Abstract
Highest catalytic performance for complete oxidation of propylene and toluene was obtained by using a Pt catalyst on a mesoporous silica support with pore sizes from 20 to 50 nm and 10 to 40 nm, respectively.
Similar content being viewed by others
References
K. Everaert, J. Baeyens: J. Hazar. Mater. B, 109, 113 (2004).
O. Duclaux, T. Chafic, H. Zaitan, J.L. Gass, D. Bianchi: React. Kinet. Catal. Lett., 76, 19 (2002).
M. Rahmani, M. Sofrabi: React. Kinet. Catal. Lett., 86, 397 (2005).
http://www.fuji-silysia.co.jp/english/product/catalyst_support_silica/cariact.html
K. Ogasawara, T. Kato, N. Okuda, T. Konishi, K. Kato: US patent 5853693 (1998).
K. Okabe, X. Li, M. Toba, Y. Yoshimura: React. Kinet. Catal. Lett., 86, 3 (2005).
Satterfield CN: Mass Transfer in Heterogeneous Catalysis, Cambridge, MIT Press (1970).
R.B. Bird, W.E. Stewart, E.N. Lightfoot: Transport Phenomena, Wiley & Sons Inc. (1960).
N. Wakao, J.M. Smith: Chem. Eng. Sci., 17, 825 (1962).
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Uchisawa, J., Nanba, T., Masukawa, S. et al. Optimization of silica support pore size for Pt catalysts in the complete oxidation of volatile organic compounds. React Kinet Catal Lett 95, 391–398 (2008). https://doi.org/10.1007/s11144-008-5364-9
Received:
Revised:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s11144-008-5364-9