Comparison of catalytic degradation of aniline by immobilized iron oxide catalysts

Environmental Engineering Science

Volumn 28, Issue 12, 2011, Pages 891-896

  Huang, Yao Hui ^a   Su, Chia Chi ^b   Yang, Yun Pei ^a   Lu, Ming Chun ^b  

^a NATIONAL CHENG KUNG UNIVERSITY   (Taiwan)

^b CHIA NAN UNIVERSITY OF PHARMACY AND SCIENCE   (Taiwan)

Author keywords

Aniline; Heterogeneous catalysis; Hydrogen radical; Immobilized iron oxide; Kinetics

Indexed keywords

AG CATALYSTS; ALUMINA GRANULE; CATALYST SYSTEM; CATALYTIC DECOMPOSITION; CATALYTIC DEGRADATION; DEGRADATION RATE; FLUIDIZED BED REACTORS; HYDROGEN RADICAL; HYDROXYL RADICALS; INITIAL STAGES; IRON OXIDE CATALYST; LARGER PARTICLE SIZES; SURFACE SITES;

ACTIVATION ENERGY; ANILINE; CATALYSIS; CATALYSTS; CHEMICAL REACTORS; DEGRADATION; ENZYME KINETICS; FLUIDIZATION; FLUIDIZED BEDS; GRANULATION; HYDROGEN; IRON; PRECIPITATION (CHEMICAL); SILICA; SINTERED ALUMINA;

IRON OXIDES;

ALUMINUM OXIDE; ANILINE; HYDROGEN PEROXIDE; HYDROXYL RADICAL; IRON OXIDE; SILICON DIOXIDE;

ARTICLE; CATALYSIS; COMPARATIVE STUDY; DECOMPOSITION; OXIDATION; PARTICLE SIZE; TEMPERATURE;

EID: 82555183077     PISSN: 10928758     EISSN: 15579018     Source Type: Journal    
DOI: 10.1089/ees.2010.0441     Document Type: Article

References (18)

1. Anotai, J., Bunmahotama, W., Lu, M.C. (2010a). Oxidation of aniline with sulfate radicals in the presence of citric acid. Environ. Eng. Sci. 28, 1.
2. Anotai, J., Su, C.C., Tsai, Y.C., and Lu, M.C. (2010b). Effect of hydrogen peroxide on aniline oxidation by electro-Fenton and fluidized-bed Fenton processes. J. Hazard. Mater. 183, 888.
3. Boonrattanakij, N., Lu, M.C., and Anotai, J. (2009). Kinetics and mechanism of 2,6-dimethyl-aniline degradation by hydroxyl radicals. J. Hazard. Mater. 172, 952.
4. Brillas, E., and Casado, J. (2002). Aniline degradation by electro- Fenton and peroxi-coagulation processes using a flow reactor for wastewater treatment. Chemosphere 47, 241.
5. 2+ on catalytic oxidation in a fluidized bed reactor. Chemosphere 39, 1997.
6. Chou, S.S., Huang, C.P., and Huang, Y.H. (2001). Heterogeneous and homogeneous catalytic oxidation by supported γ-FeOOH in a fluidized-bed reactor: kinetic approach. Environ. Sci. Technol. 35, 1247.
7. Eisenberg, G.M. (1943). Colorimetric determination of hydrogen peroxide. Ind. Eng. Chem. Anal. Ed. 15, 327.
8. 2 oxidation reactions in dilute aqueous solution using atrazine as a model organic compound. Water Res. 34, 3107.
9. Huang, C.P., Chen, C.R., Huang, Y.F., Lu, Y.W., Huang, Y.H. (2009a). Reductive dissolution and oxidative catalysis of an immobilized iron oxide in the presence of catechol and phenol. J. Mol. Catal. A. Chem. 304, 121.
10. Huang, C.P., Huang, Y.F., Cheng, H.P., and Huang, Y.H. (2009b). Kinetic study of an immobilized iron oxide for catalytic degradation of azo dye reactive black B with catalytic decomposition of hydrogen peroxide. Catal. Commun. 10, 561.
11. Huang, C.Y., and Huang, Y.H. (2008). Comparison of catalytic decomposition of hydrogen peroxide and catalytic degradation of phenol by immobilized iron oxides. Appl. Catal. A Gen. 346, 140.
12. Hsueh, C.L., Huang, Y.H., Wang, C.C., and Chen, C.Y. (2006). Photoassisted fenton degradeation of nonbiodegradable azodye (Reactive Black 5) over a novel supported iron oxide catalyst at neutrall pH. J. Mol. Catal. A Chem. 245, 78.
13. Kang, Y.W., and Hwang, K.Y. (2000). Effects of reaction conditions on the oxidation efficiency in the Fenton process. Water Res. 34, 2786.
14. Kwan, W.P., and Voelker, B.M. (2003). Rates of hydroxyl radical generation and organic compound oxidation in mineralcatalyzed Fenton-like systems. Environ. Sci. Technol. 37, 1150.
15. Masomboon, N., Ratanatamskul, C., and Lu, M.C. (2009). Chemical oxidation of 2,6-dimethylaniline in the fenton process. Environ. Sci. Technol. 43, 8629.
16. 2 decomposition and contaminant degradation in the presence of sand. Water Res. 33, 2805.
17. 3+ -catalyzed degradation of chlorophenoxy herbicides by hydrogen peroxide. Environ. Sci. Technol. 26, 944.
18. 2+ and UVA light. Appl. Catal. B Environ. 29, 135.