Process for removing precious metal from precious metal-containing catalyst form bodies

Patent metadata

Field	Value
Publication number	US-10378082-B2
Application number	US-201515523757-A
Country	US
Kind code	B2
Filing date	Oct 12, 2015
Priority date	Nov 10, 2014
Publication date	Aug 13, 2019
Grant date	Aug 13, 2019

Abstract

Process for removing precious metal from precious metal-containing catalyst form bodies comprising form bodies and precious metal, whereby the precious metal to be removed is at least one precious metal selected from the group consisting of Au, Ag, Pd, Pt, Ir, Rh, Ru, Os, and Re, comprising the steps of: (a) producing a mixture of precious metal-containing catalyst form bodies in at least one mineral acid that is at least 1N; (b) supplying inert or oxidizing gas into the mixture containing noble metal-containing catalyst form bodies and mineral acid; (c) introducing at least one oxidation agent, in solid or liquid form, into the mixture containing noble metal-containing catalyst form body and mineral acid; and (d) separating the form bodies from the liquid.

First claim

The invention claimed is:

1. A process for removing a precious metal from precious metal-containing catalyst form bodies comprising form bodies and a precious metal, whereby the precious metal to be removed is at least one precious metal selected from the group consisting of Au, Ag, Pd, Pt, Ir, Rh, Ru, Os, and Re, comprising the steps of:
(a) producing, in a reaction vessel, a mixture of the precious metal-containing catalyst form bodies in at least one mineral acid that is at least 1N;
(b) supplying an inert or oxidising gas into the mixture containing the precious metal-containing catalyst form bodies and the at least one mineral acid;
(c) introducing at least one oxidation agent, in solid or liquid form, into the mixture containing the precious metal-containing catalyst form bodies and the at least one mineral acid, the at least one oxidation agent being introduced into the mixture in a lower half of the reaction vessel; and
(d) separating the form bodies from the mixture,
wherein step (a) precedes steps (b) and (c).

2. The process according to claim 1 , further comprising an additional step (e), in which the at least one oxidation agent is a solid and the solid is washed.

3. The process according to claim 1 , wherein the mineral acid is selected from the group consisting of hydrochloric acid, hydrobromic acid, hydriodic acid, nitric acid, sulfuric acid, and phosphoric acid.

4. The process according to claim 1 , wherein the at least one oxidation agent is selected from the group consisting of chlorates, nitrates, bromates, iodates, chlorites, bromites, iodites, hypochlorites, hypobromites, hypoiodites, perchlorates, bromine, iodine, peroxides, permanganates, and chromates.

5. The process according to claim 1 , wherein the precious metal-containing catalyst form body is fully covered by liquid in the mixture.

6. The process according to claim 1 , wherein the precious metal-containing catalyst form bodies contain precious metals in oxidation stage (0).

7. The process according to claim 1 , wherein 75-100% by weight of the form bodies consist of oxides of at least one element selected from the group consisting of Al, Ti, Mg, Zr, Sn, Fe, and Si that are inert with respect to acids.

8. The process according to claim 1 , wherein the precious metal-containing catalyst form bodies used in step (a) contain precious metal in an amount of 0.1% by weight to 50% by weight.

9. The process according to claim 1 , wherein the exposure time of the at least one oxidation agent in step (c) is 5-240 min.

10. The process according to claim 1 , wherein the process temperature during steps (b) and (c) is in the range of 15° C. to the boiling temperature.

11. The process according to claim 1 , wherein the process temperature during steps (b) and (c) is in the range of 30 to 90° C.

12. The process of claim 1 , wherein the form bodies are porous.

13. The process of claim 1 , wherein the form bodies are pure oxide ceramics or mixed oxide ceramics.

14. The process of claim 13 , wherein the pure oxide ceramics are selected from aluminum oxide, magnesium oxide, zirconium oxide, titanium oxide, and silicon dioxide.

15. The process of claim 13 , wherein the mixed oxide ceramics are selected from aluminum titanate, lead-zirconate titanate, barium titanate and Al 2 O 3 /ZrO 2 dispersion ceramics.

Assignees

• Heraeus Deutschland Gmbh & Co Kb
• Heraeus Deutschland Gmbh & Co Kg

Inventors

• Roehlich Christoph
• Thiel Vasco
• Fuchs-Alameda Stefanie
• Schapp Jan
• Voss Steffen

Classifications

• C22B11/06 Primary

  Chloridising · CPC title

• C22B11/048 Primary

  from spent catalysts · CPC title

• B01J38/68

  including substantial dissolution or chemical precipitation of a catalyst component in the ultimate reconstitution of the catalyst · CPC title

• B01J23/96

  of catalysts comprising metals, oxides or hydroxides of the noble metals · CPC title

• Y02P10/214

  Cross-Sectional Technologies · mapped topic