Interaction between support and V2O5 in the selective catalytic reduction of NO by NH3

被引:23
作者
Guo, Feng [1 ,2 ]
Yu, Jian [1 ]
Chu, Mo [2 ]
Xu, Guangwen [1 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
[2] China Univ Min & Technol, Sch Chem & Environm Engn, Beijing 100083, Peoples R China
基金
国家高技术研究发展计划(863计划);
关键词
OXIDE CATALYSTS; NITRIC-OXIDE; MIXED OXIDES; AMMONIA; SCR; ZIRCONIA; REMOVAL; VANADIA; SPECTROSCOPY; TEMPERATURES;
D O I
10.1039/c4cy00098f
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
V2O5-based catalysts for NH3-selective catalytic reduction (SCR) have been prepared by an impregnation method using different supports including nano-TiO2, meso-TiO2, nano-ZrO2, meso-Al2O3 and meso-SiO2. Activity evaluations clarified that V2O5/meso-TiO2 possessed the highest activity and a wide activitytemperature window of 240-400 degrees C, while V2O5/ nano-TiO2 and V2O5/ nano-ZrO2 had activities were the next most active to V2O5/ meso-TiO2. The realized NO removal was lowest over V2O5/meso-Al2O3 and V2O5/ meso-SiO2. In flue gas with 900 ppm SO2 and 10 vol.% steam the catalyst V2O5/meso-TiO2 showed the best activity stability at 350 degrees C and 240 degrees C. Characterizing the catalysts revealed that the differences in their redox properties and acidities should be responsible for their different activities and poisoning resistance. The dispersion of V2O5 on all the supports obviously decreased its H-2-reduction temperature, and the lower the reduction temperature, the better the catalyst appeared to be in activity and poisoning resistance. Overall, only the TiO2 support and its consequent interactions with V2O5 guaranteed the expected good activity and also poisoning resistance for NH3-SCR of NO. The higher pore volume of meso-TiO2 enabled a larger tolerance capacity to ammonium sulfate and sulfite so that this catalyst had better low-temperature activity stability.
引用
收藏
页码:2147 / 2155
页数:9
相关论文
共 37 条
[1]  
Belhekar A. A., 2002, CHEM COMMUN, P453
[2]   Effect of the Y2O3-ZrO2 support composition on nickel catalyst evaluated in dry reforming of methane [J].
Bellido, Jorge D. A. ;
Assaf, Elisabete M. .
APPLIED CATALYSIS A-GENERAL, 2009, 352 (1-2) :179-187
[3]   Chemical and mechanistic aspects of the selective catalytic reduction of NOx by ammonia over oxide catalysts:: A review [J].
Busca, G ;
Lietti, L ;
Ramis, G ;
Berti, F .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1998, 18 (1-2) :1-36
[4]   SCR of NO by NH3 over TiO2-supported V2O5-MoO3 catalysts:: reactivity and redox behavior [J].
Casagrande, L ;
Lietti, L ;
Nova, I ;
Forzatti, P ;
Baiker, A .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1999, 22 (01) :63-77
[5]   Promotional Effect of Ce-doped V2O5-WO3/TiO2 with Low Vanadium Loadings for Selective Catalytic Reduction of NOx by NH3 [J].
Chen, Liang ;
Li, Junhua ;
Ge, Maofa .
JOURNAL OF PHYSICAL CHEMISTRY C, 2009, 113 (50) :21177-21184
[6]   INORGANIC SOLID ACIDS AND THEIR USE IN ACID-CATALYZED HYDROCARBON REACTIONS [J].
CORMA, A .
CHEMICAL REVIEWS, 1995, 95 (03) :559-614
[7]   SILICA-SUPPORTED ZIRCONIA .1. CHARACTERIZATION BY INFRARED-SPECTROSCOPY, TEMPERATURE-PROGRAMMED DESORPTION, AND X-RAY-DIFFRACTION [J].
DANG, Z ;
ANDERSON, BG ;
AMENOMIYA, Y ;
MORROW, BA .
JOURNAL OF PHYSICAL CHEMISTRY, 1995, 99 (39) :14437-14443
[8]   Effect of vanadia and tungsten loadings on the physical and chemical characteristics of V2O5-WO3/TiO2 catalysts [J].
Djerad, S ;
Tifouti, L ;
Crocoll, M ;
Weisweiler, W .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2004, 208 (1-2) :257-265
[9]   Tungstated zirconia as promising carrier for DeNOx catalysts with improved resistance towards alkali poisoning [J].
Due-Hansen, Johannes ;
Kustov, Arkady L. ;
Rasmussen, Soren Birk ;
Fehrmann, Rasmus ;
Christensen, Claus H. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2006, 66 (3-4) :161-167
[10]   Oxidation of sulfur dioxide to sulfur trioxide over supported vanadia catalysts [J].
Dunn, JP ;
Koppula, PR ;
Stenger, HG ;
Wachs, IE .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1998, 19 (02) :103-117