Noble metal catalysts

The invention relates to catalyst systems consisting of supported or unsupported transition metal catalysts whose surface has been modified with defined amounts of organic modifiers, to a process for their preparation and to their use.

Owing to their ease of recycleability and their possible use in continuous processes, heterogeneous catalysts find wide use in the production of base chemicals, chemical intermediates, and fine chemical and pharmaceutical products. Fine chemical and pharmaceutical catalytic processes have a high substrate specificity, i.e. particular functional groups in polyfunctional organic substrates have to be converted. The known heterogeneous catalysts usually lead to a lower selectivity of the catalytic reaction compared to homogeneous catalysts.

It is known that the selectivity with respect to particular functional groups of an organic starting molecule can be improved by modifying heterogeneous catalysts with small amounts of organic or inorganic compounds. This modification of heterogeneous catalysts opens up the possibility of widening the scope of application of a commercial solid catalyst because the chemical structure and the amount of the modifier can be adjusted in a controlled manner to the requirements of a particular chemical reaction.

The compounds which are used to modify the catalyst surface are referred to in the technical literature by different terms, for example, modifier, promoter, additive, regulator, selective catalyst poison or co- catalyst .

The term "modifier" is used hereinafter, though this

term should be understood to be entirely synonymous with the other names.

The modifiers have the property of entering into adsorptive interactions with the catalyst surface and in this way inducing desired changes in the activity and selectivity of the catalysts

a) by the variation of the number of active sites on the catalyst surface or

b) by the change in the electronic properties of the active sites on the catalyst surface or

c) by the introduction of organocatalytic functionalities, i.e. by the use of small, simple, possible chiral organic molecules, which can catalyse various reactions in a highly selective manner even without the presence of metals (Figure 1) .

Modifiers for heterogeneous catalysts consist of a structural unit which enables the adhesion (adsorption) of the modifier on the catalyst surface.

In addition, the modifiers for case c) (cf. Figure Ic) may have structural units with organocatalytic activity. The structural units in question may, for example, be amino acid or peptide structures or organo- metallic complex ligands which, even without the presence of a further metal, can catalyse chemical reactions in a highly selective manner ¹ .

The organocatalytic functional groups may also have chiral centres, such that the interaction between modifier and reaction substrate can cause chiral induction on the part of the substrates.

The known examples of a change in number or the properties of active sites of the catalyst with modifiers (partial poisoning of the active sites) includes the partial hydrogenation of alkynes to alkenes, in which the most frequently used modifiers are quinoline, but also diamines. This catalyst system finds use in the form of the so-called Lindlar catalysts ¹¹ . It is assumed that there is competing adsorption of the substrate, of the product and of the modifier.

Addition of nitrogen bases to Pd/C catalysts allows the hydrogenolysis of benzyl ether to be suppressed selectively in the presence of other reducible functional groups such as olefin, benzyl ester, nitro groups ¹¹¹ . However, aromatic N-Cbz (benzyloxycarbonyl) and haloaromatic groups are hydrogenated. In the absence of the N-bases there is in each case complete hydrogenolysis ^lv .

The use of diphenyl sulphide as a catalyst poison leads to a further expansion of the scope of application of the Pd/C catalyst. For instance, it was possible with a catalyst system modified in this way to hydrogenate olefin and acetylene groups while simultaneously suppressing the hydrogenolysis of aromatic carbonyl and halogen, benzyl ester and N-Cbz groups ^v . Further S- containing modifiers studied were thiophenol, diphenyl sulphone, diphenyl sulphoxide and diphenyl disulphide.

The examples mentioned for the modification of heterogeneous catalysts have the aim of influencing the chemoselectivity via partial poisoning of the surface. The known modification of heterogeneous catalysts with organic molecules is preparatively simple and inexpensive. Especially in catalytic applications in which the number or properties of the active sites according to Fig. Ia) and b) are influenced by

adsorption of simple nitrogen-containing bases and sulphur compounds, many successful catalyst systems are known .

However, when the objective of the catalyst modification is to control stereo-, diastereo- and enantioselectivities, a simple molecule which is adsorbed selectively on the catalyst surface is inadequate .

