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A method for producing a shaped Cu—Zn catalyst for hydrogenating organic compounds containing a carbonyl function. The shaped catalyst is suitable for hydrogenating aldehydes, ketones and also carboxylic acids and/or their esters, fatty acids and/or their esters, such as fatty acid methyl esters, to

A method for producing a shaped Cu—Zn catalyst for hydrogenating organic compounds containing a carbonyl function. The shaped catalyst is suitable for hydrogenating aldehydes, ketones and also carboxylic acids and/or their esters, fatty acids and/or their esters, such as fatty acid methyl esters, to the corresponding alcohols, dicarboxylic anhydrides, such as maleic anhydride (MAn), or esters of diacids to dialcohols, such as butanediol. The present invention further relates to Cu—Zn catalysts obtainable by the production method.

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1. A process for producing a shaped tableted catalyst body, comprising the steps of: (a) carrying out a thermal treatment of a metal carbonate mixture by heating to a temperature in the range from 200° C. to 300° C. for a time of from 1 hour to 6 hours to give a thermally treated metal carbonate mix

1. A process for producing a shaped tableted catalyst body, comprising the steps of: (a) carrying out a thermal treatment of a metal carbonate mixture by heating to a temperature in the range from 200° C. to 300° C. for a time of from 1 hour to 6 hours to give a thermally treated metal carbonate mixture having a carbonate content in the range from 2.7 to 14.0% by weight, and(b) tableting the thermally treated metal carbonate mixture obtained in step (a),wherein: the metal carbonate mixture is obtained by(i) combining a solution A and a solution B by simultaneous introduction into a joint vessel to form a precipitate 1 at a pH value in the range from 6.0 to 7.5, separating off the precipitate and drying the isolated precipitate by heating to a temperature in the range from 75° C. to 130° C., or(ii) mixing a precipitate 2, a precipitate 3 and optionally one or more precipitates 4, with the precipitates being dried by heating to a temperature in the range from 75° C. to 130° C. before mixing, after mixing or both;and: precipitate 2 is a copper carbonate-containing precipitate obtained by combining a solution C with a solution D by simultaneous introduction into a joint vessel at a pH value in the range from 6.0 to 7.5,precipitate 3 is a zinc carbonate-containing precipitate obtained by combining a solution E with a solution F by simultaneous introduction into a joint vessel at a pH value in the range from 6.0 to 7.5,precipitate 4 is a precipitate containing at least one metal carbonate different from copper carbonate and zinc carbonate and is obtained by combining at least one solution G with at least one solution H by simultaneous introduction into a joint vessel at a pH value in the range from 6.0 to 7.5;and solution A is obtained by dissolving a copper compound, a zinc compound and optionally one or more further metal compounds in a solvent, optionally with the aid of an acid or base,solutions B, D, F and H are identical or different and are obtained by dissolving a carbonate compound in a solvent,solution C is obtained by dissolving a copper compound in a solvent, optionally with the aid of an acid or base,solution E is obtained by dissolving a zinc compound in a solvent, optionally with the aid of an acid or base, andsolution G is obtained by dissolving a metal compound which is not a copper or zinc compound in a solvent, optionally with the aid of an acid or base. 2. The process as claimed in claim 1, wherein the thermal treatment is carried out at a temperature in the range from 270° C. to 290° C. for a time of from 1.5 to 5 hours. 3. The process as claimed in claim 1, wherein the copper compound is selected from the group consisting of copper, copper oxide (Cu2O and/or CuO), copper nitrate, copper sulfate, copper carbonate, copper hydroxide carbonate, copper acetate, copper halides, Cu-ammine complexes and mixtures thereof. 4. The process as claimed in claim 1, wherein the zinc compound is selected from the group consisting of zinc nitrate, zinc sulfate, zinc chloride, zinc carbonate, zinc hydroxide, zinc sulfite, zinc acetate, zinc phosphate, zinc metal and ZnO and mixtures thereof. 