Process and device for burn-off of precious metal-containing materials

Patent metadata

Field	Value
Publication number	US-10724116-B2
Application number	US-201615742152-A
Country	US
Kind code	B2
Filing date	Jun 7, 2016
Priority date	Jul 15, 2015
Publication date	Jul 28, 2020
Grant date	Jul 28, 2020

Abstract

Process for removing inorganically— and/or organically-bound carbon from a precious metal-containing composition inside an oven chamber comprising at least one direct burner and at least one exhaust gas conduit, characterised by the sequence of steps of: a) providing a precious metal-containing composition comprising fractions of inorganically— and/or organically-bound carbon inside the oven chamber; b) closing the oven chamber; c) heating the content of the oven chamber by means of at least one direct burner in order to establish a temperature T1 in the range of 450° C. to 1,000° C. and maintaining temperature T1 for 5 min-48 h; whereby, once the oven chamber is closed, any gas exchange between the oven chamber and the surroundings can take place only via the at least one direct burner and the at least one exhaust gas conduit.

First claim

What is claimed is:

1. A process for removing inorganically- and/or organically-bound carbon from a precious metal-containing composition inside an oven chamber comprising at least one direct burner and at least one exhaust gas conduit, characterised by the sequence of steps of:
a) providing a precious metal-containing composition comprising fractions of inorganically- and/or organically-bound carbon inside the oven chamber;
b) closing the oven chamber;
c) heating the content of the oven chamber by means of at least one direct burner in order to establish a temperature T1 in the range of 450° C. to 1,000° C. and maintaining the temperature T1 for 5 min to 48 h; and
d) supplying an inert gas/oxygen mixture with an oxygen content of 15-35% by volume into the oven chamber for establishing a temperature T2 in the range of 500° C. to 1,100° C., and maintaining the temperature T2 for 5 min to 48 h;
whereby, once the oven chamber is closed, any gas exchange between the oven chamber and the surroundings can take place only via the at least one direct burner and the at least one exhaust gas conduit.

2. The process of claim 1 , characterised in that the temperature T1 is constant.

3. The process of claim 1 , characterised in that the temperature T1 in step c) is in the range of 600° C. to 850° C.

4. The process of claim 1 , characterised in that the precious metal-containing composition comprises at least one precious metal from the group consisting of Pd, Pt, Ir, Ru, Rh, Ag, and Au.

5. The process of claim 1 , characterised in that the precious metal-containing composition is present as a liquid, as a solid or as a mixture of a liquid and a solid.

6. The process of claim 1 , characterised in that the precious metal-containing composition comprises at least one type from the group consisting of powders, ashes, sludges, tars, solutions, dispersions, suspensions, fibrous materials, films/foils, membranes, and granulate materials.

7. The process of claim 1 , characterised in that the inert gas is nitrogen.

8. The process of claim 1 , characterised in that the pressure in the oven chamber after step b) is in the range of 0.1 to 250 mbar lower than the ambient pressure predominating outside the oven chamber.

9. The process of claim 1 , characterised in that the precious metal-containing composition comprises a precious metal content ranging from 0.1 to 90% by weight.

10. The process of claim 1 , wherein steps a)-c) have a self-inerting effect.

Assignees

• Heraeus Deutschland Gmbh & Co Kg

Inventors

• Meyer Horst
• Voss Steffen
• Romero Jose Manuel

Classifications

• C22B11/021 Primary

  Recovery of noble metals from waste materials · CPC title

• Y02P10/20

  Recycling · CPC title

• C22B11/044

  from pyrometallurgical residues, e.g. from ashes, dross, flue dust, mud, skim, slag, sludge · CPC title

• C22B11/026 Primary

  from spent catalysts · CPC title

• C10B53/07

  {of solid raw materials consisting} of synthetic polymeric materials, e.g. tyres (recovery or working-up of waste materials of organic macromolecular compounds or compositions based thereon by dry-heat treatment for obtaining partially depolymerised materials C08J11/10; production of liquid hydrocarbon mixtures from rubber or rubber waste C10G1/10) · CPC title