A highly active, chemoselective and environmentally friendly Ag-In catalyst which enables the extremely difficult selective hydrogenation of acrolein to allyl alcohol is described. The catalyst performance far exceeds the space-time yield for the industrially performed synthesis of allyl alcohol by the isomerization of propene oxide, and can be regarded as a basis for a one step hydrogenation process of acrolein.
The ProblemThe preferred hydrogenation of a C=O group in the presence of a C=C bond in a,b-unsaturated aldehydes is of special interest for the chemical industry because the partially hydrogenated products, namely unsaturated alcohols of the allyl type, are used for the production of fine chemicals, pharmaceuticals, and perfumes [1]. At present, however, the most simple unsaturated alcohol, allyl alcohol, is not produced by hydrogenation of acrolein but by expensive multistep manufacturing processes [1, 2] based on allyl chloride, propene oxide or allyl acetate using basic substances and catalysts, some of them being environmentally polluting. This applies as well to cadmium containing catalysts which are said to have selective hydrogenation properties in the production of allyl alcohol from acrolein in the gas phase [3]. These disadvantages could be avoided by succeeding in selectively producing allyl alcohol with high space-time yields in a one step synthesis by selective hydrogenation of acrolein in the presence of environmentally friendly heterogeneous catalysts.The development of active and selective hydrogenation catalysts for these reactions is not only important from an industrial point of view, but is also of fundamental scientific interest for catalysis because thermodynamic and kinetic reasons favor the formation of the non-desired saturated aldehyde (free reaction enthalpy for the hydrogenation of the C=C bond is more negative by 30 kJ mol ±1 , and higher reactivity of a C=C bond compared to the C=O group [4]). While homologous a,b-unsaturated aldehydes such as cinnamaldehyde, citral or prenal can be selectively hydrogenated to the corresponding allyl alcohols (cinnamyl alcohol, geraniol/nerol, prenol) over new Pt, Rh or Ru catalysts (conditions: large (5±200 nm) metal particles; bimetallic particles modified by organic ligands; immobilized metal particles cages of zeolite Y [5]), the selective hydrogenation of C 3 -and C 4 -a,b-unsaturated aldehydes (acrolein, crotonaldehyde) is much more difficult. It has to be noted that acrolein is the a,b-unsaturated aldehyde which is the most difficult to hydrogenate at the carbonyl group: When using monometallic supported catalysts with typical Group VIII elements useful for hydrogenations, the selectivity to allyl alcohol is smaller than 10 % [5, 6]. Even the bimetallic Rh-Sn/SiO 2 catalysts developed by our research group, which still selectively hydrogenate crotonaldehyde in the gas phase under optimal reaction conditions to crotyl alcohol (S = 68 %), exhibit lower turnover frequencies (TOF) by a factor of two to three during the acrolein hydrogenat...