GB798712A - Improvements in or relating to recovery of platinum group metal from catalyst - Google Patents

Improvements in or relating to recovery of platinum group metal from catalyst

Info

Publication number
GB798712A
GB798712A GB2283356A GB2283356A GB798712A GB 798712 A GB798712 A GB 798712A GB 2283356 A GB2283356 A GB 2283356A GB 2283356 A GB2283356 A GB 2283356A GB 798712 A GB798712 A GB 798712A
Authority
GB
United Kingdom
Prior art keywords
catalyst
platinum
aluminium chloride
alumina
aluminium
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
Application number
GB2283356A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Universal Oil Products Co
Original Assignee
Universal Oil Products Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Universal Oil Products Co filed Critical Universal Oil Products Co
Publication of GB798712A publication Critical patent/GB798712A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00Obtaining noble metals
    • C22B11/02Obtaining noble metals by dry processes
    • C22B11/021Recovery of noble metals from waste materials
    • C22B11/026Recovery of noble metals from waste materials from spent catalysts
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Catalysts (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

Platinum group metal is recovered from a catalyst containing also aluminium oxide and carbonaceous deposits by calcining the catalyst in the presence of an oxygen-containing gas to burn off the carbonaceous deposits, then treating with aluminium chloride vapour in a stripping zone at 93-870 DEG C. and removing from the stripping zone vapours containing volatile platinum group metal compounds. The process is especially suitable for recovering platinum from a catalyst which has been used in a hydrocarbon conversion operation. In a preferred process, the spent catalyst is heated in air at 370-870 DEG C. for 1-12 hours or more and then subjected to magnetic separation to remove iron. Washing the catalyst follows, using water or an aqueous solution containing acetic acid, nitric acid, phosphoric acid, sulphuric acid, hydrochloric acid, sodium hydroxide, ammonium hydroxide, or a surface-active agent; acetone, chloroform, ether, carbon tetrachloride, and alcohol are alternative washing agents. The catalyst is dried at 93-870 DEG C. in air, chlorine, carbon monoxide, or carbon dioxide and then subjected to treatment with vaporous aluminium chloride. The vapour may be passed through the catalyst, or the catalyst may be mixed with aluminium chloride, or a solution thereof, and heated; another method is to treat the catalyst with phosphorus pentachloride vapours which react with the alumina to form aluminium chloride. The aluminium chloride vapour may be formed by heating aluminium chloride, by contacting alumina with carbon monoxide and chlorine or with carbon tetrachloride, or by contacting a mixture of alumina and carbon with chlorine; in use the aluminium chloride vapours may be diluted with helium, nitrogen, chlorine, carbon dioxide, or carbon monoxide; oxygen is excluded, for example by providing a bed of charcoal at the entrance to the stripping zone. The vaporous product from the stripping zone is contacted with water or an aqueous solution of aluminium chloride, which may contain hydrochloric acid. When platinum is being recovered, a solution of platinum chloride is formed which is treated with a reducing agent, e.g. aluminium metal, hydrazine hydrate, or stannous chloride, to form metallic platinum. In examples, platinum is recovered from an alumina-platinum catalyst and palladium from an alumina-palladium catalyst. Other platinum group metals referred to are iridium, rhodium, ruthenium, and osmium; the catalyst may also contain silica or combined halogen.
GB2283356A 1955-07-25 1956-07-24 Improvements in or relating to recovery of platinum group metal from catalyst Expired GB798712A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US798712XA 1955-07-25 1955-07-25

Publications (1)

Publication Number Publication Date
GB798712A true GB798712A (en) 1958-07-23

Family

ID=22153332

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2283356A Expired GB798712A (en) 1955-07-25 1956-07-24 Improvements in or relating to recovery of platinum group metal from catalyst

Country Status (1)