In this case, the modifier molecules, as well as groups which enable the adsorption on the catalyst surface, require additional organocatalytic functionalities which enter into controlled interactions with the functional groups of the reaction substrate at the surface of the catalyst.

In stereo-, diastereo- and enantioselective reactions in which catalysts having organocatalytic functionalities according to Fig. Ic) are required, the number of successful applications for modified catalysts is still very limited.

The significance of amines for this type of reaction becomes clear with regard to the hydrogenation of l-methylindene-2-carboxylic acid (1-MICA) in the presence of PdMl ₂ O ₃ ^V1 (Figure 2) .

The syn addition of two hydrogen atoms adsorbed on the Pd surface predominantly gives rise to the cis product.

In the case of addition of modifiers (cinchonidine and quinuclidine) , the trans/cis ratio is more than doubled. The influence of the tertiary amine modifiers is explained by the acid-base interactions between 1-MICA and the modifier which promotes the adsorption and hydrogenation of 1-MICA in the "upside-down" position .

In the case of enantioselective catalytic reactions, noble metal supported catalysts combined with chiral modifiers can transmit chiral information directly to particular substrate groups.

The combination of Pt/Al ₂ θ3/cinchona alkaloid allows α-ketocarboxylic esters to be hydrogenated with enantioselectivities of 85-98% ^V11 (Figure 3) .

The stereoselective hydrogenation of β-ketocarboxylic esters ^V111 , with Raney nickel as a catalyst and tartaric acid as a chiral modifier and NaBr as a promoter leads to stereoselectivities for the hydroxyl esters of approximately 80-98%. Further suitable substrates are other β-functionalized ketones and sterically demanding methyl ketones ^lx .

The combination of palladium with unsubstituted cinchona alkaloids or some vinca alkaloids gives rise to enantioselective catalysts for α, β-unsaturated carboxylic acids (ee up to 74%) and hydroxymethylpyrones (ee up to 94%) ^x .

Some other supported Pd catalysts with chiral modifiers (for example, amino alcohols, amino acids) have been reported, but the enantioselectivities achieved were only approximately 20-25%.

The overall impression is that the successful applications in the field of stereo-, diastereo- and enantioselective reactions are restricted to readily activable substrates which are converted under mild reaction conditions (low H ₂ pressure in the case of hydrogenation, low temperature) .

One cause of this is suspected to lie in the limited inertness and in the undesirable degradation of the

chiral modifier during the catalytic reaction.

For instance, it is known that cinchona modifiers which are used in the enantioselective hydrogenation in conjunction with Pt catalysts are adsorbed as a result of the interaction between their aromatic ring system and the catalyst surface. This aromatic group is, however, hydrogenated during the reaction. This leads to the detachment of the modifier from the catalyst and hence to the decline or complete loss of selectivity.

Furthermore, adsorption groups which enter into more labile adsorption interactions have the disadvantage that the adsorption of these molecules requires specific metal surfaces or adsorption sites. The usability of corresponding modifiers is therefore tied to particular metal particle structures, support materials and to narrowly-specified preparation methods of the heterogeneous catalysts.

Functioning enantioselective Pt-cinchona alkaloid systems are based, for example, on AI2O3 as the support material. Activated carbon-supported catalysts, in contrast, exhibit only low selectivities .

It is an object of the invention, therefore, to develop catalyst systems with robust organic modifiers which have both organocatalytic functionalities and adsorption groups which enable strong unspecific adsorption on the catalyst surface. These inventive catalyst systems can activate comparatively unreactive substrates under relatively severe reaction conditions (elevated temperature, elevated pressure) and convert them chemo-, stereo-, diastereo- and/or enantio- selectively.

The invention provides catalyst systems consisting of supported or unsupported transition metal catalysts

whose surface has been modified with defined amounts of organic modifiers, which are characterized in that the modifier has a sulphur-containing functionality (Go) .

Even though, according to the prior art, sulphur- containing molecules are known predominantly for the poisoning of catalysts, it has been found in the case of the inventive catalysts which are treated with sulphur compounds that, surprisingly, an increase both in activity and selectivity can occur compared to unmodified catalysts.

