Method for recovering noble metal from heterogeneous catalysts containing noble metal

Patent metadata

Field	Value
Publication number	US-2023407503-A1
Application number	US-202118248987-A
Country	US
Kind code	A1
Filing date	Aug 31, 2021
Priority date	Oct 16, 2020
Publication date	Dec 21, 2023
Grant date	—

Abstract

A method for recovering noble metal from a heterogeneous catalyst comprising a solid carrier material and palladium, platinum or rhodium, present at least partially in elemental form, said method comprising the steps of converting the noble metal to an oxidation state>0 by treating the heterogeneous catalyst with an oxidizing agent in the presence of hydrochloric acid so as to form a two-phase system A comprising a hydrochloric aqueous phase A1 and a solid phase comprising the carrier material which is insoluble therein, optionally, at least partially separating the hydrochloric aqueous phase A1 from the two-phase system A and adding a further aqueous phase to the remaining residue of the two-phase system A so as to form a two-phase system B comprising a hydrochloric aqueous phase and a solid phase comprising the carrier material insoluble therein.

First claim

1 . A method for recovering noble metal of and/or from a heterogeneous catalyst comprising a solid carrier material and at least one noble metal which is selected from the group consisting of palladium (Pd), platinum (Pt), and rhodium (Rh), and is present at least partially in elemental form, comprising the successive steps of:
(a) converting the at least one noble metal present at least partially in elemental form into an oxidation state>0 by treating the heterogeneous catalyst with oxidizing agent in the presence of hydrochloric acid to form a two-phase system A comprising a hydrochloric aqueous phase A1 and a solid phase comprising the carrier material that is insoluble therein, (b) optionally at least partially separating the hydrochloric aqueous phase A1 from the two-phase system A, and adding a further aqueous phase to the remaining residue of the two-phase system A to form a two-phase system B comprising a hydrochloric aqueous phase B1 and a solid phase comprising the carrier material that is insoluble therein, (b′) if step (b) has taken place, optionally, once or multiple times, repeatedly at least partially separating the hydrochloric aqueous phase from the two-phase system formed in the preceding step, and adding a further aqueous phase to form a further two-phase system comprising a hydrochloric aqueous phase and a solid phase comprising the carrier material that is insoluble therein, and (c) cathodic electro-deposition of the at least one noble metal either (c1) from the hydrochloric aqueous phase A1 of the two-phase system A or (c2) from the hydrochloric aqueous phase B1 of the two-phase system B or (c3) from the hydrochloric aqueous phase of the two-phase system formed finally in step (b′).

2 . The method according to claim 1 , wherein the further aqueous phase is a hydrochloric acid solution, hydrochloric acid, or water.

3 . The method according to claim 1 , comprising the successive steps (a) and (c) in variant (c1) without steps (b) and (b′).

4 . The method according to claim 1 , comprising the successive steps (a), (b), and (c) in variant (c2) without step (b′).

5 . The method according to claim 1 , comprising the successive steps (a), (b), (b′), and (c) in variant (c3).

6 . A method for recovering palladium of and/or from a heterogeneous catalyst comprising a solid carrier material and palladium present at least partially in elemental form, comprising the successive steps of:
(a) converting the palladium present at least partially in elemental form into an oxidation state>0 by treating the heterogeneous catalyst with oxidizing agent in the presence of hydrochloric acid to form a two-phase system A comprising a hydrochloric aqueous phase A1 and a solid phase comprising the carrier material that is insoluble therein, (b) optionally at least partially separating the hydrochloric aqueous phase A1 from the two-phase system A, and adding a further aqueous phase to the remaining residue of the two-phase system A to form a two-phase system B comprising a hydrochloric aqueous phase B1 and a solid phase comprising the carrier material that is insoluble therein, (b′) if step (b) has taken place, optionally, once or multiple times, repeatedly at least partially separating the hydrochloric aqueous phase from the two-phase system formed in the preceding step, and adding a further aqueous phase to form a further two-phase system comprising a hydrochloric aqueous phase and a solid phase comprising the carrier material that is insoluble therein, (c′) adjusting a basic pH of the hydrochloric aqueous phase A1 of the two-phase system A or of the hydrochloric aqueous phase B1 of the two-phase system B or of the hydrochloric aqueous phase of the two-phase system formed finally in step (b′), in the range of ≥8 to 14 using ammonium hydroxide, and (c) cathodic electro-deposition of the palladium from the hydrochloric aqueous phase of the two-phase system basically adjusted in step (c′).

7 . The method according to claim 1 , wherein the heterogeneous catalyst is a spent heterogeneous catalyst.

8 . The method according to claim 1 , wherein the heterogeneous catalyst has been subjected to one or more pretreatment steps before step (a).

9 . The method according to claim 1 , wherein the oxidizing agent is selected from chlorates, nitrates, bromates, iodates, chlorites, bromites, iodites, hypochlorites, perchlorates, peroxide compounds, chlorine, and/or ozone.

10 . The method according to claim 1 , wherein the noble metal recovery takes place in the sense of an almost complete removal from the carrier material.

11 . The method according to claim 1 , wherein the cathodic electro-deposition is carried out with spatial separation of the partial reactions.

12 . The method according to claim 1 , wherein the cathodic electro-deposition takes place until a noble metal concentration of <50 wt.ppm in the hydrochloric aqueous phase is reached.

Assignees

• Heraeus Deutschland Gmbh & Co Kg

Inventors

• Maier Dirk
• Gebauer Christian

Classifications

• C25C1/20 Primary

  of noble metals · CPC title

• C22B11/048

  from spent catalysts · CPC title

• C22B3/10

  Hydrochloric acid {, other halogenated acids or salts thereof} · CPC title

• C22B1/005

  Preliminary treatment of scrap (C22B1/02 - C22B1/26 take precedence) · CPC title

• C22B3/22

  by physical processes, e.g. by filtration, by magnetic means {, or by thermal decomposition} (treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title