GB922021A - Recovery of palladium from catalysts - Google Patents
Recovery of palladium from catalystsInfo
- Publication number
- GB922021A GB922021A GB243259A GB243259A GB922021A GB 922021 A GB922021 A GB 922021A GB 243259 A GB243259 A GB 243259A GB 243259 A GB243259 A GB 243259A GB 922021 A GB922021 A GB 922021A
- Authority
- GB
- United Kingdom
- Prior art keywords
- palladium
- hydrochloric acid
- give
- solution
- recovered
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/04—Obtaining noble metals by wet processes
- C22B11/042—Recovery of noble metals from waste materials
- C22B11/048—Recovery of noble metals from waste materials from spent catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/90—Regeneration or reactivation
- B01J23/96—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the noble metals
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/06—Chloridising
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
Palladium is recovered from a deactivated catalyst by stripping the palladium from the support by slurrying with hydrochloric acid and passing chlorine gas in to form a palladium-containing solution, removing insoluble materials from the solution and precipitating palladium from the solution by the addition of a more electropositive metal, e.g. aluminium or magnesium. Prior to treatment the catalyst may be cleaned either by washing with an organic solvent, e.g. xylene followed by steam heating to remove the solvent or by heating in air, both steps being followed by washing with an alkaline reducing agent. The palladium recovered may be further purified by dissolving it in hydrochloric acid while passing chlorine gas in and filtering to removing insolubles. Ammonium hydroxide is then added to the filtrate and the mixture warmed to redissolve the palladium complex and give Pd(NH3)4 Cl2. Insolubles are again filtered off and the filtrate acidified with hydrochloric acid to give Pd(NH3)2 Cl2 as a precipitate. This precipitate is then either treated with hydrazine hydrate or heated in hydrogen to give pure palladium. The recovered or refined palladium may be dissolved in hydrochloric acid whilst passing gaseous chlorine through the mixture to give a solution of palladium chloride for the production of a catalyst by the methods described in Specifications 718,306, 746,385, 760,737 and 922,022. Specification 456,070 also is referred to.ALSO:Palladium is recovered from a deactivated catalyst by stripping the palladium from the support by slurrying with hydrochloric acid and passing chlorine gas in to form a palladium-containing solution, removing insoluble materials from the solution and precipitating palladium from the solution by the addition of a more electropositive metal, e.g. aluminium or magnesium. Prior to treatment the catalyst may be cleaned either by washing with an organic solvent, e.g. xylene, followed by steam heating to remove the solvent or by heating in air, both steps being followed by washing with an alkaline reducing agent. The palladium recovered may be further purified by dissolving it in hydrochloric acid while passing chlorine gas in and filtering to removing insolubles. Ammonium hydroxide is then added to the filtrate and the mixture warmed to redissolve the palladium complex and give Pd(NH3)4Cl2. Insolubles are again filtered off and the filtrate acidified with hydrochloric acid to give Pd(NH3)2Cl2 as a precipitate. This precipitate is then either treated with hydrazine hydrate or heated in hydrogen to give pure palladium. Specifications 456,070, 718,306, 746,385, 760,737 and 922,022 are referred to.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB243259A GB922021A (en) | 1959-01-22 | 1959-01-22 | Recovery of palladium from catalysts |
FR816288A FR1255965A (en) | 1959-01-22 | 1960-01-21 | Process for recovering palladium from catalysts |
