Bulk mixed Mo-V-Te-O catalysts for propane oxidation to acrylic acid

被引:66
作者
Guliants, VV [1 ]
Bhandari, R
Al-Saeedi, JN
Vasudevan, VK
Soman, RS
Guerrero-Pérez, O
Bañares, MA
机构
[1] Univ Cincinnati, Dept Chem & Mat Engn, Cincinnati, OH 45221 USA
[2] Univ Cincinnati, Coll Appl Sci, Cincinnati, OH 45206 USA
[3] CSIC, Inst Catalisis & Petroleoquim, E-28049 Madrid, Spain
基金
美国国家科学基金会;
关键词
mixed Mo-V-Te oxides; hydrothermal synthesis; phase diagram; propane oxidation;
D O I
10.1016/j.apcata.2004.05.049
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 model Mo-V-Te-O catalysts containing the orthorhombic (M1) and hexagonal (M2) phases with well-defined crystal morphologies and promising for the selective oxidation of propane to oxygenates were obtained hydrothermally over a wide range of synthesis compositions (MO0.70-0.30V0.60-0.2OTe0.15-0.05). The bulk (ICP), local (EDS) elemental and structural (XRD) analyses of this compositionally simple model system indicated that the M1 phase with the bulk Mo/V ratio of similar to2 was dominant in the Mo-V-Te-O catalysts. This phase has been proposed as active and selective for propane oxidation to oxygenates and ammoxidation to acrylonitrile. The model catalysts displayed high selectivity to acrylic acid in the presence of water vapor in the feed, which is believed to enhance the apparent rates of formation of oxygenates as well as maintain the catalytic surface in a partially reduced oxidation state. The selectivity to acrylic acid over these model catalysts correlated with the extent of exposure of the surface ab planes of the M1 phase proposed to contain the active and selective surface sites. Therefore, the Mo-V-Te-O catalysts represent a well-defined and highly promising model system for elucidating the surface molecular structure-activity/selectivity relationships in propane oxidation to acrylic acid over multicomponent Mo-V-Te-Nb-O catalysts. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:123 / 132
页数:10
相关论文
共 36 条
[1]   Model bulk Mo-V-Te-O catalysts for selective oxidation of propane to acrylic acid [J].
Al-Saeedi, JN ;
Vasudevan, VK ;
Guliants, VV .
CATALYSIS COMMUNICATIONS, 2003, 4 (10) :537-542
[2]   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
[3]   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
[4]   Propane oxidation on MoVTeNbO mixed oxide catalysts: study of the phase composition of active and selective catalysts [J].
Baca, M ;
Pigamo, A ;
Dubois, JL ;
Millet, JMM .
TOPICS IN CATALYSIS, 2003, 23 (1-4) :39-46
[5]   Simple chemical processes based on low molecular-mass alkanes as chemical feedstocks [J].
Baerns, M ;
Buyevskaya, O .
CATALYSIS TODAY, 1998, 45 (1-4) :13-22
[6]   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
[7]   Preparation, characterisation and catalytic behaviour of a new TeVMoO crystalline phase [J].
Botella, P ;
Nieto, JML ;
Solsona, B .
CATALYSIS LETTERS, 2002, 78 (1-4) :383-387
[8]   In situ IR, Raman, and UV-Vis DRS spectroscopy of supported vanadium oxide catalysts during methanol oxidation [J].
Burcham, LJ ;
Deo, G ;
Gao, XT ;
Wachs, IE .
TOPICS IN CATALYSIS, 2000, 11 (1-4) :85-100
[9]   Selective oxidation of light alkanes: Interaction between the catalyst and the gas phase on different classes of catalytic materials [J].
Cavani, F ;
Trifirò, F .
CATALYSIS TODAY, 1999, 51 (3-4) :561-580
[10]  
Cavani F, 1997, STUD SURF SCI CATAL, V110, P19