The inventive catalyst system may consist of an unsupported catalyst or a supported catalyst and an organic modifier and be characterized in that the modifier has, as a sulphur-containing functionality

(G ₀ ) thiol, (poly) sulphane, thiophene or thiopyran groups .

The inventive catalyst system may be characterized in that the modifier has at least one further functional group (Gi) with Brønsted-basic, Brønsted-acidic, Lewis- basic or Lewis-acidic properties.

The inventive catalyst system may be characterized in that the modifier has a spacer (Sp) between the sulphur-containing functionality (Go) and the Brønsted- basic, Brønsted-acidic or Lewis-basic functionality (G ₁ ) .

The inventive catalyst system may be characterized in that the unsupported catalyst or the supported catalyst comprises one or more catalytically active components, where these components may be compounds of the elements of transition group I, II, VII and VIII of the Periodic Table and preferably compounds of the elements Pt, Pd, Rh, Ru, Re, Ir, Au, Ag, Ni, Co, Cu and Fe.

The inventive catalyst system may be characterized in that the modifier is adsorbed on the catalyst surface during or immediately after the preparation of the metal or supported metal catalyst and is introduced into the catalytic process stage as such a catalyst system.

The inventive catalyst system may be characterized in that the modifier is adsorbed on the catalyst surface immediately before the introduction into the catalytic process stage.

The inventive catalyst system may be characterized in that the modifier and the heterogeneous catalyst are introduced into the catalytic process stage, and the modifier is adsorbed on the catalyst surface in situ.

The inventive catalyst system may be characterized in that the modifier, as a sulphur-containing functionality (Go) has alkylthiol or alkylsulphane or alkyldisulphane or alkyltrisulphane or alkyl- polysulphane groups, or arylthiol or arylsulphane or aryldisulphane or aryltrisulphane or arylpolysulphane groups, or alkylarylthiol or alkylarylsulphane or alkylaryldisulphane or alkylalkyltrisulphane or alkylarylpolysulphane groups.

The inventive catalyst system may be characterized in that the modifier preferably has, as a sulphur- containing functionality (Go) , phenylthiol or phenylsulphane groups or benzylthiol or benzylsulphane groups .

The inventive catalyst system may be characterized in that the mass ratio of modifier : catalyst is in the range between 10 000:1 and 1:10 000 and preferably between 10:1 and 1:1000.

The inventive catalyst system may be characterized in that the modifier has, as a functional group (Gi) one or more groups from the group of amino and/or carboxylic acid and/or carboxylic ester and/or carboxamide and/or aminocarboxylic acid and/or aminocarboxylic ester and/or aminocarboxamide and/or hydroxycarboxylic acid and/or hydroxycarboxylic ester and/or hydroxycarboxamide and/or aminoalcohol and/or diol and/or urea and/or thiourea .

Preferred modifiers with a sulphur-containing functionality (G ₀ ) according to the invention may be organic molecules which contain thiol, (poly) sulphane, thiophene or thiopyran groups and additionally also have at least one further functional group (Gi) with

Brønsted-basic, Brønsted-acidic, or Lewis-basic properties, for example amino, amino acid, hydroxycarboxylic acid, aminoalcohol, diol, biphenol, urea or thiourea groups.

The modifiers of the inventive catalysts may have a spacer (Sp) which is disposed between functionality Go and Gi. The spacer may have, for example, the structures detailed in Table 1.

Examples of such modifiers are compiled in Fig. 4 and Table 1.

Table 1

Examples of the functional groups Sp, Go and Gi of the inventive modifiers

The S-containing functionalities Go of the modifiers of the inventive catalyst system documented in Fig. 4 can serve for the strong adsorption of the modifier on the metal surface, which is maintained even in the case of elevated reaction temperature and high concentrations of reactive substrates.

The modifiers of the inventive catalysts may have at

least one chiral centre.

