GB1031194A - Improvements in the fractionation of aqueous solutions - Google Patents

Improvements in the fractionation of aqueous solutions

Info

Publication number
GB1031194A
GB1031194A GB1063663A GB1063663A GB1031194A GB 1031194 A GB1031194 A GB 1031194A GB 1063663 A GB1063663 A GB 1063663A GB 1063663 A GB1063663 A GB 1063663A GB 1031194 A GB1031194 A GB 1031194A
Authority
GB
United Kingdom
Prior art keywords
aqueous
batches
batch
organic
series
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
GB1063663A
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.)
Nihon Genshiryoku Kenkyusho
Original Assignee
Nihon Genshiryoku Kenkyusho
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 Nihon Genshiryoku Kenkyusho filed Critical Nihon Genshiryoku Kenkyusho
Publication of GB1031194A publication Critical patent/GB1031194A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/04Solvent extraction of solutions which are liquid
    • B01D11/0492Applications, solvents used
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G56/00Compounds of transuranic elements
    • C01G56/001Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
    • 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
    • C22B3/26Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
    • C22B3/28Amines
    • 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
    • C22B3/26Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
    • C22B3/38Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds containing phosphorus
    • C22B3/382Phosphine chalcogenides, e.g. compounds of the formula R3P=X with X = O, S, Se or Te
    • 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
    • C22B3/26Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
    • C22B3/38Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds containing phosphorus
    • C22B3/384Pentavalent phosphorus oxyacids, esters thereof
    • C22B3/3846Phosphoric acid, e.g. (O)P(OH)3
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B60/00Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
    • C22B60/02Obtaining thorium, uranium, or other actinides
    • C22B60/0204Obtaining thorium, uranium, or other actinides obtaining uranium
    • C22B60/0217Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes
    • C22B60/0252Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes treatment or purification of solutions or of liquors or of slurries
    • C22B60/026Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes treatment or purification of solutions or of liquors or of slurries liquid-liquid extraction with or without dissolution in organic solvents
    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21CNUCLEAR REACTORS
    • G21C19/00Arrangements for treating, for handling, or for facilitating the handling of, fuel or other materials which are used within the reactor, e.g. within its pressure vessel
    • G21C19/42Reprocessing of irradiated fuel
    • G21C19/44Reprocessing of irradiated fuel of irradiated solid fuel
    • G21C19/46Aqueous processes, e.g. by using organic extraction means, including the regeneration of these means
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors
    • 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
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Metallurgy (AREA)
  • Geology (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Environmental & Geological Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Plasma & Fusion (AREA)
  • General Engineering & Computer Science (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Inorganic Chemistry (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

A mixture of Pu/U/fission products, or a mixture of Fe, Co, and Ni are separated in solution by a graded concentration multi-stage extraction system. There is set up an array of vessels containing batches of an organic extractant for the species to be separated, or a solution of such extractant in an inert diluent, e.g. tributyl phosphate in CCl4 for U/Pu and trioctyl phosphine oxide in CCl4 for Fe, Co, Mi. The materials to be separated are in aqueous mineral acid solution, and a second series of vessels are prepared containing batches of aqueous mineral acid, each batch containing acid of different concentration, the concentration varying stepwise along the aqueous series, the final vessel of this series preferably containing water. The first aqueous batch, i.e. that containing the materials to be separated is mixed with the first batch of organic extractant, allowed to settle and separated, the aqueous layer is then shaken with the second organic batch, and separated and is then shaken in turn with all the remainder of the organic batches. The first aqueous batch is followed through the organic series by the second aqueous batch, i.e. an aqueous acid solution, and the third and subsequent aqueous batches until each aqueous batch has been treated with each organic batch. The net result of this procedure is that upon completion, the organic batches are uncontaminated and may be used again, whilst the mixture of solutes is so distributed through the aqueous series that each solute occupies almost exclusively a particular range of batches in the aqueous series and may thus be easily separated, e.g. 23 batches of aqueous nitric acid used in the separation of U/Pu/fission products batches 1-5 contained almost all the fission products, Pu 239 was contained in batches 6-10 and U was contained in batches 10-20, and similar results were obtained for Fe, Co and Mi using HCl solutions. If desired the concentration of extractant may be varied stepwise from batch to batch in the organic series.ALSO:In a graded concentration multistage extraction system, e.g for a mixture of Pu/U/fission products, or a mixture of Fe, Co, and Ni, there is set up an array of vessels containing batches of an organic extractant for the species to be separated or a solution of such extractant in an inert diluent e.g. tributyl phosphate in CCl4 for U/Pu and trioctyl phosphine oxide in CCl4 for Fe, Co, Mi. The materials to be separated are in aqueous mineral acid solution, and a second series of vessels are prepared containing batches of aqueous mineral acid, each batch containing acid of different concentration, the concentration varying stepwise along the aqueous series the final vessel of this series preferably containing water. The first aqueous batch i.e. that containing the materials to be separated is mixed with the first batch of organic extractant, allowed to settle and separated, the aqueous layer is then shaken with the second organic batch and separated, and is then shaken in turn with all the remainder of the organic batches. The first aqueous batch is followed through the organic series by the second aqueous batch, i.e. an aqueous acid solution, and the third and subsequent aqueous batches until each aqueous bath has been trated with each organic batch. The net result of this procedure is that upon completion, the organic batches are uncontaminated and may be used again, whilst the mixture of solutes is so distributed through the aqueous series that each solute occupies almost exclusively a particular range of batches in the aqueous series and may thus be easily separated e.g. of 23 batches of aqueous nitric acid used in the separation of U/Pu/fission products batches 1-5 contained almost all the fission products, Pu 239 was contained in batches 6-10 and U was contained in batches 10-20, and similar results were obtained for Fe, Co and Ni using HCl solutions. ]If desired the concentration of extractant may be varied stepwise from batch to batch in the organic series.
GB1063663A 1962-04-02 1963-03-18 Improvements in the fractionation of aqueous solutions Expired GB1031194A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP1258462 1962-04-02
JP4481462 1962-10-16

Publications (1)

Publication Number Publication Date
GB1031194A true GB1031194A (en) 1966-06-02

Family

ID=26348209

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1063663A Expired GB1031194A (en) 1962-04-02 1963-03-18 Improvements in the fractionation of aqueous solutions

Country Status (3)

Country Link
DE (1) DE1277812B (en)
FR (1) FR1382924A (en)
GB (1) GB1031194A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3454366A (en) * 1965-06-29 1969-07-08 Commissariat Energie Atomique Electronic controls of a plutonium extraction battery employing neutron detectors
CN110465113A (en) * 2019-08-21 2019-11-19 广东联捷生物科技有限公司 Integrated sample extraction box

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4188361A (en) * 1978-04-12 1980-02-12 Davy International (Oil And Chemicals) Limited Recovery of uranium values

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3454366A (en) * 1965-06-29 1969-07-08 Commissariat Energie Atomique Electronic controls of a plutonium extraction battery employing neutron detectors
CN110465113A (en) * 2019-08-21 2019-11-19 广东联捷生物科技有限公司 Integrated sample extraction box

Also Published As

Publication number Publication date
DE1277812B (en) 1968-09-19
FR1382924A (en) 1964-12-24

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