GB674400A - Treatment of monazite - Google Patents

Treatment of monazite

Info

Publication number
GB674400A
GB674400A GB18286/50A GB1828650A GB674400A GB 674400 A GB674400 A GB 674400A GB 18286/50 A GB18286/50 A GB 18286/50A GB 1828650 A GB1828650 A GB 1828650A GB 674400 A GB674400 A GB 674400A
Authority
GB
United Kingdom
Prior art keywords
thorium
uranium
caustic soda
acid
hydroxides
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
GB18286/50A
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.)
PRODUITS CHIM TERRES RARES SOC
Original Assignee
PRODUITS CHIM TERRES RARES SOC
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 PRODUITS CHIM TERRES RARES SOC filed Critical PRODUITS CHIM TERRES RARES SOC
Publication of GB674400A publication Critical patent/GB674400A/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
    • 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
    • C22B60/0221Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes by leaching
    • C22B60/0247Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes by leaching using basic solutions or liquors
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F15/00Compounds of thorium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B59/00Obtaining rare earth metals
    • 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
    • C22B60/0291Obtaining thorium, uranium, or other actinides obtaining thorium

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Environmental & Geological Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

Ground monazite is attacked by, say 55-70 per cent, caustic soda solution near the boiling point, and the reaction mixture is diluted at above 55 DEG C, with water or a mother liquor from a subsequent operation to produce a solution of sodium phosphate, which is crystallized, and insoluble thorium, uranium and rare earth hydroxides which are subsequently separated. For the separation, the hydroxides are washed with dilute caustic soda solution-the wash liquor being used in the dilution operation -to reduce the P2O5 content to less than 1 per cent by weight of the hydroxides, and treated by hydrochloric, nitric or sulphuric acid to effect separation of the rare earths from the uranium and thorium. The acid treatment comprises (a) complete dissolution followed by neutralization with rare earth carbonates to pH about 4 to precipitate thorium, or (b) addition of acid to pH about 3.2 to dissolve the rare earths leaving the thorium and uranium insoluble. During the acid extraction, iron is oxidized. The rare earth chloride, say, solution may be evaporated to dryness, or the carbonates precipitated by sodium carbonate. The thorium concentrate may be dissolved in hydrochloric or nitric acid, and thorium sulphate then precipitated by sulphuric acid. The mother liquor is treated with potassium sulphate to precipitate the remainder of the thorium as thorium-potassium sulphate, and residual rare earths. The double salt is attacked by caustic soda, and the hydroxides returned to the acid treatment stage, (a) or (b) above. The mother liquor containing uranium is treated with sodium carbonate, and the uranium precipitated by caustic soda. The caustic soda mother liquor from the crystallization of the sodium phosphate may be used in the dilution operation, or may be concentrated for reuse in the attack on the monaazite.
GB18286/50A 1949-07-21 1950-07-21 Treatment of monazite Expired GB674400A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR674400X 1949-07-21

Publications (1)

Publication Number Publication Date
GB674400A true GB674400A (en) 1952-06-25

Family

ID=9018733

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18286/50A Expired GB674400A (en) 1949-07-21 1950-07-21 Treatment of monazite

Country Status (1)

Country Link
GB (1) GB674400A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013203048A1 (en) * 2013-02-25 2014-08-28 Siemens Aktiengesellschaft Process for the extraction of rare earths
CN111018223A (en) * 2019-12-26 2020-04-17 湖南中核金原新材料有限责任公司 Method for realizing zero discharge of wastewater in process of producing rare earth chloride from monazite
CN111945001A (en) * 2019-05-17 2020-11-17 永州市湘江稀土有限责任公司 Treatment method of monazite optimal slag

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013203048A1 (en) * 2013-02-25 2014-08-28 Siemens Aktiengesellschaft Process for the extraction of rare earths
CN111945001A (en) * 2019-05-17 2020-11-17 永州市湘江稀土有限责任公司 Treatment method of monazite optimal slag
CN111945001B (en) * 2019-05-17 2021-12-03 永州市湘江稀土有限责任公司 Treatment method of monazite optimal slag
CN111018223A (en) * 2019-12-26 2020-04-17 湖南中核金原新材料有限责任公司 Method for realizing zero discharge of wastewater in process of producing rare earth chloride from monazite

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