The inventive catalyst system may be characterized in that the catalyst system can catalyse reactions of the following reaction classes: chemo-, stereo-, diastereo- and/or enantioselective hydrogenations of substrates which contain one or more carbonyl groups and/or one or more C=C double bonds and/or one or more aromatic and/or heteroaromatic groups and/or one or more nitro groups and/or one or more nitrile groups and/or one or more imine groups and/or one or more hydroxylamine groups and/or one or more alkyne groups, the chemo-, stereo-, diastereo-, or enantioselective reductive alkylation of primary or secondary amines or the chemo-, stereo-, diastereo- or enantioselective reductive amination of aldehydes or ketones with ammonium salts or amines.

The temperature range of the catalytic use of the inventive catalysts may be -70 to 220 ⁰ C, preferably -10 to 200 ⁰ C and especially 20 to 140°C.

The pressure range (partial H ₂ pressure) of the catalytic use of the inventive catalysts may be 0.1 to 300 bar, preferably 0.5 to 100 bar.

The mass ratio of catalyst :modifier of the inventive catalyst may be between 1:1 and 10 000:1, preferably between 10:1 and 1000:1.

With the varying functionalities Zi and Z ₂ of the group Gi (see Table 1 and Fig. 4), it is possible to control the chemo-, stereo-, diastereo- and/or enantio-

selectivity of the catalytic reaction of different reaction and substrate classes.

The inventive catalyst system can be used to catalyse the following reaction classes: chemo-, stereo-, diastereo- and/or enantioselective hydrogenation of substrates which have at least one functional group or a plurality of functional groups from the group of: one or more carbonyl groups, one or more C=C double bonds, one or more aromatic and/or heteroaromatic groups, one or more nitro groups, one or more nitrile groups, one or more imine groups, one or more hydroxylamine groups, one or more alkyne groups.

The inventive catalyst system can also be used for the chemo-, stereo-, diastereo- or enantioselective reductive alkylation of primary or secondary amines.

The inventive catalyst system can also be used for the chemo-, stereo-, diastereo- or enantioselective reductive amination of aldehydes or ketones with ammonium salts or amines.

The active metal components of the inventive catalyst system may consist of one or more noble metals such as Pd, Pt, Ag, Au, Rh, Ru, Ir, and/or further transition metals such as Ni, Cu, Co, Mo.

The catalysts may comprise further elements, for example, alkali metals and alkaline earth metals, elements of main group 3, 4 and 5 and/or elements of transition group 1 to 8.

The metal components of the catalysts may be applied to

supports, in which case the supports used may be activated carbons, carbon black and oxidic materials such as AI2O3, SiO ₂ , TiO ₂ , ZrO ₂ , aluminosilicates, MgO, CaO, SrO, BaO, or mixed oxides composed of the oxides mentioned.

The novel inventive robust organic modifiers allow effective modification of different supported metal catalysts and are no longer restricted to narrowly specified support and metal particle properties.

The resulting inventive catalyst systems open up access to a multitude of chemo-, stereo-, diastereo- and enantioselective chemical reactions.

Examples

The examples concentrate on the use of inventive modified catalysts in reactions in which elevated reaction temperatures and partial hydrogen pressures are required for the substrate activation and for which the inventive catalyst systems have a significant improvement compared to the prior art.

Example 1

Heterogeneously catalysed enantioselective reductive amination in the presence of Pt catalysts which have been modified with amino acid sulphane/thiol derivatives

A library of 36 modifiers was generated. This library is based on the α-amino acid base structure shown in Fig. 5a. The substituents Go, Gi and, within the group Gi the functionalities Z ₁ and Z ₂ (see also Table 1) were varied systematically according to Fig. 5b.

The representatives of the substance library according

to Fig. 5 were used for the modification of different Pt catalysts. These catalysts each contained 5% by mass of Pt on an AI2O3 support (corresponds to Catasium F214 in Table Ia and b) or 3% by mass of Pt on an activated carbon support (corresponds to F1082QHA/W3% in Table Ia and b) . The modified Pt catalysts were used in the reductive amination of ethyl phenyl ketone to propylphenylamine .

