Process for producing a supported silver catalyst
AssigneeBASF SE
InventorsTOBIAS ROSENDAHL, Torsten Mäurer, Cornelia K. Dobner, Andreas Lehr, Johanna Wanka
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Abstract
Process for producing a supported silver catalyst, which comprises (a) reacting oxalic acid with an alkali metal base in a solvent, preferably water, to the second equivalence point of oxalic acid to give alkali metal oxalate; (b) reacting the alkali metal oxalate obtained according to (a) with silver salt in a solvent, preferably water, to give silver oxalate; (c) forming a complexation of the silver oxalate obtained according to (b) with a diamine compound in a solvent, preferably water, to give a diamine-silver oxalate complex.
Claims12
1-18. (canceled)
19:
- A supported silver catalyst obtained or obtainable by a process which comprises
- (a) reacting oxalic acid with an alkali metal base in a solvent to the second equivalence point of oxalic acid to give alkali metal oxalate;
- (b) reacting the alkali metal oxalate obtained according to (a) with a silver salt in a solvent to give silver oxalate;
- (c) forming a complex of the silver oxalate obtained according to (b) with a diamine compound in a solvent to give a diamine-silver oxalate complex,
- (d) adding at least one promoter to the solution obtained according to (c) (e) providing a porous support material,
- (f) impregnating the porous support material with the solution obtained according to (c) or (d),
- (g) calcining the impregnated support material obtained according to (f).
The supported silver catalyst according to claim 19 having a silver content in the range from 5 to 30% by weight, a lithium content in the range from 25 to 400 ppm by weight, a cesium content in the range from 25 to 750 ppm by weight, a tungsten content in the range from 5 to 500 ppm by weight, a rhenium content in the range from 25 to 600 ppm by weight and a sulfur content in the range from 0 to 50 ppm by weight applied to the porous support material by impregnation, in each case calculated as element and based on the total weight of the catalyst, wherein the porous support material has a cylindrical geometry.
The supported silver catalyst according to claim 19 having a silver content in the range from 5 to 30% by weight, a lithium content in the range from 25 to 400 ppm by weight, a cesium content in the range from 25 to 750 ppm by weight, a tungsten content in the range from 5 to 500 ppm by weight, a rhenium content in the range from 25 to 600 ppm by weight and a sulfur content in the range from 0 to 50 ppm by weight applied to the porous support material by impregnation, in each case calculated as element and based on the total weight of the catalyst, wherein the porous support material has a cylindrical geometry, wherein a cylinder has a length in the range from 5 to 10 mm, an external diameter in the range from 5 to 10 mm and a ratio of external diameter/mm to wall thickness/mm in the range from 2.5 to 4.5.
The supported silver catalyst according to claim 19, wherein the solvent used in the process for producing the supported silver catalyst is water.
The supported silver catalyst according to claim 19, wherein the porous support material used in the process for producing the supported silver catalyst comprises at least 98% by weight of alpha-aluminum oxide.
The supported silver catalyst according to claim 19, wherein the calcining step in the process for producing the supported silver catalyst is carried out at a temperature in the range from 270 to 295° C.
A precursor of a supported silver catalyst obtained or obtainable by a process for producing a supported silver catalyst, which comprises
- (a) reacting oxalic acid with an alkali metal base in a solvent to the second equivalence point of oxalic acid to give alkali metal oxalate;
- (b) reacting the alkali metal oxalate obtained according to (a) with a silver salt in a solvent to give silver oxalate;
- (c) forming a complex of the silver oxalate obtained according to (b) with a diamine compound in a solvent to give a diamine-silver oxalate complex,
- (d) adding at least one promoter to the solution obtained according to (c),
- (e) providing a porous support material;
- (f) impregnating the porous support material with the solution obtained according to (c) or (d).
A process for preparing ethylene oxide by direct oxidation of ethene by means of oxygen wherein the supported silver catalyst according to claim 19 is used as catalyst.
The supported silver catalyst according to claim 19, wherein the porous support material comprises alpha-aluminum oxide.
Dependencies are inferred from the claim text.