Factors affecting degradation of dimethyl sulfoxide (DMSO) by fluidized-bed Fenton process

被引:0
作者
Luzvisminda M. Bellotindos
Meng-Hsuan Lu
Thanakorn Methatham
Ming-Chun Lu
机构
[1] Universidad de Zamboanga,Archie Eustaquio Research Laboratory
[2] Chia Nan University of Pharmacy and Science,Department of Environmental Resources Management
[3] Metropolitan Waterworks Authority (MWA),Investment and Planning Division, Department of Policy and Strategy, Deputy Governor (Plan and Development)
来源
Environmental Science and Pollution Research | 2014年 / 21卷
关键词
Dimethyl sulfoxide; Advance oxidation process; Fluidized-bed Fenton; Fenton’s reagents; Heterogeneous catalysis;
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中图分类号
学科分类号
摘要
In this study, the target compound is dimethyl sulfoxide (DMSO), which is used as a photoresist stripping solvent in the semiconductor and thin-film transistor liquid crystal display (TFT-LCD) manufacturing processes. The effects of the operating parameters (pH, Fe2+ and H2O2 concentrations) on the degradation of DMSO in the fluidized-bed Fenton process were examined. This study used the Box-Behnken design (BBD) to investigate the optimum conditions of DMSO degradation. The highest DMSO removal was 98 % for pH 3, when the H2O2 to Fe2+ molar ratio was 12. At pH 2 and 4, the highest DMSO removal was 82 %, when the H2O2 to Fe2+ molar ratio was 6.5. The correlation of DMSO removal showed that the effect of the parameters on DMSO removal followed the order Fe2+ > H2O2 > pH. From the BBD prediction, the optimum conditions were pH 3, 5 mM of Fe2+, and 60 mM of H2O2. The difference between the experimental value (98 %) and the predicted value (96 %) was not significant. The removal efficiencies of DMSO, chemical oxygen demand (COD), total organic carbon (TOC), and iron in the fluidized-bed Fenton process were higher than those in the traditional Fenton process.
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页码:14158 / 14165
页数:7
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共 110 条
[1]  
Abellán MN(2009)Evaluation of two types of TiO J Photoch Photobio A 202 164-171
[2]  
Dillert R(2009)-based catalysts by photodegradation of DMSO in aqueous suspension J Hazard Mater 165 874-880
[3]  
Giménez J(2010)Kinetics of nitrobenzene oxidation and iron crystallization in fluidized-bed Fenton process J Hazard Mater 183 888-893
[4]  
Bahnemann D(2009)Effect of hydrogen peroxide on aniline oxidation by electro-Fenton and fluidized-bed Fenton processes J Hazard Mater 162 230-236
[5]  
Anotai J(2011)A statistical experiment design approach for advanced oxidation of Direct Red azo-dye by photo-Fenton treatment Water Res 45 3255-3262
[6]  
Sakulkittimasak P(2004)Iron crystallization in a fluidized-bed Fenton process Chemosphere 54 859-866
[7]  
Boonrattanakij N(2007)Factors influencing the preparation of supported iron oxide in fluidized-bed crystallization Anal Chim Acta 597 179-186
[8]  
Lu MC(2004)Box-Behnken design: an alternative for the optimization of analytical methods Adv Environ Res 8 501-551
[9]  
Anotai J(2006)A review of imperative technologies for wastewater treatment I: oxidation technologies at ambient conditions J Hazard Mater B136 763-769
[10]  
Su C-C(2011)Importance of H Bioresource Technol 102 5609-5616