Enhancing the Performance of 2,4-Dichlorophenol Remove by FBR-Fenton Crystallization Process

碩士 === 國立高雄第一科技大學 === 環境與安全衛生工程所 === 94 === ABSTRACT The aim of this study is to develop a Fenton oxidation/fluidization crystallization process for both removing chlorinated phenols and reducing the formed iron-containing sludge while the organic pollutant decompose. A typical persistent organic po...

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Main Authors: Ting-Wei Yeh, 葉庭維
Other Authors: Chung-Hsuang Hung
Format: Others
Language:zh-TW
Published: 2006
Online Access:http://ndltd.ncl.edu.tw/handle/14513434768390831742
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spelling ndltd-TW-094NKIT55190332016-05-20T04:18:02Z http://ndltd.ncl.edu.tw/handle/14513434768390831742 Enhancing the Performance of 2,4-Dichlorophenol Remove by FBR-Fenton Crystallization Process 應用FBR-Fenton程序去除水中2、4-二氯酚與合成含鐵觸媒之研究 Ting-Wei Yeh 葉庭維 碩士 國立高雄第一科技大學 環境與安全衛生工程所 94 ABSTRACT The aim of this study is to develop a Fenton oxidation/fluidization crystallization process for both removing chlorinated phenols and reducing the formed iron-containing sludge while the organic pollutant decompose. A typical persistent organic pollutant, 2,4-dichlorinephenol (2,4-DCP), is selected as the target compound for the investigation. Series of tests involving major experimental variables of solution pH level, H2O2 concentrations and its dosage ways, and iron concentrations are conducted for process development. Recycled scraped iron chip provides the iron source for the Fenton (or Fenton like) reaction and silicon sand is applied as the carrier for the fluidize bed reactor. The experimental results shows that more than 99% of 2,4-DCP can be removed in a short reaction period by the fluidized bed Fenton (FBR-Fenton) process. The initial degradation rate of 2,4-DCP follows a pseudo first-order reaction kinetics. The achieved first-order reaction rate constants (k) of 2,4-DCP in various pH sloution are 0.2166, 0.0094 and 00.0101 min-1 for solution pH level equal to 3, 5 and 7, respectively. FBR-Fenton process not only can keep high degradation rate of 2,4-DCP as traditional homogenous Fenton process, but also up to 68% reduction in sludge production can be achieved at pH= 3. This investigation demonstrates the FBR-Fenton process is a V advanced oxidation process taking both advantages of fast reaction and low sludge yield. In addition, the experimental results indicate that the derived iron-containing silicon sand pebbles can be further recycled as the catalyst for heterogeneous Fenton-like reactions even though their reaction rate is not so fast as the homogenous Fenton reaction. Chung-Hsuang Hung 洪崇軒 2006 學位論文 ; thesis 115 zh-TW
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language zh-TW
format Others
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description 碩士 === 國立高雄第一科技大學 === 環境與安全衛生工程所 === 94 === ABSTRACT The aim of this study is to develop a Fenton oxidation/fluidization crystallization process for both removing chlorinated phenols and reducing the formed iron-containing sludge while the organic pollutant decompose. A typical persistent organic pollutant, 2,4-dichlorinephenol (2,4-DCP), is selected as the target compound for the investigation. Series of tests involving major experimental variables of solution pH level, H2O2 concentrations and its dosage ways, and iron concentrations are conducted for process development. Recycled scraped iron chip provides the iron source for the Fenton (or Fenton like) reaction and silicon sand is applied as the carrier for the fluidize bed reactor. The experimental results shows that more than 99% of 2,4-DCP can be removed in a short reaction period by the fluidized bed Fenton (FBR-Fenton) process. The initial degradation rate of 2,4-DCP follows a pseudo first-order reaction kinetics. The achieved first-order reaction rate constants (k) of 2,4-DCP in various pH sloution are 0.2166, 0.0094 and 00.0101 min-1 for solution pH level equal to 3, 5 and 7, respectively. FBR-Fenton process not only can keep high degradation rate of 2,4-DCP as traditional homogenous Fenton process, but also up to 68% reduction in sludge production can be achieved at pH= 3. This investigation demonstrates the FBR-Fenton process is a V advanced oxidation process taking both advantages of fast reaction and low sludge yield. In addition, the experimental results indicate that the derived iron-containing silicon sand pebbles can be further recycled as the catalyst for heterogeneous Fenton-like reactions even though their reaction rate is not so fast as the homogenous Fenton reaction.
author2 Chung-Hsuang Hung
author_facet Chung-Hsuang Hung
Ting-Wei Yeh
葉庭維
author Ting-Wei Yeh
葉庭維
spellingShingle Ting-Wei Yeh
葉庭維
Enhancing the Performance of 2,4-Dichlorophenol Remove by FBR-Fenton Crystallization Process
author_sort Ting-Wei Yeh
title Enhancing the Performance of 2,4-Dichlorophenol Remove by FBR-Fenton Crystallization Process
title_short Enhancing the Performance of 2,4-Dichlorophenol Remove by FBR-Fenton Crystallization Process
title_full Enhancing the Performance of 2,4-Dichlorophenol Remove by FBR-Fenton Crystallization Process
title_fullStr Enhancing the Performance of 2,4-Dichlorophenol Remove by FBR-Fenton Crystallization Process
title_full_unstemmed Enhancing the Performance of 2,4-Dichlorophenol Remove by FBR-Fenton Crystallization Process
title_sort enhancing the performance of 2,4-dichlorophenol remove by fbr-fenton crystallization process
publishDate 2006
url http://ndltd.ncl.edu.tw/handle/14513434768390831742
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