Country Link
GB (1) GB798712A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4913736A (en) * 1987-02-13 1990-04-03 The British Petroleum Company P.L.C. Process for recovering platinum group metals
FR2671104A1 (en) * 1990-12-28 1992-07-03 Inst Francais Du Petrole Process for antipollution treatment of a deactivated catalyst containing at least one noble metal and total recovery of the said metal and of the support alumina
WO1996017097A1 (en) * 1994-12-01 1996-06-06 Prior Engineering Ag Material beneficiation process and device
WO2004050926A1 (en) * 2002-12-02 2004-06-17 Council Of Scientific And Industrial Research A process for the recovery of adsorbed palladium from spent silica
WO2004106563A1 (en) * 2003-05-30 2004-12-09 Council Of Scientific And Industrial Research Process for recovery of palladium from spent catalyst
US7108839B2 (en) 2002-12-03 2006-09-19 Council Of Scientific And Industrial Research Process for the recovery of palladium from spent silica
CN100387344C (en) * 2006-06-21 2008-05-14 浙江工业大学 Method for recovering ruthenium catalyst carried by active carbon
US7473406B2 (en) 2003-05-30 2009-01-06 Council Of Scientific And Industrial Research Process for recovery of palladium from spent catalyst
CN102443707A (en) * 2011-11-30 2012-05-09 徐州浩通新材料科技股份有限公司 Method for recycling platinum from organic alcohol waste liquor
US9889429B2 (en) 2012-10-16 2018-02-13 Bill W. Helton Hydrogen production catalysts and associated systems and methods
US10457999B2 (en) * 2014-06-19 2019-10-29 Yeda Research And Development Co. Ltd. Method for platinum group metals recovery from spent catalysts
US11473168B2 (en) 2016-10-30 2022-10-18 Yeda Research And Development Co. Ltd. Method for platinum group metals recovery from spent catalysts

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4913736A (en) * 1987-02-13 1990-04-03 The British Petroleum Company P.L.C. Process for recovering platinum group metals
FR2671104A1 (en) * 1990-12-28 1992-07-03 Inst Francais Du Petrole Process for antipollution treatment of a deactivated catalyst containing at least one noble metal and total recovery of the said metal and of the support alumina
WO1996017097A1 (en) * 1994-12-01 1996-06-06 Prior Engineering Ag Material beneficiation process and device
US6626978B1 (en) 1994-12-01 2003-09-30 Prior Engineering Ag Method for dressing materials
WO2004050926A1 (en) * 2002-12-02 2004-06-17 Council Of Scientific And Industrial Research A process for the recovery of adsorbed palladium from spent silica
US7108839B2 (en) 2002-12-03 2006-09-19 Council Of Scientific And Industrial Research Process for the recovery of palladium from spent silica
WO2004106563A1 (en) * 2003-05-30 2004-12-09 Council Of Scientific And Industrial Research Process for recovery of palladium from spent catalyst
US7473406B2 (en) 2003-05-30 2009-01-06 Council Of Scientific And Industrial Research Process for recovery of palladium from spent catalyst
CN100387344C (en) * 2006-06-21 2008-05-14 浙江工业大学 Method for recovering ruthenium catalyst carried by active carbon
CN102443707A (en) * 2011-11-30 2012-05-09 徐州浩通新材料科技股份有限公司 Method for recycling platinum from organic alcohol waste liquor
US9889429B2 (en) 2012-10-16 2018-02-13 Bill W. Helton Hydrogen production catalysts and associated systems and methods
US10457999B2 (en) * 2014-06-19 2019-10-29 Yeda Research And Development Co. Ltd. Method for platinum group metals recovery from spent catalysts
US11898220B2 (en) 2014-06-19 2024-02-13 Yeda Research And Development Co. Ltd. Apparatus for platinum group metals recovery from spent catalysts
US11473168B2 (en) 2016-10-30 2022-10-18 Yeda Research And Development Co. Ltd. Method for platinum group metals recovery from spent catalysts

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