The reaction was performed in a pressure reactor at a partial H ₂ pressure of 30 bar and a reaction temperature of 50 ⁰ C to 8O ⁰ C in methanol as a solvent. The catalysts were suspended in 3 ml of the solvent. Thereafter, 1 ml of the solution of the modifier in the solvent was added and the mixture was stirred at room temperature for 30 min. Thereafter, 1 ml of the substrate solution and 1 ml of the solution of the ammonium salt were added. The reactor was first purged with nitrogen and then charged with hydrogen up to the intended reaction pressure, and the reaction temperature was established. At the start of the reaction, the molar ethyl phenyl ketone :NH ₄ OH ratio was 1:3. The molar ratio of substrate to modifier was varied in the range of 1:1 to 10 000:1. Table 2a) and b) contain yields or propylphenylamine and ee values for selected experiments of these variations. It is found that, especially with the inventive catalyst/modifier systems No. 8, 11, 12, 14, 15, 16, 17, 18, 29, 30, 32, 35, 36 (Table 2a, b) , enantio- selectivities are achieved which are both above the ee

values of a sulphur-free modifier analogue (N-acetylphenylalanine) , and above the ee values which are obtained without use of a modifier.

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Table 2a :

Number Mass of the of Reac ^¬ modi f ier cat ^¬ tion c (Subs n (subs. ) Ketone Amine

( see alyst/ Temp/ time/ trate) n (NH ₄ OH) / / conver- yield/

Fig . 6b) Modif ier Catalyst mg ⁰ C p/bar run /g/1 n (subs . ) n (mod . ) sion/% % 7 S -benzyl-L-cysteine*HCl Catasium F218 30 56 30 1028 D 1 3 0 100 28 28 7 S -benzyl-L-cysteine*HCl F 1082 QHA/W 3% 30 57 30 1028 0.1 3.0 100 27 27 8 N-Ac-S -benzyl-L- cysteine F 1082 QHA/W 3% 30 58 30 1028 0.1 2.9 5 33 33

