Abstract
The dehydrogenation of isobutane over supported chromium oxide catalysts was studied by a combination of in situ UV-Vis diffuse reflectance spectroscopy and on line GC analysis. A well-defined set of experiments, based on an experimental design, was carded out to develop mathematical models, which quantitatively relate Cr-speciation and dehydrogenation activity with reaction temperature and time, support composition, gas composition and Cr loading. It will be shown that: (1) the dehydrogenation activity is proportional with the amount of in situ measured surface Cr2+/3+, and maximum for a 7.5 wt.% Cr/Al2O3 catalyst operating at 500°C in 2% isobutane in N2; and (2) Cr3+-sites are more active in alkane dehydrogenation than Cr2+-sites. This paper is the first example of the use of experimental design for deriving structure-activity relationships in the field of heterogeneous catalysis. (C) 2000 Elsevier Science B.V.
| Original language | English |
|---|---|
| Pages (from-to) | 115-131 |
| Number of pages | 17 |
| Journal | Journal of Molecular Catalysis A: Chemical |
| Volume | 151 |
| Issue number | 1-2 |
| DOIs | |
| Publication status | Published - 15 Feb 2000 |
| Externally published | Yes |
Funding
B.M.W. is a postdoctoral fellow of the Fonds voor Wetenschappelijk Onderzoek-Vlaanderen (FWO). A.A.V. acknowledges a doctoral research grant of the Instituut voor Wetenschap en Technologie (IWT). This work was financially supported by the Geconcerteerde Onderzoeksactie (GOA) of the Flemish Government and by the FWO.
Keywords
- Chemometrics
- Diffuse reflectance spectroscopy
- Experimental design
- In situ spectroscopy
- Supported chromium oxide catalysts