Abstract
The kinetics of the selective oxidation of isobutene to methacrolein over multicomponent molybdate catalyst were investigated in a differential tubular flow reactor at low conversion levels. The study was carried out over the temperature range 609 to 694 K. The data were fitted to a number of standard kinetic models based on Mars-van Krevelen and Langmuir-Hinshelwood mechanisms, and also to the empirical power rate law model. The kinetics of the formation of methacrolein were best represented by the redox model in which non-dissociated oxygen is involved in the reoxidation step. The rate determining step was found to be the catalyst reduction with an energy of activation of 177 kJ/mol. The activation energy for catalyst reoxidation is found to be 71 kJ/mol.
Original language | English |
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Pages (from-to) | 149-159 |
Number of pages | 11 |
Journal | Applied Catalysis |
Volume | 70 |
Issue number | 1 |
DOIs | |
Publication status | Published - 1 Jan 1991 |
Keywords
- catalyst preparation (co-precipitation).
- isobutene
- kinetics
- methacrolein
- multicomponent molybdate catalyst
- redox model
- selective oxidation
ASJC Scopus subject areas
- Engineering(all)