Degradation Kinetic of 2,4,6-Trichlorophenol in Aqueous During Nano-ZnO Catalyic Ozonation Processes

碩士 === 弘光科技大學 === 環境工程研究所 === 94 === Abstract Ozone is an powerful oxidant and important method for the degradation of organic pollutants in aqueous solution . However,the refractory organic pollutants usually not to tally oxidized and only a small mineralization is achieved. Several approaches h...

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Main Authors: Wang, Chun-Chen, 王春鎮
Other Authors: Huang, Winn-Jung
Format: Others
Language:zh-TW
Published: 2006
Online Access:http://ndltd.ncl.edu.tw/handle/09151057229102118238
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spelling ndltd-TW-094HKU055150012016-06-01T04:14:22Z http://ndltd.ncl.edu.tw/handle/09151057229102118238 Degradation Kinetic of 2,4,6-Trichlorophenol in Aqueous During Nano-ZnO Catalyic Ozonation Processes 奈米氧化鋅催化臭氧分解水相2,4,6-三氯酚之動力研究 Wang, Chun-Chen 王春鎮 碩士 弘光科技大學 環境工程研究所 94 Abstract Ozone is an powerful oxidant and important method for the degradation of organic pollutants in aqueous solution . However,the refractory organic pollutants usually not to tally oxidized and only a small mineralization is achieved. Several approaches have been taken to improve the oxidizing power of the technique by combined the oxidants (ex.H2O2) or catalysts (ex. TiO2、MnO2)﹒ Removal of 2,4,6-trichlorophenol (TCP) from water has been accomplished through zinc oxide (ZnO) catalytic ozonation. In the presence of ZnO catalyst, aqueous ozone (O3) can be described by a two-stage behavior, first involving a short-term rapid decomposition followed by a second slow decomposition. The low reaction rate (kd2) of second stage for O3-ZnO systems suggested that most of O3 was transferred into OH radical by ZnO catalyst and was rapidly consumed during the first stage. The combined use of O3 and ZnO catalyst leads to a conspicuous 99.8 % of TCP conversion in 30 min which compares favorably to the hardly 75 % reached in the absence of the catalyst. The high reactivity of hydroxyl radicals that were generated by O3-ZnO during the oxidation process effectively degraded TCP. Without regard to the O3 dose, the catalytic-oxidation kinetics of the process depends on the concentration of ZnO catalyst and size of ZnO particles. At the same concentration of three different ZnO size in batch tests, TCP degradation rates were in the order of nanometer > submicrometer > micrometer. The effect of pore diffusion on the rate of TCP-ZnO reactions was determined by examination of the effectiveness factor using different particle sizes of ZnO. Calculations show that the rate of TCP decomposition by nano-size ZnO was strongly controlled by surface reaction with little influence of pore diffusion, as indicated by the high effectiveness factors. Keywords: zinc oxide; catalyst; ozone; 2,4,6-trichlorophenol; nanometer Huang, Winn-Jung Fang, Guor-Cheng 黃文鑑 方國權 2006 學位論文 ; thesis 91 zh-TW
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description 碩士 === 弘光科技大學 === 環境工程研究所 === 94 === Abstract Ozone is an powerful oxidant and important method for the degradation of organic pollutants in aqueous solution . However,the refractory organic pollutants usually not to tally oxidized and only a small mineralization is achieved. Several approaches have been taken to improve the oxidizing power of the technique by combined the oxidants (ex.H2O2) or catalysts (ex. TiO2、MnO2)﹒ Removal of 2,4,6-trichlorophenol (TCP) from water has been accomplished through zinc oxide (ZnO) catalytic ozonation. In the presence of ZnO catalyst, aqueous ozone (O3) can be described by a two-stage behavior, first involving a short-term rapid decomposition followed by a second slow decomposition. The low reaction rate (kd2) of second stage for O3-ZnO systems suggested that most of O3 was transferred into OH radical by ZnO catalyst and was rapidly consumed during the first stage. The combined use of O3 and ZnO catalyst leads to a conspicuous 99.8 % of TCP conversion in 30 min which compares favorably to the hardly 75 % reached in the absence of the catalyst. The high reactivity of hydroxyl radicals that were generated by O3-ZnO during the oxidation process effectively degraded TCP. Without regard to the O3 dose, the catalytic-oxidation kinetics of the process depends on the concentration of ZnO catalyst and size of ZnO particles. At the same concentration of three different ZnO size in batch tests, TCP degradation rates were in the order of nanometer > submicrometer > micrometer. The effect of pore diffusion on the rate of TCP-ZnO reactions was determined by examination of the effectiveness factor using different particle sizes of ZnO. Calculations show that the rate of TCP decomposition by nano-size ZnO was strongly controlled by surface reaction with little influence of pore diffusion, as indicated by the high effectiveness factors. Keywords: zinc oxide; catalyst; ozone; 2,4,6-trichlorophenol; nanometer
author2 Huang, Winn-Jung
author_facet Huang, Winn-Jung
Wang, Chun-Chen
王春鎮
author Wang, Chun-Chen
王春鎮
spellingShingle Wang, Chun-Chen
王春鎮
Degradation Kinetic of 2,4,6-Trichlorophenol in Aqueous During Nano-ZnO Catalyic Ozonation Processes
author_sort Wang, Chun-Chen
title Degradation Kinetic of 2,4,6-Trichlorophenol in Aqueous During Nano-ZnO Catalyic Ozonation Processes
title_short Degradation Kinetic of 2,4,6-Trichlorophenol in Aqueous During Nano-ZnO Catalyic Ozonation Processes
title_full Degradation Kinetic of 2,4,6-Trichlorophenol in Aqueous During Nano-ZnO Catalyic Ozonation Processes
title_fullStr Degradation Kinetic of 2,4,6-Trichlorophenol in Aqueous During Nano-ZnO Catalyic Ozonation Processes
title_full_unstemmed Degradation Kinetic of 2,4,6-Trichlorophenol in Aqueous During Nano-ZnO Catalyic Ozonation Processes
title_sort degradation kinetic of 2,4,6-trichlorophenol in aqueous during nano-zno catalyic ozonation processes
publishDate 2006
url http://ndltd.ncl.edu.tw/handle/09151057229102118238
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