GB966807A - Improvements in or relating to the production of uranium - Google Patents

Improvements in or relating to the production of uranium

Info

Publication number
GB966807A
GB966807A GB18109/62A GB1810962A GB966807A GB 966807 A GB966807 A GB 966807A GB 18109/62 A GB18109/62 A GB 18109/62A GB 1810962 A GB1810962 A GB 1810962A GB 966807 A GB966807 A GB 966807A
Authority
GB
United Kingdom
Prior art keywords
alloy
stirrer
cathode
uranium
molybdenum
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
GB18109/62A
Inventor
Alan Robert Gibson
Ronald George Avery
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.)
UK Atomic Energy Authority
Original Assignee
UK Atomic Energy Authority
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 UK Atomic Energy Authority filed Critical UK Atomic Energy Authority
Priority to GB18109/62A priority Critical patent/GB966807A/en
Priority to US277894A priority patent/US3272726A/en
Priority to DEU9792A priority patent/DE1191117B/en
Priority to FR934302A priority patent/FR1363451A/en
Priority to ES287883A priority patent/ES287883A1/en
Publication of GB966807A publication Critical patent/GB966807A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/34Electrolytic production, recovery or refining of metals by electrolysis of melts of metals not provided for in groups C25C3/02 - C25C3/32
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/005Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells of cells for the electrolysis of melts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

<PICT:0966807/C6-C7/1> Pure uranium, or an alloy thereof, is produced electrolytically using as electrolyte an alkaline earth metal halide, e.g. MgCl2 or CaCl2 in which UO2 is suspended, and maintaining the temperature below the melting point of uranium metal, e.g. 850-950 DEG C. The cathode may be inert, e.g. molybdenum, or may form an alloy with uranium, e.g. using a molten layer of aluminium. For example, an aluminium alloy containing 74.2% U is formed corresponding to UAl3. This powder is washed and heated in an alumina boat at 1500 DEG C. in vacuo, yielding a product of 79% U corresponding to UAl2, melting at 1590 DEG C. An iron alloy is made using as cathode a eutectic mixture of U and Fe containing 183 g. U and 26 g. Fe; after electrolysis the cathode alloy contained 89% U compared with 87.6% of the original cathode alloy. In a suitable apparatus, an alumina crucible 1 heated in a furnace 2 is provided with a lid of pyrophyllite having an aperture 5 for the supply of an inert gas, e.g. argon. Carbon black anodes 12a are carried on a graphite rod 13 protected by an alumina sheath 14. A stirrer 6 of molybdenum is carried on an inner steel shaft 7, and the molybdenum cathodes 9 are circular and provided with louvres 10, through which the suspension of UO2 flows impelled by the stirrer. The cathodes are connected to a tungsten rod 11. A suspension of hydrogen-refined UO2 is suspended in molten CaCl2 and this electrolyte is treated at 5-6V. for 2 hours, the stirrer being stopped before the end of the run to ensure reduction of any UO2 resting on the cathode. The product of pure uranium powder is then washed and dried. The UO2 used as starting material is either electrolytic or hydrogen-precipitated; the hydro-precipitated oxide is not satisfactory. In apparatus for making U/Al alloy no stirrer is used, but in the case of U/Fe alloys a stirrer may be employed. Specification 889,307 is referred to.
GB18109/62A 1961-05-10 1961-05-10 Improvements in or relating to the production of uranium Expired GB966807A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
GB18109/62A GB966807A (en) 1961-05-10 1961-05-10 Improvements in or relating to the production of uranium
US277894A US3272726A (en) 1961-05-10 1963-05-03 Production of uranium
DEU9792A DE1191117B (en) 1961-05-10 1963-05-08 Process and device for the electrolytic production of uranium or uranium alloys
FR934302A FR1363451A (en) 1961-05-10 1963-05-09 Process for the electrolytic production of metallic uranium and its alloys
ES287883A ES287883A1 (en) 1961-05-10 1963-05-10 Procedure and apparatus for the obtaining of metallic uranium or an alloy thereof (Machine-translation by Google Translate, not legally binding)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB18109/62A GB966807A (en) 1961-05-10 1961-05-10 Improvements in or relating to the production of uranium

Publications (1)

Publication Number Publication Date
GB966807A true GB966807A (en) 1964-08-19

Family

ID=10106810

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18109/62A Expired GB966807A (en) 1961-05-10 1961-05-10 Improvements in or relating to the production of uranium

Country Status (5)

Country Link
US (1) US3272726A (en)
DE (1) DE1191117B (en)
ES (1) ES287883A1 (en)
FR (1) FR1363451A (en)
GB (1) GB966807A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3948735A (en) * 1973-06-01 1976-04-06 The United States Of America As Represented By The United States Energy Research And Development Administration Concentration and purification of plutonium or thorium
GB9018419D0 (en) * 1990-08-22 1990-10-03 British Nuclear Fuels Plc A method of producing uranium alloy and apparatus therefor
US6911134B2 (en) * 2002-09-06 2005-06-28 The University Of Chicago Three-electrode metal oxide reduction cell
US10550489B2 (en) * 2016-07-11 2020-02-04 Uchicago Argonne, Llc Actinide and rare earth drawdown system for molten salt recycle
GB2570700A (en) * 2018-02-03 2019-08-07 Richard Scott Ian Continuous processing of spent nuclear fuel
CN113023782B (en) * 2021-03-10 2023-05-05 哈尔滨工程大学 Sodium diuranate (Na) 2 U 2 O 7 ) Direct preparation of UO 2 Is a method of (2)

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE538989A (en) *
US2519792A (en) * 1942-04-10 1950-08-22 Rosen Raphael Electrolytic production of metallic uranium
US2773825A (en) * 1944-04-28 1956-12-11 Frank A Newcombe Electrolysis apparatus
US2781304A (en) * 1946-08-15 1957-02-12 Harley A Wilhelm Electrodeposition of uranium
US2951793A (en) * 1957-10-09 1960-09-06 Wilford N Hansen Electrolysis of thorium and uranium
US3079324A (en) * 1958-06-30 1963-02-26 Dow Chemical Co Apparatus for production of uranium

Also Published As

Publication number Publication date
FR1363451A (en) 1964-06-12
US3272726A (en) 1966-09-13
ES287883A1 (en) 1963-08-01
DE1191117B (en) 1965-04-15

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