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Application of transient methods in three-phase catalysis: Hydrogenation of a dione in a catalytic plate column

Tutkimustuotos: LehtiartikkeliKonferenssiartikkeliTieteellinenvertaisarvioitu

7 Sitaatiot (Scopus)

Abstrakti

The continuous enantioselective hydrogenation of 1-phenyl-1,2-propanedione was investigated in fixed-bed reactor at 25°C and 5 bar H2 over a knitted Pt silica fibre catalyst modified with (-)-cinchonidine. Transient data were quantitatively modelled based on the reaction mechanism which assumes two parallel and tilted adsorption modes for the modifier and two distinct adsorption modes for 1- and 2-carbonyls, each of them requiring different number of surface sites. A dynamic axial dispersion model described the tube reactor with the Peclet number estimated from the separate impulse experiments carried out with an inert tracer. The modelling revealed that inclusion of sorption dynamics of components is of critical importance for the adequate description of transient data.

AlkuperäiskieliEnglanti
Sivut383-389
Sivumäärä7
JulkaisuCatalysis Today
Vuosikerta79-80
DOI - pysyväislinkit
TilaJulkaistu - 30 huhtik. 2003
OKM-julkaisutyyppiA4 Artikkeli konferenssijulkaisuussa
TapahtumaCatalysis in Multiphase Reactors - Naples, Italy
Kesto: 29 toukok. 200029 toukok. 2000

Rahoitus

This work is part of the activities at the Åbo Akademi Process Chemistry Group within the Finnish Centre of Excellence Programme (2000–2005) by the Academy of Finland. Financial support from Finnish Graduate School in Chemical Engineering (GSCE) is gratefully acknowledged.

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