ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received July 5, 2002
Accepted September 6, 2002
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

Catalytic Combustion of Benzene over Supported Metal Oxides Catalysts

Division of Chemical Engineering, Pukyong National University, 100 Yongdang-dong, Nam-ku, Busan 608-739, Korea
sshong@pknu.ac.kr
Korean Journal of Chemical Engineering, May 2003, 20(3), 440-444(5), 10.1007/BF02705544
downloadDownload PDF

Abstract

Catalytic combustion of benzene over supported metal oxides has been investigated. The catalysts have been prepared by incipient wetness method and characterized by XRD, FT-Raman, ESR and TPR. Among supported metal oxides, CuOx supported on TiO2 is found to have the highest activity for benzene oxidation. In addition, among the catalysts of copper oxide supported on TiO2, Al2O3 and SiO2, titania-supported catalyst (CuOx/TiO2) gives the highest catalytic activity. CuOx/TiO2 (Cu loading 5.5 wt%) shows the total oxidation of benzene at about 250 ℃. From the ESR and FT-Raman results, the CuO dispersed on the TiO2 surface acts as an active site of CuOx/TiO2 catalysts on the oxidative decomposition of benzene. The catalytic activity gradually increases with an increase of Cu loading on TiO2. When Cu loading reaches 5.5 wt%, the total conversion temperature is lowered to 300 ℃. However, the catalytic activity considerably decreases at 7 wt% Cu loading. The catalytic activity increased with an increase of oxygen concentration but the concentration of benzene showed no difference in the benzene conversion. This result suggests that the rate determining step is the adsorption of oxygen.

References

Berger J, Roth JF, J. Phys. Chem., 71, 4307 (1967) 
Cho SJ, Ryoo MW, Soun KS, Lee JH, Kang SK, Korean J. Chem. Eng., 16(4), 478 (1999)
Coq B, Tachon D, Figueras F, Mabilon G, Prigent M, Appl. Catal. B: Environ., 6(3), 271 (1995) 
Cordoba G, Viniegra M, Fierro JLG, Padolla J, Arroyo R, J. Solid State Chem., 138, 1 (1998) 
Dow WP, Wang YP, Huang TJ, J. Catal., 160(2), 155 (1996) 
Ferreira RSG, de Oliveira PGP, Noronha FB, Appl. Catal. B: Environ., 29(4), 275 (2001) 
Gallardo-Amores JM, Armaroli T, Ramis G, Finocchio E, Busca G, Appl. Catal. B: Environ., 22(4), 249 (1999) 
Hutchins GJ, Heneghan CS, Hudson ID, Taylor SH, Nature, 384(6607), 341 (1996) 
Kim HJ, Yang JC, Jung KT, Shul YG, Chun KY, Han HS, Joe YI, Kim YW, Korean J. Chem. Eng., 18(5), 662 (2001)
Larsson PO, Andersson A, J. Catal., 179(1), 72 (1998) 
Larsson PO, Andersson A, Wallenberg LR, Svensson B, J. Catal., 163(2), 279 (1996) 
Liu Y, Luo MF, Wei ZB, Xin Q, Ying PL, Li C, Appl. Catal. B: Environ., 29(1), 61 (2001) 
Reimann K, Syassen K, Solid State Commun., 76, 137 (1990) 
Sanati M, Andersson A, Wallenberg LR, Rebenstorf B, Appl. Catal. A: Gen., 106, 51 (1993) 
Satterfield CN, "Heterogeneous Catalysis in Industrial Practise," 2nd ed., McGraw-Hill, New York (1991)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
TEL. No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로