The origin of the ligand effect in metal oxide catalysts: Novel fixed-bed in situ infrared and kinetic studies during methanol oxidation

Citation
Lj. Burcham et al., The origin of the ligand effect in metal oxide catalysts: Novel fixed-bed in situ infrared and kinetic studies during methanol oxidation, J CATALYSIS, 203(1), 2001, pp. 104-121
Citations number
64
Categorie Soggetti
Physical Chemistry/Chemical Physics","Chemical Engineering
Journal title
JOURNAL OF CATALYSIS
ISSN journal
00219517 → ACNP
Volume
203
Issue
1
Year of publication
2001
Pages
104 - 121
Database
ISI
SICI code
0021-9517(20011001)203:1<104:TOOTLE>2.0.ZU;2-D
Abstract
Supported and bulk metal oxide catalysts generally exhibit a "ligand effect " in the selective oxidation of methanol to formaldehyde. This phenomenon i s identified by orders of magnitude variations in the turnover frequency (T OF; TOF = activity per active surface site) of the same active metal oxide metal atom, for example, V or Mo active sites, as changes are made in the c hoice of support cation or bulk mixed metal oxide co-cation. The mechanisti c origin of this ligand effect has been investigated in the present study u sing a novel in situ IR cell designed to operate as a fixed-bed catalytic r eactor with coupling to an online gas chromatograph for analysis of gas-pha se product distributions. The active site determinations required for calcu lation of TOFs were performed using methanol chemisorption and IR spectrosc opy. Moreover, under actual methanol oxidation reaction conditions, quantif ication of the adsorbed, steady-state concentrations of methoxylated surfac e intermediates by in situ IR spectroscopy allowed for decoupling of the re action mechanism to yield individual estimates of the adsorption and surfac e reaction kinetic parameters. Comparisons of the relative values of the ad sorption equilibrium constant, K-ads, and the kinetic rate constant for the surface decomposition step, k(rds), indicate that the TOF clearly correlat es with the rate constant for the surface decomposition step. For example, supported vanadia catalysts exhibit a 12-fold increase in the surface decom position rate constant, k(rds), for vanadia supported on silica, alumina, t itania, and ceria supports. Conversely, the adsorption constant, K-ads, is relatively invariant for vanadia supported on silica, alumina, and titania, decreasing in value by about half only for the vanadia/ceria catalyst. It also appears that the origin of the ligand effect is fundamentally related to the electronegativity of the ligand cation, the more electropositive lig ands (titania and ceria support cations) always having higher TOFs than the more electronegative ligands (alumina and silica support cations). Most li kely, the ligand cation electronegativity affects the magnitude of the rate -determining surface reaction step, k(rds), via its influence on the abilit y of the active metal cation to decompose the adsorbed methoxylated surface intermediates by hydride abstraction of methyl hydrogen. (C) 2001 Academic Press.