ES0255303A ES255303A1 (en) | 1959-01-22 | 1960-01-26 | Recovery of palladium from catalysts |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB243259A GB922021A (en) | 1959-01-22 | 1959-01-22 | Recovery of palladium from catalysts |
Publications (1)
Publication Number | Publication Date |
---|---|
GB922021A true GB922021A (en) | 1963-03-27 |
Family
ID=9739483
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB243259A Expired GB922021A (en) | 1959-01-22 | 1959-01-22 | Recovery of palladium from catalysts |
Country Status (2)
Country | Link |
---|---|
ES (1) | ES255303A1 (en) |
GB (1) | GB922021A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0220811A1 (en) * | 1985-08-29 | 1987-05-06 | 296388 B.C. Ltd. | Process and apparatus for removing precious metals from solutions |
WO2001014058A1 (en) * | 1999-08-24 | 2001-03-01 | Degussa Ag | Method for regenerating platinum group metal suspension catalysts |
WO2009094732A1 (en) | 2008-01-30 | 2009-08-06 | G.E. Conseils Sprl | Process for the recovery of precious metals from used and/or defective catalytic carriers |
CN102994771A (en) * | 2011-09-13 | 2013-03-27 | 郴州市金贵银业股份有限公司 | Method for extracting palladium sponge from silver electrolysis anode slime parting liquid |
US20160115567A1 (en) * | 2014-10-22 | 2016-04-28 | Chevron U.S.A. Inc. | Metallurgical extraction technique to recover platinum group metals from a filter cake |
CN110964921A (en) * | 2018-09-28 | 2020-04-07 | 荆门市格林美新材料有限公司 | Production method of refined palladium |
CN110964917A (en) * | 2018-09-28 | 2020-04-07 | 荆门市格林美新材料有限公司 | Palladium refining process |
-
1959
- 1959-01-22 GB GB243259A patent/GB922021A/en not_active Expired
-
1960
- 1960-01-26 ES ES0255303A patent/ES255303A1/en not_active Expired
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0220811A1 (en) * | 1985-08-29 | 1987-05-06 | 296388 B.C. Ltd. | Process and apparatus for removing precious metals from solutions |
WO2001014058A1 (en) * | 1999-08-24 | 2001-03-01 | Degussa Ag | Method for regenerating platinum group metal suspension catalysts |
US7309675B1 (en) | 1999-08-24 | 2007-12-18 | Degussa Ag | Method for regenerating platinum catalysts |
WO2009094732A1 (en) | 2008-01-30 | 2009-08-06 | G.E. Conseils Sprl | Process for the recovery of precious metals from used and/or defective catalytic carriers |
BE1017974A3 (en) * | 2008-01-30 | 2010-02-02 | Variabel Daniel | METHOD FOR THE VALORISATION OF USUAL AND / OR DEFECTIVE CATALYTIC SUPPORT ELEMENTS |
AU2009208314B2 (en) * | 2008-01-30 | 2011-02-24 | G.E. Conseils Sprl | Process for the recovery of precious metals from used and/or defective catalytic carriers |
AU2009208314B9 (en) * | 2008-01-30 | 2011-06-23 | G.E. Conseils Sprl | Process for the recovery of precious metals from used and/or defective catalytic carriers |
CN102994771A (en) * | 2011-09-13 | 2013-03-27 | 郴州市金贵银业股份有限公司 | Method for extracting palladium sponge from silver electrolysis anode slime parting liquid |
CN102994771B (en) * | 2011-09-13 | 2014-03-26 | 郴州市金贵银业股份有限公司 | Method for extracting palladium sponge from silver electrolysis anode slime parting liquid |
US20160115567A1 (en) * | 2014-10-22 | 2016-04-28 | Chevron U.S.A. Inc. | Metallurgical extraction technique to recover platinum group metals from a filter cake |
WO2016064444A1 (en) * | 2014-10-22 | 2016-04-28 | Chevron U.S.A. Inc. | A metallurgical extraction technique to recover platinum group metals from a filter cake |
US10017837B2 (en) | 2014-10-22 | 2018-07-10 | Chevron U.S.A. Inc. | Metallurgical extraction technique to recover platinum group metals from a filter cake |
CN110964921A (en) * | 2018-09-28 | 2020-04-07 | 荆门市格林美新材料有限公司 | Production method of refined palladium |
CN110964917A (en) * | 2018-09-28 | 2020-04-07 | 荆门市格林美新材料有限公司 | Palladium refining process |
Also Published As
Publication number | Publication date |
---|---|
ES255303A1 (en) | 1960-04-16 |
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