Investigation of the structure and activity of VOx/ZrO2/SiO2 catalysts for methanol oxidation to formaldehyde

被引:25
作者
Vining, William C.
Strunk, Jennifer
Bell, Alexis T. [1 ]
机构
[1] Univ Calif Berkeley, Dept Chem & Biomol Engn, Berkeley, CA 94720 USA
基金
美国国家卫生研究院;
关键词
Methanol; Formaldehyde; Oxidation; Vanadia; Ziirconia; Silica; VANADIUM-OXIDE CATALYSTS; X-RAY-ABSORPTION; MOLECULAR-STRUCTURES; SELECTIVE OXIDATION; RUTILE TIO2(110); SOLID-SOLUTIONS; ZIRCONIA; SILICA; SPECTROSCOPY; TITANIA;
D O I
10.1016/j.jcat.2011.05.001
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
High surface area silica-supported bilayered VOx/ZrO2/SiO2 catalysts were prepared with a constant vanadium surface density of 0.5 V nm(-2) and zirconium surface coverages ranging from 0.0 to 2.1 Zr nm(-2). In all cases, the zirconia layer was predominantly amorphous in nature. The vanadia existed as isolated tetrahedral O=V(-OM)(3) (M = Si, Zr) regardless of zirconia surface density. At least two distinct tetrahedral vanadia environments were identified by V-51 NMR on the support: O=V(O-Si)(3) and O=V(O-Zr)(3), with up to 35% of all V in the latter site at the highest Zr loading. The fraction of V bound to Zr as determined by V-51 NMR agrees with an independent determination of the fraction of sites reduced by methanol at 600 K, a temperature too low for significant reduction of vanadia on silica. The turnover frequency for methanol oxidation increased by nearly two orders of magnitude as the Zr loading was increased. When normalized by the number of O=V(O-Zr)(3) sites determined from V-51 NMR and UV-Visible, the turnover frequency for methanol oxidation to formaldehyde was constant with zirconia surface coverage. It is proposed that the much higher activity of O=V(O-Zr)(3) compared with O=V(O-Si)(3) sites is attributable to differences in the mechanism by which H-abstraction from V-OCH3 groups in the rate-limiting step leads to formaldehyde formation associated with the two types of sites. (C) 2011 Elsevier Inc. All rights reserved.
引用
收藏
页码:222 / 230
页数:9
相关论文
共 48 条
[1]   In situ UV-visible spectroscopic measurements of kinetic parameters and active sites for catalytic oxidation of alkanes on vanadium oxides [J].
Argyle, MD ;
Chen, KD ;
Iglesia, E ;
Bell, AT .
JOURNAL OF PHYSICAL CHEMISTRY B, 2005, 109 (06) :2414-2420
[2]   Methanol: a "smart" chemical probe molecule [J].
Badlani, M ;
Wachs, IE .
CATALYSIS LETTERS, 2001, 75 (3-4) :137-149
[3]   OPTICAL ENERGY GAPS IN MONOCLINIC OXIDES OF HAFNIUM AND ZIRCONIUM AND THEIR SOLID SOLUTIONS [J].
BENDORAI.JG ;
SALOMON, RE .
JOURNAL OF PHYSICAL CHEMISTRY, 1965, 69 (10) :3666-&
[4]   Mechanistic studies of methanol oxidation to formaldehyde on isolated vanadate sites supported on high surface area zirconia [J].
Bronkema, Jason L. ;
Bell, Alexis T. .
JOURNAL OF PHYSICAL CHEMISTRY C, 2008, 112 (16) :6404-6412
[5]   Mechanistic studies of methanol oxidation to formaldehyde on isolated vanadate sites supported on MCM-48 [J].
Bronkema, Jason L. ;
Bell, Alexis T. .
JOURNAL OF PHYSICAL CHEMISTRY C, 2007, 111 (01) :420-430
[6]   The origin of the support effect in supported metal oxide catalysts: in situ infrared and kinetic studies during methanol oxidation [J].
Burcham, LJ ;
Wachs, IE .
CATALYSIS TODAY, 1999, 49 (04) :467-484
[7]   REACTIVITY OF SUPPORTED VANADIUM-OXIDE CATALYSTS - THE PARTIAL OXIDATION OF METHANOL [J].
DEO, G ;
WACHS, IE .
JOURNAL OF CATALYSIS, 1994, 146 (02) :323-334
[8]   Oxidation of methanol to formaldehyde on supported vanadium oxide catalysts compared to gas phase molecules [J].
Döbler, J ;
Pritzsche, M ;
Sauer, J .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2005, 127 (31) :10861-10868
[9]   SOLID-STATE V-15 NMR STRUCTURAL STUDIES ON SUPPORTED VANADIUM(V) OXIDE CATALYSTS - VANADIUM-OXIDE SURFACE-LAYERS ON ALUMINA AND TITANIA SUPPORTS [J].
ECKERT, H ;
WACHS, IE .
JOURNAL OF PHYSICAL CHEMISTRY, 1989, 93 (18) :6796-6805
[10]   Vanadium oxide catalysts supported on zirconia and titania I. Preparation and characterization [J].
Enache, DI ;
Bordes-Richard, E ;
Ensuque, A ;
Bozon-Verduraz, F .
APPLIED CATALYSIS A-GENERAL, 2004, 278 (01) :93-102