degradation by UV/H2O2: Deduction of ROH,UV modeling and application\",\"authors\":\"Xinxin Qin , Xinyue Liu , Yi He , Yichun Zhu , Zuwen Liu , Wentao Li , Mengkai Li , Zhimin Qiang , Junfeng Lian\",\"doi\":\"10.1016/j.chemosphere.2024.143836\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Eight sulfonamide (SA) antibiotics were effectively degraded using a UV/H<sub>2</sub>O<sub>2</sub> process in a quasi-collimated beam apparatus, utilizing optimized fluence quantification. Fluence-based rate constants (<em>k</em><em>k</em>'<sub>SA</sub>) for the UV/H<sub>2</sub>O<sub>2</sub> process were established. A curve-fitting method, derived from <em>R</em><sub>OH,UV</sub> modeling, was developed for the UV/H<sub>2</sub>O<sub>2</sub> process to quantitatively assess the impact of critical factors, including water quality and direct UV photolysis. It was observed that <em>k</em>'<sub>SA</sub> values approached a limiting value as initial H<sub>2</sub>O<sub>2</sub> concentration increased. The specific second-order rate constants for <sup>•</sup>OH reactions with neutral and anionic SA species were determined to be within (2.2–5.7) × 10⁹ M⁻<sup>1</sup> s⁻<sup>1</sup>, showing minimal variation among species. For the eight SAs studied, <em>k</em>'<sub>SA</sub> values were calculated from 3.9 × 10⁻⁴ to 6.0 × 10⁻<sup>2</sup> cm<sup>2</sup> mJ⁻<sup>1</sup> across a typical pH range of 6.5–9.5. Direct UV photolysis was notably significant in SA degradation, particularly for sulfisoxazole, contributing at least 35%. An energy cost equation was formulated to evaluate the cost-effectiveness of SA degradation by UV/H<sub>2</sub>O<sub>2</sub> and optimize operational parameters. This model, validated in real water scenarios, shows promise for predicting SA removal in UV/H<sub>2</sub>O<sub>2</sub> processes. The developed curve-fitting method, pH-independent and accounting for both direct photolysis and OH radical reactions, is apt for modeling mixed-contaminant degradation in UV/H<sub>2</sub>O<sub>2</sub> processes, simplifying calculations in <em>R</em><sub>OH,UV</sub> modeling.</div></div>\",\"PeriodicalId\":276,\"journal\":{\"name\":\"Chemosphere\",\"volume\":\"369 \",\"pages\":\"Article 143836\"},\"PeriodicalIF\":8.1000,\"publicationDate\":\"2024-12-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemosphere\",\"FirstCategoryId\":\"93\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0045653524027383\",\"RegionNum\":2,\"RegionCategory\":\"环境科学与生态学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENVIRONMENTAL SCIENCES\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemosphere","FirstCategoryId":"93","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0045653524027383","RegionNum":2,"RegionCategory":"环境科学与生态学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENVIRONMENTAL SCIENCES","Score":null,"Total":0}
Kinetic modeling of sulfonamide degradation by UV/H2O2: Deduction of ROH,UV modeling and application
Eight sulfonamide (SA) antibiotics were effectively degraded using a UV/H2O2 process in a quasi-collimated beam apparatus, utilizing optimized fluence quantification. Fluence-based rate constants (kk'SA) for the UV/H2O2 process were established. A curve-fitting method, derived from ROH,UV modeling, was developed for the UV/H2O2 process to quantitatively assess the impact of critical factors, including water quality and direct UV photolysis. It was observed that k'SA values approached a limiting value as initial H2O2 concentration increased. The specific second-order rate constants for •OH reactions with neutral and anionic SA species were determined to be within (2.2–5.7) × 10⁹ M⁻1 s⁻1, showing minimal variation among species. For the eight SAs studied, k'SA values were calculated from 3.9 × 10⁻⁴ to 6.0 × 10⁻2 cm2 mJ⁻1 across a typical pH range of 6.5–9.5. Direct UV photolysis was notably significant in SA degradation, particularly for sulfisoxazole, contributing at least 35%. An energy cost equation was formulated to evaluate the cost-effectiveness of SA degradation by UV/H2O2 and optimize operational parameters. This model, validated in real water scenarios, shows promise for predicting SA removal in UV/H2O2 processes. The developed curve-fitting method, pH-independent and accounting for both direct photolysis and OH radical reactions, is apt for modeling mixed-contaminant degradation in UV/H2O2 processes, simplifying calculations in ROH,UV modeling.
期刊介绍:
Chemosphere, being an international multidisciplinary journal, is dedicated to publishing original communications and review articles on chemicals in the environment. The scope covers a wide range of topics, including the identification, quantification, behavior, fate, toxicology, treatment, and remediation of chemicals in the bio-, hydro-, litho-, and atmosphere, ensuring the broad dissemination of research in this field.