8 N-Ac-S -benzyl-L- cysteine F 1082 QHA/W 3% 30 57 30 1070 0.1 2.8 11 30 27

8 N-Ac-S -benzyl-L- cysteine F 1082 QHA/W 3% 30 57 30 1028 0.1 3.0 52 28 26

8 N-Ac-S -benzyl-L- cysteine F 1082 QHA/W 3% 30 57 30 1028 0.1 3.0 54 31 29

8 N-Ac-S -benzyl-L- cysteine F 1082 QHA/W 3% 30 56 30 1028 0.1 3.0 106 30 23

8 N-Ac-S -benzyl-L- cysteine F 1082 QHA/W 3% 30 55 30 1028 0.1 2.9 107 29 23

8 N-Ac-S-benzyl-L-cysteine F 1082 QHή/W 3% 30 55 30 1028 0 1 2 9 500 34 30

9 N-propionyl-S-benzyl-L- Catasium F214 30 55 30 1020 0.1 3.0 100 22 17 cysteme

9 N-propionyl-S-benzyl-L- F 1082 QHA/W 3% 30 55 30 1020 0.1 3.0 100 22 18 cysteme

10 N-trimethylacetyl-S- Catasium F214 30 54 30 1020 0.1 3.0 100 10 10 benzyl-L-cysteine

10 N-tπmethylacetyl-S- F 1082 QHA/W 3% 30 55 30 1020 0.1 3.0 100 12 12 benzyl - L- cysteine

11 N-benzyl-S-benzyl-L- Catasium F214 30 55 30 1020 0.1 3.0 100 21 20 cysteine

11 N-benzyl-S-benzyl-L- F 1082 QHA/W 3% 30 54 30 1020 0.1 3.0 100 23 23 cysteme

12 N-phenylacetyl-S -benzyl- Catasium F214 30 55 30 1020 0.1 3.0 100 17 17 L-cysteme

12 N-phenylacetyl-S -benzyl- F 1082 QHA/W 3% 30 55 30 1020 0.1 3.0 100 21 20

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L-cysteme

13 S -phenyl-L-cysteine*HCl Catasium F214 30 55 30 1070 0.1 3.0 100 19 28

13 S -phenyl-L-cysteine*HCl F 1082 QHA/W 3% 30 55 30 1070 D.I 3.0 100 21 27

14 N-Ac-ξ -phenyl-L- cysteine Catasium F214 30 55 30 1070 0.1 3.0 100 32 31

14 N-Ac-S -phenyl-L- cysteine F 1082 QHA/W 3% 30 55 30 1070 D.I 3.0 100 31 30

15 N-propionyl-S-phenyl-L- Catasium F214 30 55 30 1070 0.1 3.0 100 28 19 cysteine

15 N-propionyl-ξ-phenyl-L- F 1082 QHA/W 3% 30 55 30 1070 D 1 3 0 100 29 21 cysteine

1 6 N-tπmethylacetyl-S- Catasium F214 30 55 30 1070 0.1 3.0 100 23 18 phenyl -L-cysteine ethyl

1 6 N-tπmethylacetyl-S- F 1082 QHA/W 3% 30 55 30 1070 D.I 3.0 100 27 20 phβnyl -L-cysteine ethyl

17 N-benzyl-S-phenyl-L- Catasium F214 30 55 30 1012 0.1 3.0 100 27 26 cysteine

17 M-benzyl-S-phenyl-L- F 1082 QHA/W 3% 30 55 30 1012 D 1 3 0 100 29 28 cysteme

18 N-phenylacetyl-S -phenyl- Catasium F214 30 55 30 1012 0.1 3.0 100 31 30 L-cysteme

18 N-phenylacetyl-S-phenyl- F 1082 QHA/W 3% 30 55 30 1012 D.I 3.0 100 30 28 L-cysteine

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Table 2b:

Number of Mass the of Reac ^¬ modifier cat ^¬ tion c (Subs n(subs.)/ Ketone Amine (see Fig. alyst/ Temp/ time/ trate) n (NH ₄ OH)/ n(mod.) conver- yield

6b) Modifier Catalyst mg ⁰ C p/bar mm /g/1 n (subs . )

19 L-cysteine ethyl Catasium F 214 10 55 3D 1046 D 1 3 6 9 8 ester*HCl 21 N-propionyl-L-cysteine F 1082 QHA/W 3% 30 57 30 1048 0.1 3.1 54 3 3 ethyl ester 21 N-propionyl-L-cysteme F 1082 QHA/W 3% 30 56 3D 1048 0.1 3.0 219 8 8 ethyl ester

24 N-phenylacetyl-L- F 1082 QHA/W 3% 30 56 31 1080 0.1 3.1 217 9 9 cysteine ethyl ester

25 S-benzyl-L-cysteine Catasium F214 30 57 31 990 D 1 2 8 109 22 22 ethyl ester*HCl

25 S-benzyl-L-cysteine F 1082 QHA/W 3% 30 54 34 990 0.1 2.8 109 22 22 ethyl ester*HCl

26 N-Ac-ξ-benzyl-L-cysteine Catasium F214 30 55 31 990 0.1 2.8 219 20 20 ethyl ester

26 N-Ac-S-benzyl-L-cysteine F 1082 QHA/W 3? 30 53 31 990 0.1 2.8 219 23 23 ethyl ester

27 N-propionyl-S-benzyl-L- Catasium F214 30 56 31 990 0 1 2 8 100 20 20 cysteine ethyl ester

27 N-propionyl-S-benzyl-L- F 1082 QHA/W 3? 30 56 30 990 0.1 2.8 100 20 20 cysteme ethyl ester

29 N-benzyl-S-benzyl-L- Catasium F214 30 57 31 1040 0.1 3.0 100 21 21 cysteme ethyl ester

29 N-benzyl-S-benzyl-L- F 1082 QHA/W 3? 30 56 31 1040 0.1 3.0 100 36 35 cysteine ethyl ester

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30 N-phenylacetyl-ξ-benzyl- Catasrum F214 30 55 32 1040 0.1 3.0 100 25 25

