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Catalytic performance of Fe_3O_4-CoO/Al_2O_3 catalyst in ozonation of 2-(2,4-dichlorophenoxy) propionic acid,nitrobenzene and oxalic acid in water 被引量:10

Catalytic performance of Fe_3O_4-CoO/Al_2O_3 catalyst in ozonation of 2-(2,4-dichlorophenoxy) propionic acid,nitrobenzene and oxalic acid in water
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摘要 Fe3O4-CoO/Al2O3 catalyst was prepared by incipient wetness impregnation using Fe(NO3)3.9H2O and Co(NO3)2.6H2O as the precursors, and its catalytic performance was investigated in ozonation of 2-(2,4-dichlorophenoxy)propionic acid (2,4-DP), nitrobenzene and oxalic acid. The experimental results indicated that Fe3O4-CoO/Al2O3 catalyst enabled an interesting improvement of ozonation efficiency during the degradation of each organic pollutant, and the Fe3O4-CoO/Al2O3 catalytic ozonation system followed a radical-type mechanism. The kinetics of ozonation alone and Fe3O4-CoO/Al2O3 catalytic ozonation of three organic pollutants in aqueous solution were discussed under the mere consideration of direct ozone reaction and OH radical reaction to well investigate its performance. In the catalytic ozonation of 2,4-DP, the apparent reaction rate constants (k) were determined to be 1.456 × 10^-2 min-1 for ozonation alone and 4.740 × 10^-2 min^-1 for O3/Fe3O4-CoO/Al2O3. And O3/Fe3O4-CoO/Al2O3 had a larger Rot (6.614 × 10^-9) calculated by the relative method than O3 did (1.800 x 10-9), showing O3/Fe3O4-CoO/Al2O3 generated more hydroxyl radical. Similar results were also obtained in the catalytic ozonation of nitrobenzene and oxalic acid. The above results demonstrated that the catalytic performance of Fe3O4-CoO/Al2O3 in ozonation of studied organic substance was universal to a certain degree. Fe3O4-CoO/Al2O3 catalyst was prepared by incipient wetness impregnation using Fe(NO3)3.9H2O and Co(NO3)2.6H2O as the precursors, and its catalytic performance was investigated in ozonation of 2-(2,4-dichlorophenoxy)propionic acid (2,4-DP), nitrobenzene and oxalic acid. The experimental results indicated that Fe3O4-CoO/Al2O3 catalyst enabled an interesting improvement of ozonation efficiency during the degradation of each organic pollutant, and the Fe3O4-CoO/Al2O3 catalytic ozonation system followed a radical-type mechanism. The kinetics of ozonation alone and Fe3O4-CoO/Al2O3 catalytic ozonation of three organic pollutants in aqueous solution were discussed under the mere consideration of direct ozone reaction and OH radical reaction to well investigate its performance. In the catalytic ozonation of 2,4-DP, the apparent reaction rate constants (k) were determined to be 1.456 × 10^-2 min-1 for ozonation alone and 4.740 × 10^-2 min^-1 for O3/Fe3O4-CoO/Al2O3. And O3/Fe3O4-CoO/Al2O3 had a larger Rot (6.614 × 10^-9) calculated by the relative method than O3 did (1.800 x 10-9), showing O3/Fe3O4-CoO/Al2O3 generated more hydroxyl radical. Similar results were also obtained in the catalytic ozonation of nitrobenzene and oxalic acid. The above results demonstrated that the catalytic performance of Fe3O4-CoO/Al2O3 in ozonation of studied organic substance was universal to a certain degree.
出处 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2010年第10期1623-1628,共6页 环境科学学报(英文版)
基金 supported by the National Natural Science Foundation of China(No.50578146,20876151) the National Science Foundation of Zhejiang Province,China(No.Y5080178)
关键词 catalytic ozonation Fe3O4-CoO/Al2O3 2 4-DP NITROBENZENE oxalic acid kinetics catalytic ozonation Fe3O4-CoO/Al2O3 2,4-DP nitrobenzene oxalic acid kinetics
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  • 1Aaron J J,Oturan M A,2001.New photochemical and electrochemical methods for the degradation of pesticides in aqueous media.Environmental Applications,Turkish Journal of Chemistry,25(4):509-520.
  • 2Bader H,Hoigne J,1981.Determination of ozone in water by the indigo method.Water Research,15(4):449-456.
  • 3Bell L S,Devlin J F,Giilham R W,Binning P J,2003.A sequential zero valent iron and aerobic biodegradation treatment system for nitrobenzene.Journal of Contaminant Hydrology,66(3-4):201-217.
  • 4Beltran F J,2003.Ozone Reaction Kinetics for Water and Wastewater Systems.Lewis Publishers,Florida.
  • 5Beltran F J,Rivas F J,Espinosa R M,2002.Catalytic ozonation of oxalic acid in an aqueous TiO2 slurry reactor.Applied Catalysis B:Environmental,39(3):221-231.
  • 6Beltran F J,Rivas F J,Espinosa R M,2004.A TiO2/Al2O3 catalyst to improve the ozonation of oxalic acid in water.Applied Catalysis B:Environmental,47(2):101-109.
  • 7Beltran F J,Rivas J,Montero-de-Espinosa R,2003.Mineralization improvement of phenol aqueous solutions through heterogeneous catalytic ozonation.Journal of Chemical Technology and Biotechnology,78(12):1225-1233.
  • 8China Environmental Protection Bureau,1998.Water and Wastewater Analytic Method (3ed.).China Environmental Science Publisher House,Beijing.354-356.
  • 9Contreras S,Rodriguez M,Chamarro E,Esplugas S,2001.UV-and UV/Fe(Ⅲ)-enhanced ozonation of nitrobenzene in aqueous solution.Journal of Photochemistry and Photobiology A:Chemistry,142(1):79-83.
  • 10Elovitz M S,von Gunten U,1999.Hydroxyl radical/ozone ratios during ozonation processes I:The Rct concept.Ozone Science and Engineering,21(3):239-260.

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