5. The process as claimed in claim 1, wherein the metal compound, which is not a copper compound or zinc compound, is a compound selected from the group consisting of Al, Ti, Mn, Ni, Cr, Fe, Co, Mo, Ce and Zr and mixtures thereof. 6. The process as claimed in claim 1, wherein the carbonate compound is selected from the group consisting of alkali metal, alkaline earth metal and ammonium carbonates, alkali metal, alkaline earth metal and ammonium hydrogen carbonates and mixtures thereof. 7. The process as claimed in claim 1, wherein the thermally treated metal carbonate mixture contains 5% by weight or less, based on the total weight of the thermally treated metal carbonate mixture. 8. The process as claimed in claim 1, wherein a lubricant is added in an amount of from 0.1 to 5% by weight, based on the total weight of the composition to be tableted, to the thermally treated powder obtained from step (a) before tableting. 9. The process as claimed in claim 8, wherein the lubricant is added in an amount of from 0.5 to 5% by weight, based on the total weight of the composition to be tableted. 10. The process as claimed in claim 8, wherein the lubricant is graphite. 11. The process as claimed in claim 1, further comprising the step of: (c) reducing the shaped tableted catalyst body obtained from step (b) to give a reduced shaped catalyst body. 12. The process as claimed in claim 11, wherein reduction is effected by hydrogen. 13. The process as claimed in claim 11, wherein reduction is carried out at a temperature in the range from 150° C. to 400° C. 14. The process as claimed in claim 11, wherein reduction is carried out over a time of from 1 hour to 10 days. 15. The process as claimed in claim 11, wherein (a) the reduced shaped catalyst body is covered with a liquid with exclusion of air after reduction, or(b) a mixture of an oxygen-containing gas and an inert gas is supplied to the reduced shaped catalyst body with the concentration of oxygen in the mixture during introduction being from 0.001% by volume to 50% by volume. 16. A shaped tableted catalyst body obtained by a process as claimed in claim 1. 17. The shaped tableted catalyst body as claimed in claim 16, having a carbonate content in the range from 2.7 to 14.0% by weight. 18. A reduced shaped tableted catalyst body obtained by a process as claimed in claim 11, wherein the shaped tableted catalyst body obtained from step (b) has, before reduction, a carbonate content in the range from 2.7 to 14.0% by weight. 19. The reduced shaped tableted catalyst body as claimed in claim 18, whose Cu metal surface area is 19 m2/g or more, based on the total mass of the catalyst. 20. The shaped tableted catalyst body as claimed in claim 18, containing Cu(0) in a proportion in the range from 5 to 70% by weight, based on the shaped tableted catalyst body. 21. A method for hydrogenating an organic compound comprising the step of exposing the organic compound to a shaped tableted catalyst body as claimed in claim 16, during manufacture of the organic compound. 22. The method as claimed in claim 21 where the organic compound has at least one carbonyl group. 23. The method as claimed in claim 21, wherein the organic compound is selected from the group consisting of aldehydes, ketones and monocarboxylic, dicarboxylic and polycarboxylic acids and/or esters thereof. 24. A method for catalyzing a reaction comprising the step of exposing the reaction to a shaped tableted catalyst body as claimed in claim 16, wherein the reaction is selected from the group consisting of synthesis gas reactions, methanol syntheses, Fischer-Tropsch syntheses, pyridine syntheses, ester hydrogenolyses, amination reactions, N-alkylations, hydrogenations of nitriles, hydrogenation of esters, hydrogenation of diesters to diols, hydrogenation of sugars to polyols, alkylation of a phenol by means of an alcohol, amination of an alcohol, dehydrogenation of a primary alcohol to the aldehyde, dehydrogenation of a secondary alcohol to a ketone, dehydrogenation of alkanes to alkenes, dehydrogenation of cycloalkanes to aromatics, dehydrogenation of diols, hydrogenation of an aldehyde, hydrogenation of an amide, hydrogenation of a fatty acid, selective hydrogenation of a fat, selective hydrogenation of an oil, hydrogenation of a nitroaromatic hydrocarbon, hydrogenation of a ketone, hydrogenation of furfural and hydrogenation of carbon monoxide or carbon dioxide to form methanol.