L-cysteine ethyl ester

30 N-phenylacetyl-S-benzyl- F 1082 QHA/W 3% 30 55 30 1040 0.1 3.0 100 36 36 L-cysteine ethyl ester

31 S-phenyl-L-cysterne Catasrum F214 30 55 30 1040 0.1 3.0 100 29 27 ethyl ester*HCl

31 S-phenyl-L-cysterne F 1082 QHA/W 3% 30 54 31 1040 0.1 3.0 100 33 31 ethyl ester*HCl

32 N-Ac-S-phenyl-benzyl-L- Catasrum F214 30 55 30 1040 0.1 3.0 100 17 16 cysteme ethyl ester

32 N-Ac-S-phenyl-L-cysterne F 1082 QHA/W 3% 30 54 30 1040 0.1 3.0 100 30 29 ethyl ester

33 N-propronyl-S-phenyl-L- Catasrum F214 30 56 30 1040 0.1 3.0 100 15 15 cysteme ethyl ester

33 N-propronyl-S-phenyl-L- F 1082 QHA/W 3% 30 55 30 1040 0.1 3.0 100 22 22 cysteine ethyl ester

34 N-trrmethylacetyl-S- Catasrum F214 30 55 30 1040 0.1 3.0 100 19 19 phenyl-L-cysterne ethyl ester

34 N-trrmethylacetyl-S- F 1082 QHA/W 3% 30 56 30 1040 ).l 3.0 100 24 24 phenyl-L-cysterne ethyl ester

35 N-benzyl-S-phenyl-L- Catasrum F214 30 55 30 1040 0.1 3.0 100 21 cysterne ethyl ester

35 N-benzyl-S-phenyl-L- F 1082 QHA/W 3% 30 55 30 1040 0.1 3.0 100 32 31 cysterne ethyl ester

36 N-phenylacetyl-S-phenyl- Catasrum F214 30 54 30 1040 0.1 3.0 100 22 21 L-cysterne ethyl ester

36 N-phenylacetyl-S-phenyl- F 1082 QHA/W 3% 30 56 30 1040 0.1 3.0 100 35 34

L-cysteine ethyl ester Reference N-acetylphenylalanine Catasrum F214 30 55 30 1000 0.1 3.0 100 30 16

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Reference N-acetylphenylalanme F 1082 QHA/W 3% 30 55 30 1000 1 3.0 100 28 16

Reference No modifier Catasium F214 11 55 31 980 1 2.8 0 17 17

Reference No modifier F 1082 QHA/W 3% 29 56 31 1080 1 3.0 0 33 30

K*

O

Example 2

Representative No. 8 of the substance library according to Fig. 5 was used for the modification of a Pt catalyst (5% by mass of Pt supported on AI2O3) . The catalyst was obtained by suspending 3 g of aluminium oxide at room temperature in 40 ml of 2.5% sodium carbonate solution (Na ₂ COa) with a magnetic stirrer at 50°C for 15 min. 400 mg of hexachloroplatinic acid hexahydrate (H ₂ PtCl6*6H ₂ O corresponding to 150 mg of Pt) , dissolved in 30 ml of water, were added dropwise to the support suspension within approx. 30 min.

After the addition had ended, the mixture was stirred for another 15 min and then the pH was adjusted to 10.5. The reduction was effected by adding 0.3 g of sodium borohydride (NaBH ₄ ) in 30 ml of water at 50 ⁰ C. After the reduction had set in (recognizable by immediate blackening of the catalyst), the mixture was stirred for another about 45 min, before the catalyst was removed with a frit, washed with water and dried overnight at approx. 70 ⁰ C in a drying cabinet.

Immediately after the preparation, the catalyst was suspended in 40 ml of a methanol solution which contained 0.4 mmol/1 of modifier No. 8 (cf . Fig. 5) . Thereafter, the solid was filtered off again, optionally washed with water and dried at room temperature in a vacuum cabinet.

The modified Pt catalysts were used in the reductive amination of ethyl phenyl ketone to propylphenylamine .

The reaction was performed in a pressure reactor at a partial H ₂ pressure of 30 bar and a reaction temperature of 50 ⁰ C in methanol as a solvent. The catalyst was suspended in 4 ml of the solvent. Thereafter 1 ml of

the substrate solution and 1 ml of the solution of the ammonium salt were added. The reactor was first purged with nitrogen and then charged with hydrogen up to the intended reaction pressure, and the reaction temperature was established. At the start of the reaction, the molar ethyl phenyl ketone :NH ₄ OH ratio was 1:3.

