GB1312765A - Benefication process for iron-containing titaniferous material - Google Patents

Benefication process for iron-containing titaniferous material

Info

Publication number
GB1312765A
GB1312765A GB675071*[A GB1312765DA GB1312765A GB 1312765 A GB1312765 A GB 1312765A GB 1312765D A GB1312765D A GB 1312765DA GB 1312765 A GB1312765 A GB 1312765A
Authority
GB
United Kingdom
Prior art keywords
heating
tio
leaching
until
iron content
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
GB675071*[A
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.)
British Titan Ltd
Original Assignee
British Titan Ltd
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 British Titan Ltd filed Critical British Titan Ltd
Publication of GB1312765A publication Critical patent/GB1312765A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G23/00Compounds of titanium
    • C01G23/04Oxides; Hydroxides
    • C01G23/047Titanium dioxide
    • C01G23/053Producing by wet processes, e.g. hydrolysing titanium salts
    • C01G23/0532Producing by wet processes, e.g. hydrolysing titanium salts by hydrolysing sulfate-containing salts
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B34/00Obtaining refractory metals
    • C22B34/10Obtaining titanium, zirconium or hafnium
    • C22B34/12Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
    • C22B34/1204Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 preliminary treatment of ores or scrap to eliminate non- titanium constituents, e.g. iron, without attacking the titanium constituent
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/61Micrometer sized, i.e. from 1-100 micrometer

Landscapes

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

Abstract

1312765 Upgrading ilmenite BRITISH TITAN Ltd 15 Oct 1971 [12 March 1971] 6750/71 Addition to 1282508 Headings C1A and C1N A TiO 2 concentrate is obtained by heating comminuted massive ilmenite at 700-800‹ C. to oxidize the iron content to Fe<SP>3+</SP>, heating at 650-800‹ C. to reduce the iron content to Fe<SP>2+</SP>, leaching with 10-30% H 2 SO 4 until the TiO 2 content of the dry solid is 70-80% by wt., and heating at 100-800‹ C. Both initial heating steps may be carried out in a fluidized bed or rotary kiln. The reducing agent may be H 2 (Œ steam), CO, or CH 4 , e.g. natural gas. The initial material may have an average particle size below 355 Á and may be milled before leaching until 85-90% of the particles are below 44 Á. Leaching may be effected in at least 2 stages at above 100‹ C., preferably at b.pt., using waste sulphate process acid, optionally in the presence of a cationic surfactant. The leached product may be washed and dried at above 100‹ C., e.g. 200‹ C. It may then be digested in conc. H 2 SO 4 and dissolved to form a titanyl sulphate solution, an organic flocculating agent added and the solids removed, and the solution hydrolysed to give TiO 2 .
GB675071*[A 1971-03-12 1971-03-12 Benefication process for iron-containing titaniferous material Expired GB1312765A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB675071 1971-03-12

Publications (1)

Publication Number Publication Date
GB1312765A true GB1312765A (en) 1973-04-04

Family

ID=9820101

Family Applications (1)

Application Number Title Priority Date Filing Date
GB675071*[A Expired GB1312765A (en) 1971-03-12 1971-03-12 Benefication process for iron-containing titaniferous material

Country Status (6)

Country Link
AU (1) AU3481171A (en)
CA (1) CA957511A (en)
DE (1) DE2157341A1 (en)
FR (1) FR2128309A6 (en)
GB (1) GB1312765A (en)
ZA (1) ZA716997B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0801030A2 (en) * 1996-04-13 1997-10-15 Tioxide Group Services Limited Production of titanium oxide
WO2005026397A2 (en) * 2003-09-18 2005-03-24 Outokumpu Technology Oy Process and plant for the heat treatment of solids containing titanium
EP1733063A1 (en) * 2004-03-18 2006-12-20 BHP Billiton Innovation Pty Ltd Production of titania

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3418269A1 (en) * 1984-05-17 1985-11-21 Metallgesellschaft Ag, 6000 Frankfurt METHOD FOR PRODUCING A TIO (DOWN ARROW) 2 (ARROW DOWN) CONCENTRATES FROM TIO (DOWN ARROW) 2 (ARROW DOWN) CONTAINERS
DE3924796A1 (en) * 1989-07-27 1991-01-31 Metallgesellschaft Ag GAINING TIO (ARROW DOWN) 2 (ARROW DOWN) CONCENTRATES FROM TIO (ARROW DOWN) 2 (ARROW ABLE) CONTAINING SUBSTANCES
FI104965B (en) * 1997-04-03 2000-05-15 Kemira Pigments Oy Process for the preparation of titanium dioxide

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0801030A2 (en) * 1996-04-13 1997-10-15 Tioxide Group Services Limited Production of titanium oxide
US6090354A (en) * 1996-04-13 2000-07-18 Tioxide Group Services Limited Process for the production of titanium oxide
WO2005026397A2 (en) * 2003-09-18 2005-03-24 Outokumpu Technology Oy Process and plant for the heat treatment of solids containing titanium
WO2005026397A3 (en) * 2003-09-18 2005-07-21 Outokumpu Oy Process and plant for the heat treatment of solids containing titanium
AU2004272735B2 (en) * 2003-09-18 2009-12-10 Outotec Oyj Process and plant for the heat treatment of solids containing titanium
EP1733063A1 (en) * 2004-03-18 2006-12-20 BHP Billiton Innovation Pty Ltd Production of titania
EP1733063A4 (en) * 2004-03-18 2008-10-01 Bhp Billiton Innovation Pty Production of titania

Also Published As

Publication number Publication date
FR2128309A6 (en) 1972-10-20
CA957511A (en) 1974-11-12
AU3481171A (en) 1973-05-03
ZA716997B (en) 1973-06-27
DE2157341A1 (en) 1972-09-21

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee