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.
|Number of pages||7|
|Publication status||Published - 30 Mar 2001|
|MoE publication type||A4 Article in a conference publication|
|Event||Catalysis in Multiphase Reactors - Napoles, Italy|
Duration: 29 May 2000 → 29 May 2000
- Enantioselective hydrogenation
- Pt/AlO catalyst