Table 3 shows yields of propylphenylamine and ee values which are significantly above the values of the unmodified catalyst (cf. Example 1, Table 2b).

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Table 3:

Number of the Reac ^¬ c (Sub ^¬ Ketone modifier Mass of tion strate n (NH ₄ OH) n (subs . ) conver ^¬ Amine Amine

(see catalyst/ Temp/ time/ ) / / sion yield select-

Fig. 6b) Modifier Catalyst mg ⁰ C p/ba mm / n (subs . ) n (mod. ) /% /% ivity/% ee r g/i

8 N-Ac-S-benzyl- Pt/Al ₂ 0 ₃ 10.3 56 30.2 1070 0.1 2.8 11 21.0 21 100.0 20.8

L-cysteme

8 N-Ac-S-benzyl- Pt/Al ₂ O ₃ 10.0 55 30.3 1070 0.1 2.8 110 23.0 23 100.0 26.5 K*

L-cysteme

Example 3

Representative No. 8 in the substance library according to Fig. 5 was used for the modification of a Pt catalyst (3% by mass of Pt supported on activated carbon, referred to as F1082QHA/W3%) .

The Pt catalyst was used in the reductive amination of ethyl phenyl ketone to propylphenylamine and modified in situ with N-Ac-S-benzyl-L-cysteine .

The reaction was performed in a pressure reactor at a partial H ₂ pressure of 30 bar and a reaction temperature of 50 ⁰ C to 80 ⁰ C in methanol as a solvent. The catalyst was suspended in 3 ml of the solvent. The reactor was first purged with nitrogen and then charged with hydrogen up to the intended reaction pressure, and the reaction temperature was established. Thereafter, 3 ml of a methanol solution which comprised the modifier NH ₄ OH and the substrate were added to the catalyst suspension under reaction conditions with stirring. The molar ethyl phenyl ketone :NH ₄ OH ratio was 1:3. The molar substrate :modifier ratio in the reactor was 1:11.

Table 4 shows yields of propylphenylamine and ee values which are significantly above the values of the unmodified catalyst (cf. Example 1, Table 2b).

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Table 4:

Number of the Reacc (SubsKetone modifier Mass tion trate) n (NH ₄ OH n (subs. ) converAmine Mini

(see of Temp time/ / ) / sion yield selec

Fig. 6b) Modifier Catalyst cata/ p/bar mm g/i / n (mod. ) /% /% lvity lyst/ ⁰ C n (subs . mg )

8 N-Ac-S-benzyl- F 1082 QHA/W 3% 9.9 55 30.1 1070 0.1 2.8 11 44.2 22.9 51.9

L-cysteine

8 N-Ac-S-benzyl- F 1082 QHA/W 3% 9.8 57 30 1070 0.1 2.8 11 44.2 26.7 60.4

L-cysteme

Example 4

Heterogeneously catalysed enantioselective hydrogenations of α-keto carboxylic acid derivatives

For the enantioselective hydrogenation of ethyl pyruvate, a Pt/Al ₂ C>3 catalyst (5% by mass of Pt) was modified with the following compounds: N-acetylphenylalanine N-Ac-S-phenyl-L-cysteine

The catalysts were suspended in 3 ml of the solvent. Thereafter, 1 ml of the solution of the modifier in the solvent was added and the mixture stirred at room temperature for 30 min. The chemical conversion was effected at 50 ⁰ C and a partial H ₂ pressure of 5 bar in acetic acid as a solvent. One reaction batch contained in each case 10 mg of the dry catalyst and 6 ml of the reaction solution with a substrate concentration of 750 mmol/1 and a modifier concentration of 0.2 mmol/1.

The yields and ee values are summarized in Table 5.

Table 5

Results of the conversion of ethyl pyruvate (40 ⁰ C, 5 bar, substrate concentration 750 mmol/1; modifier concentration 0.2 mmol/1) .

The inventive catalyst/modifier system exhibits the highest enantiomeric enrichment compared to the modifier-free system and to the system comprising the sulphur-free modifier under the selected reaction conditions .

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