Abstract
In a two-phase (supercritical fluid-fluid) system, the rate of conversion of a bimolecular reaction A + B → AB reacting in the layer adjacent to the interface and in the bulk phase was determined. The mass transfer associated with the chemical reaction was measured in a stirred and thermostatically controlled cell varying reaction temperature, pressure and stirring speed. As model system, the Diels-Alder reaction between 9-hydroxymethylanthracene and maleic acid was chosen in the solvent pair supercritical propane/water. The cell was developed for high pressures and temperatures. The reaction was monitored in both phases with on line UV-spectroscopy. The experimental results are compared to simulated data obtained by using a film model. An improved theoretical model describing the changes in concentration of the reactants in the two phases is presented.
Original language | English |
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Pages (from-to) | 335-344 |
Number of pages | 10 |
Journal | Catalysis Today |
Volume | 66 |
Issue number | 2-4 |
DOIs | |
State | Published - 30 Mar 2001 |
Event | Catalysis in Multiphase Reactors - Napoles, Italy Duration: 29 May 2000 → 29 May 2000 |
Keywords
- Mass transfer with chemical reaction
- Stirred cell for high pressure
- Supercritical fluid