GB831745A - Process for the recovery of dissolved metal values - Google Patents

Process for the recovery of dissolved metal values

Info

Publication number
GB831745A
GB831745A GB24531/57A GB2453157A GB831745A GB 831745 A GB831745 A GB 831745A GB 24531/57 A GB24531/57 A GB 24531/57A GB 2453157 A GB2453157 A GB 2453157A GB 831745 A GB831745 A GB 831745A
Authority
GB
United Kingdom
Prior art keywords
matrix
solution
metal
char
agitated
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
GB24531/57A
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.)
Arthur D Little Inc
Original Assignee
Arthur D Little Inc
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 Arthur D Little Inc filed Critical Arthur D Little Inc
Publication of GB831745A publication Critical patent/GB831745A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/288Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/42Treatment or purification of solutions, e.g. obtained by leaching by ion-exchange extraction
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/22Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
    • C22B3/24Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition by adsorption on solid substances, e.g. by extraction with solid resins
    • 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

Abstract

Metal values are recovered from aqueous solutions by chemically combining the metal with a substantially water-insoluble chelating agent adsorbed on a solid particulate matrix. Specially suited materials for the matrix are granular activated chars derived from fruit pits or coconut shell, or resins having high absorptive capacity but insignificant ion-exchange activity. Suitable chelating agents include thenoyltrifluoroacetone, 8-hydroxyquinoline, diphenylthio carbazone, dioctyl phosphoric acids, e.g. di-2-ethyl hexyl pyrophosphoric acid, mixtures of mono- and di-octyl orthophosphoric acids, mono-octyl orthophosphoric acid, di-isoamyl pyrophosphoric acid, mixtures of mono- and di-isoamyl orthophosphoric acids, mixtures of mono- and di-2-ethylhexyl orthophosphoric acids, and mixtures of mono- and di-capryl orthophosphoric acids. In one example, an extractive matrix for uranium is prepared by agitating a solution of dioctyl pyrophosphoric acid in ethanol with activated char, and the char is then removed, washed with water and dried in air. In another example an emulsion of di-2-ethylhexyl pyrophosphoric acid in water was agitated with a resin (Duolite S-30), and the resin was then removed, washed, and dried. The prepared matrix is agitated with the aqueous metal-containing medium, in conventional manner such as counter-current or batch, separated, and the matrix now containing the metal is treated with a suitable solvent to remove the chelated metal, and thus regenerate the matrix. By suitable selection of different chelating agents and operating conditions, it is possible to utilize the process to separate the individual metal components of the solution. In an example, a char containing dioctyl pyrophosphoric acid was agitated with a solution containing uranium at a pH of 1.0. The matrix was removed, and the chelated uranium recovered by stripping with a sodium carbonate-bicarbonate solution. Other methods of stripping the metal values from the matrix include washing with a solution of increased hydrogenion concentrations or by washing with a solution containing a complexing agent which forms a more stable compound with the metal, or which can successfully compete for the metal against the chelated form on the matrix. In another example a char containing 8-hydroxyquinoline was agitated with a sulphuric acid solution of cupric copper and nickelous nickel at a pH of 2.3. It is found that when the char is removed, the solution has been freed of copper, and the char is practically free of nickel. The copper may be stripped from the char by washing with a hydrochloric acid solution at pH = 1.ALSO:Metal values are recovered from aqueous solutions by chemically combining the metal with a substantially water-insoluble chelating agent adsorbed on a solid particulate matrix. Specially suited materials for the matrix are granular activated chars derived from fruit pits or coconut shell, or resins having high absorptive capacity but insignificant ion-exchange activity. Suitable chelating agents include thenoyl trifluoroacetone, 8-hydroxyquinoline, Diphenyl thiocarbazone, Diodyl phosphoric acids e.g. di-2-ethyl hexyl pyrophosphoric acid, mixtures of mono and dioctyl orthophosphoric acids, Monsoctyl orthophosphoric acid, mixtures of mono- and di-2-ethyl hexyl orthophosphoric acid, and mixtures of mono- and di-capryl orthophosphoric acids. In one example, an extractive matrix for uranium is prepared by agitating a solution of di-octyl pyrophosphoric acid in ethanol with activated char, removing the char, washing it with water, and drying in air. In another example an emulsion of di-2-ethylhexyl pyrophosphoric acid in water was agitated with a resin (Duolite S-30), the resin was removed, washed and dried. The prepared matrix is agitated with the aqueous metal solution in conventional manner such a countercurrent or batch, separated, and the matrix is then regenerated and the chelated metal removed with a suitable solvent. By suitable selection of different chelating agents and operating conditions it is possible to utilise the process to separate the component metals. In an example, a char containing dioctyl pyrophosphoric acid was agitated with a solution containing uranium at a pH of 1,0. The matrix was regenerated and the uranium recovered by stripping with a sodium carbonate-bicarbonate solution. Other methods of stripping include washing with a solution of increased pH, or with a solution containing a complexing agent which forms a more stable compound with the metal or which can successfully compete for the metal with the chelated form on the matrix. In another example a char containing 8-hydroxyquinoline was agitated with a sulphuric acid solution of cupric and nickelous at a pH of 23. It was found that the solution is freed of copper and that the char is free of nickel. The copper may be stripped from the char by washing with a hydrochloric acid at a pH of 1.
GB24531/57A 1956-08-09 1957-08-02 Process for the recovery of dissolved metal values Expired GB831745A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US831745XA 1956-08-09 1956-08-09

