Chinese Journal of Catalysis ›› 2012, Vol. 33 ›› Issue (12): 1965-1973.DOI: 10.3724/SP.J.1088.2012.20746

• Research papers • Previous Articles     Next Articles

Influence of MnOx Loading on Activity of MnOx/Ce0.7Zr0.2La0.1O2-Al2O3 Catalyst for Catalytic Combustion of Diesel Soot

ZHU Yi1, PAN Hao2, CHEN Shanhu2, WANG Shidan2, ZHAO Ming2, GONG Maochu2, CHEN Yaoqiang2,*   

  1. 1College of Architecture and Environment, Sichuan University, Chengdu 610065, Sichuan, China; 2Key Laboratory of Green Chemistry and Technology of the Ministry of Education, College of Chemistry, Sichuan University, Chengdu 610064, Sichuan, China
  • Received:2012-07-30 Revised:2012-09-06 Online:2013-01-18 Published:2012-12-18

Abstract: A series of MnOx/Ce0.7Zr0.2La0.1O2-Al2O3 supported catalysts with the Ce0.7Zr0.2La0.1O2:Al2O3 mass ratio of 1:1 and different MnOx loadings were prepared by the incipient wetness method. The catalysts were characterized by X-ray diffraction, low temperature N2 adsorption-desorption, X-ray photoelectron spectroscopy, O2 temperature-programmed desorption, and H2 temperature-programmed reduction. The catalytic performance of these catalysts for the combustion of diesel soot was investigated. It is found that surface-adsorbed active oxygen species and low-temperature reducibility of MnOx are the determinants of catalytic activity. When the MnOx loading is 5%, the catalyst activity decreases owing to the loss of active oxygen species, which are necessary for the catalytic combustion. When the MnOx loading is increased to 10%, the catalyst activity is dramatically increased because of the enhanced reducible manganese species. Interestingly, the optimal values for reducible manganese species and surface-adsorbed oxygen species can be achieved in the catalyst with 20% MnOx, and so the catalyst exhibits the best catalytic activity, giving a light-off temperature about 179 oC lower than that of the non-catalytic soot combustion. With a further addition of MnOx species up to 30%, its catalytic activity is deteriorated mainly due to the decrease in surface-trapped oxygen species and upper shift of the reduction temperature.

Key words: manganese oxide, loading amount, soot, catalytic combustion, ceria, zirconia, lanthana, alumina