Sammanfattning
A kinetic model was developed for the enantioselective hydrogenation of 1-phenyl-1,2-propanedione based on parallel racemic and enantioselective routes in the presence of cinchonidine. The Langmuir-Hinshelwood type of competitive adsorption approach was used in the model, which was combined with a batch reactor model. The proposed model could sufficiently describe the observed kinetic results.
| Originalspråk | Engelska |
|---|---|
| Sidor (från-till) | 411-417 |
| Antal sidor | 7 |
| Tidskrift | Catalysis Today |
| Volym | 66 |
| Nummer | 2-4 |
| DOI | |
| Status | Publicerad - 30 mars 2001 |
| MoE-publikationstyp | A4 Artikel i en konferenspublikation |
| Evenemang | Catalysis in Multiphase Reactors - Napoles, Italien Varaktighet: 29 maj 2000 → 29 maj 2000 |
Finansiering
The authors are grateful to Mr. Markku Reunanen for his contribution to the GC–MS analyses and to Mr. Kari Eränen for the construction of the hydrogenation equipment. The financial support received from the Academy of Finland and the Graduate School in Chemical Engineering is gratefully acknowledged.
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