Model bulk Mo-V-Te-O catalysts for selective oxidation of propane to acrylic acid

被引:31
作者
Al-Saeedi, JN [1 ]
Vasudevan, VK [1 ]
Guliants, VV [1 ]
机构
[1] Univ Cincinnati, Dept Chem & Mat Engn, Cincinnati, OH 45221 USA
基金
美国国家科学基金会;
关键词
Mo-V-Te oxides; M1 and M2 phases; TEM; crystal structure;
D O I
10.1016/j.catcom.2003.08.007
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 crystal structures and chemical compositions of the M I and M2 phases proposed as active and selective in propane oxidation to acrylic acid over the bulk mixed Mo-V-Te-O catalysts were investigated by the transmission electron microscopy, coupled with energy dispersive analysis of X-rays. The results revealed that the crystal structure of the M I phase is orthorhombic with space group Pbca, lattice parameters a = 21.25 Angstrom, b = 27.14 Angstrom, c = 4.03 Angstrom and composition Mo0.64V0.32Te0.1O3.05 (Mo/Vsimilar to2), whereas M2 is hexagonal with space group P6mm, lattice parameters a = 7.10 Angstrom. c = 4.05 Angstrom and composition Mo1.79V1.85Te0.1O11.36 (Mo/Vsimilar to1). The M I phase was dominant in the Mo-V-Te-O catalyst. The results obtained indicated that the bulk Mo-V-Te oxides represent a well-defined model catalytic system for the studies of the surface molecular structure-activity/selectivity relationships in propane oxidation to acrylic acid. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:537 / 542
页数:6
相关论文
共 20 条
[1]   Bulk structure and catalytic properties of mixed Mo-V-Sb-Nb oxides for selective propane oxidation to acrylic acid [J].
Al-Saeedi, JN ;
Guliants, VV ;
Guerrero-Pérez, O ;
Bañares, MA .
JOURNAL OF CATALYSIS, 2003, 215 (01) :108-115
[2]   High-throughput experimentation in multicomponent bulk mixed metal oxides: Mo-V-Sb-Nb-O system for selective oxidation of propane to acrylic acid [J].
Al-Saeedi, JN ;
Guliants, VV .
APPLIED CATALYSIS A-GENERAL, 2002, 237 (1-2) :111-120
[3]  
ALSAEEDI JN, 2003, 225 ACS NAT M NEW OR
[4]   Crystal chemistry and phase composition of the MoVTeNbO catalysts for the ammoxidation of propane [J].
Aouine, M ;
Dubois, JL ;
Millet, JMM .
CHEMICAL COMMUNICATIONS, 2001, (13) :1180-1181
[5]   On the partial oxidation of propane and propylene on mixed metal oxide catalysts [J].
Bettahar, MM ;
Costentin, G ;
Savary, L ;
Lavalley, JC .
APPLIED CATALYSIS A-GENERAL, 1996, 145 (1-2) :1-48
[6]  
Buttrey DJ, 2002, ABSTR PAP AM CHEM S, V224, pU272
[7]   Advances and future trends in selective oxidation and ammoxidation catalysis [J].
Grasselli, RK .
CATALYSIS TODAY, 1999, 49 (1-3) :141-153
[8]   Solid state chemistry of bulk mixed metal oxide catalysts for the selective oxidation of propane to acrylic acid [J].
Holmes, SA ;
Al-Saeedi, J ;
Guliants, VV ;
Boolchand, P ;
Georgiev, D ;
Hackler, U ;
Sobkow, E .
CATALYSIS TODAY, 2001, 67 (04) :403-409
[9]   Selective oxidation of propane to acrylic acid with molecular oxygen [J].
Lin, MM .
APPLIED CATALYSIS A-GENERAL, 2001, 207 (1-2) :1-16
[10]   NEW COMPLEX STRUCTURES IN THE CESIUM-NIOBIUM-TUNGSTEN-OXIDE SYSTEM REVEALED BY HREM [J].
LUNDBERG, M ;
SUNDBERG, M .
ULTRAMICROSCOPY, 1993, 52 (3-4) :429-435