Effect of modifier structure in asymmetric 1-phenylpropane-1,2-dione hydrogenation

A1 Originalartikel i en vetenskaplig tidskrift (referentgranskad)


Interna författare/redaktörer


Publikationens författare: Busygin I, Toukoniitty E, Leino R, Murzin DY
Förläggare: ELSEVIER SCIENCE BV
Publiceringsår: 2005
Tidskrift: Journal of Molecular Catalysis A: Chemical
Tidskriftsakronym: J MOL CATAL A-CHEM
Volym: 236
Nummer: 1-2
Artikelns första sida, sidnummer: 227
Artikelns sista sida, sidnummer: 238
Antal sidor: 12
ISSN: 1381-1169


Abstrakt

Sixteen chiral catalyst modifiers including the natural cinchona alkaloids cinchonidine, cinchonine and quinine together with their several analogues were studied in the hydrogenation of 1-phenylpropane-1,2-dione over a 5% Pt/Al(2)O(3) catalyst at 10 bar H(2) and 15 degrees C. The influence of the different functional parts of the cinchona alkaloid on the reaction rate, enantio and regioselectivity and diol distribution was investigated. The modifier hydroxyl group in C-9 position is crucial for achieving high enantioselectivity. Replacement of the 9-OH group with a methyl ether results in a complete loss of enantioselectivity for cinchonidine and quinine, whereas an inversion of enantioselectivity was observed for the cinchonine-based modifiers. The role of the absolute configuration at C-8 and -9, the bicyclic quinuclidine part and aromatic system of the cinchona alkaloid on the reaction kinetics was studied as well. Acetic acid is detrimental for enantioselectivity in the hydrogenation of 1-phenylpropane-1,2-dione to the corresponding hydroxyketones whereas in the second hydrogenation step from hydroxyketones to diols, high enantiomeric excesses are observed. The results obtained demonstrate the principal dissimilarity in the enantiodifferentiating mechanism between the well-investigated a-keto esters and vicinal diketones. (c) 2005 Elsevier B.V. All rights reserved.


Nyckelord

1-phenylpropane-1,2-dione, chiral modifiers, cinchonidine, enantioselective hydrogenation, platinum catalyst

Senast uppdaterad 2020-19-02 vid 06:38