Enhanced soot oxidation by lattice oxygen via La3+-doped CeO2

被引:386
作者
Bueno-López, A [1 ]
Krishna, K [1 ]
Makkee, M [1 ]
Moulijn, JA [1 ]
机构
[1] Delft Univ Technol, NL-2628 BL Delft, Netherlands
关键词
active oxygen; catalysed soot oxidation; ceria; lanthana; oxygen exchange; solid solution; soot; temporal analysis of products;
D O I
10.1016/j.jcat.2004.11.027
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The catalytic behaviours of CeO2 and a series of La3+-doped CeO2 catalysts (La3+ loading between 5 and 50 wt%) have been studied for soot oxidation by O-2. XRD and Raman spectroscopy characterisation indicated that solid Solutions are formed in the studied Ce/La ratio, in which La3+ cations replace Ce4+ cations in the CeO2 lattice. Thermogravimetric analysis showed that La3+ significantly improves CeO2 catalytic activity for soot oxidation with O-2. The best catalytic activity was found with 5 wt% La3+-doped CeO2 catalyst (CeO2-5La), in both loose and tight contact conditions. This improvement seems to be related to the increase in BET surface area and the change in the catalyst redox properties of CeO2 brought about by doping with La3+. La3+ decreases the onset temperature of Ce4+ to Ce3+ reduction by H-2 from 580 degreesC (CeO2) to 325 degreesC (CeO2)-5La) and increases the amount of Ce4+ that can be reduced by H-2 (maximum amount for CeO2-5La catalyst). An advanced TAP reactor is used for the first time to study catalysed soot oxidation with labelled oxygen. In the absence of catalyst, oxidation starts above 500degreesC, and mainly labelled oxidation species (CO and CO2)) were found. In the presence of catalyst, it is shown that the gas-phase labelled oxygen replaces nonlabelled lattice oxygen, creating the highly active nonlabelled oxygen. This highly active nonlabelled oxygen reacts with soot, giving CO and CO2. The creation Of Such active oxygen species starts front 400 degreesC and thereby decreases the soot oxidation temperature. CeO2-5La produces more such active species, for example, leading to 98% oxygen conversion at 400 degreesC compared with 37% over CeO2 alone under identical circumstances. (C) 2004 Elsevier Inc. All rights reserved.
引用
收藏
页码:237 / 248
页数:12
相关论文
共 23 条
[1]  
CAMPERON T, 2004010071 SAE
[2]   Urban air quality [J].
Fenger, J .
ATMOSPHERIC ENVIRONMENT, 1999, 33 (29) :4877-4900
[3]   Structural characteristics and redox behavior of CeO2-ZrO2/Al2O3 supports [J].
Fernández-García, M ;
Martínez-Arias, A ;
Iglesias-Juez, A ;
Belver, C ;
Hungría, AB ;
Conesa, JC ;
Soria, J .
JOURNAL OF CATALYSIS, 2000, 194 (02) :385-392
[4]   Redox behavior of high surface area Rh-loaded Ce0.5Zr0.5O2 mixed oxide [J].
Fornasiero, P ;
Kaspar, J ;
Graziani, M .
JOURNAL OF CATALYSIS, 1997, 167 (02) :576-580
[5]   Automotive exhaust catalysis [J].
Gandhi, HS ;
Graham, GW ;
McCabe, RW .
JOURNAL OF CATALYSIS, 2003, 216 (1-2) :433-442
[6]   RE0.6Zr0.4-xyxO2 (RE = Ce, Pr;: x=0, 0.05) solid solutions:: an investigation on defective structure, oxygen mobility, oxygen storage capacity, and redox properties [J].
He, H ;
Dai, HX ;
Wong, KW ;
Au, CT .
APPLIED CATALYSIS A-GENERAL, 2003, 251 (01) :61-74
[7]   Thermal stability of oxygen storage properties in a mixed CeO2-ZrO2 system [J].
Hori, CE ;
Permana, H ;
Ng, KYS ;
Brenner, A ;
More, K ;
Rahmoeller, KM ;
Belton, D .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1998, 16 (02) :105-117
[8]   The red-ox treatments influence on the structure and properties of M2O3-CeO2-ZrO2 (M = Y, La) solid solutions [J].
Ikryannikova, LN ;
Aksenov, AA ;
Markaryan, GL ;
Murav'eva, GP ;
Kostyuk, BG ;
Kharlanov, AN ;
Lunina, EV .
APPLIED CATALYSIS A-GENERAL, 2001, 210 (1-2) :225-235
[9]   NO reduction by activated carbons .7. Some mechanistic aspects of uncatalyzed and catalyzed reaction [J].
IllanGomez, MJ ;
LinaresSolano, A ;
Radovic, LR ;
deLecea, CSM .
ENERGY & FUELS, 1996, 10 (01) :158-168
[10]   Use of CeO2-based oxides in the three-way catalysis [J].
Kaspar, J ;
Fornasiero, P ;
Graziani, M .
CATALYSIS TODAY, 1999, 50 (02) :285-298