Publications (1)

Publication Number Publication Date
GB831745A true GB831745A (en) 1960-03-30

Family

ID=22176652

Family Applications (1)

Application Number Title Priority Date Filing Date
GB24531/57A Expired GB831745A (en) 1956-08-09 1957-08-02 Process for the recovery of dissolved metal values

Country Status (1)

Country Link
GB (1) GB831745A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4033764A (en) * 1974-05-21 1977-07-05 Laporte Industries Limited Recovery of metals
EP0047978A2 (en) * 1980-09-12 1982-03-24 Hitachi, Ltd. Method for treating a radioactive waste liquid
EP0059623A1 (en) * 1981-02-27 1982-09-08 Hitachi, Ltd. A method of purifying liquid using oxine-impregnated activated charcoal and apparatus therefor
GB2173492A (en) * 1985-04-12 1986-10-15 Samim Soc Azionaria Minero Met Process for the separation of indium from acidic solutions
US4659512A (en) * 1983-12-21 1987-04-21 Pedro B. Macedo Fixation of dissolved metal species with a complexing agent
CN103922507A (en) * 2014-04-21 2014-07-16 中蓝连海设计研究院 Method for treating TDA wastewater through complexing extraction

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4033764A (en) * 1974-05-21 1977-07-05 Laporte Industries Limited Recovery of metals
EP0047978A2 (en) * 1980-09-12 1982-03-24 Hitachi, Ltd. Method for treating a radioactive waste liquid
EP0047978A3 (en) * 1980-09-12 1982-06-23 Hitachi, Ltd. Method for treating a radioactive waste liquid
EP0059623A1 (en) * 1981-02-27 1982-09-08 Hitachi, Ltd. A method of purifying liquid using oxine-impregnated activated charcoal and apparatus therefor
US4659512A (en) * 1983-12-21 1987-04-21 Pedro B. Macedo Fixation of dissolved metal species with a complexing agent
GB2173492A (en) * 1985-04-12 1986-10-15 Samim Soc Azionaria Minero Met Process for the separation of indium from acidic solutions
FR2580187A1 (en) * 1985-04-12 1986-10-17 Samim Soc Azionaria Minero Met PROCESS FOR SEPARATING INDIUM FROM ACID SOLUTIONS CONTAINING IT
CN103922507A (en) * 2014-04-21 2014-07-16 中蓝连海设计研究院 Method for treating TDA wastewater through complexing extraction
CN103922507B (en) * 2014-04-21 2015-12-09 中蓝连海设计研究院 A kind of method adopting complexometric extraction process TDA waste water

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