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GB1425779A - Recovery of titanium dioxide from ores - Google Patents

Recovery of titanium dioxide from ores

Info

Publication number
GB1425779A
GB1425779A GB413874A GB413874A GB1425779A GB 1425779 A GB1425779 A GB 1425779A GB 413874 A GB413874 A GB 413874A GB 413874 A GB413874 A GB 413874A GB 1425779 A GB1425779 A GB 1425779A
Authority
GB
United Kingdom
Prior art keywords
titanium
iron
oxyhydrate
ore
concentrate
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
GB413874A
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.)
Ortech Corp
Original Assignee
Ortech Corp
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 Ortech Corp filed Critical Ortech Corp
Publication of GB1425779A publication Critical patent/GB1425779A/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
    • 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
    • C22B34/1236Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching
    • C22B34/124Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching using acidic solutions or liquors
    • C22B34/1245Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching using acidic solutions or liquors containing a halogen ion as active agent
    • 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

Landscapes

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

Abstract

1425779 Recovery of TiO 2 from ilmenite ONTARIO RESEARCH FOUNDATION 29 Jan 1974 [2 Feb 1973] 04138/74 Heading C1N Pigment grade TiO 2 is recovered from ilmenite by (i) contacting the ore or a concentrate thereof in particulate form with concentrated hydrochloric acid at 15‹ to 30‹ C. to leach from the ore or concentrate at least 80%, preferably at least 95%, of the titanium and iron values, the hydrochloric acid being present in such a quantity as to provide at least 2 moles of HCl per mole of ferrous iron, at least 3 moles of HCl per mole of ferric iron and at least 4 moles of HCl per mole of titanium in the ore concentrate, (ii) separating the resulting leach liquor from residual solid material, (iii) converting any ferric iron present in the leach liquor to ferrous iron to provide an aqueous solution of titanium chlorides and ferrous chloride, (iv) hydrolysing the titanium chlorides and depositing titanium oxyhydrate while inhibiting the deposition of other metal hydroxides, (v) separating the deposited titanium oxyhydrate from the mother liquor, (vi) washing and drying the separated material and (vii) converting the dried oxyhydrate to titanium dioxide. The ore or concentrate may be treated prior to leaching, e.g. by an oxidation at 600‹ to 1000‹ C. and preferably has a particle size distribution of 90 to 95%-100 mesh and less than 50%-325 mesh. The leaching is preferably performed countercurrently at 20‹ to 25‹ C. The ferric iron values are converted to ferrous iron by the use of SO 2 or by the addition of powdered metallic iron to the solution at between 50‹ and 95‹ C. When powdered iron is used a quantity sufficient to convert all the ferric iron to ferrous iron and up to 1% of the tetravalent titanium to trivalent titanium is used. The titanium chlorides are preferably hydrolysed with 1 to 3 volumes of water per volume of leach liquor and 1 to 2% of titanium oxyhydrate is preferably added as a seed. The dried titanium oxyhydrate is suitably converted to anatase or rutile titania by heating at 700‹ to 1000‹ C. The iron values may be recovered and the hydrogen chloride values recycled to the leaching step.
GB413874A 1973-02-02 1974-01-29 Recovery of titanium dioxide from ores Expired GB1425779A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CA163,317A CA980979A (en) 1973-02-02 1973-02-02 Recovery of titanium dioxide from ores

Publications (1)

Publication Number Publication Date
GB1425779A true GB1425779A (en) 1976-02-18

Family

ID=4095786

Family Applications (1)

Application Number Title Priority Date Filing Date
GB413874A Expired GB1425779A (en) 1973-02-02 1974-01-29 Recovery of titanium dioxide from ores

Country Status (5)

Country Link
JP (1) JPS547249B2 (en)
AU (1) AU476816B2 (en)
CA (1) CA980979A (en)
DE (1) DE2405271C3 (en)
GB (1) GB1425779A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008082384A1 (en) * 2006-12-28 2008-07-10 E. I. Du Pont De Nemours And Company Processes for producing titanium dioxide
US8137647B2 (en) 2006-12-28 2012-03-20 E. I. Du Pont De Nemours And Company Processes for producing titanium dioxide
CN114162861A (en) * 2021-12-30 2022-03-11 龙佰集团股份有限公司 Comprehensive utilization method of artificial rutile mother liquor
CN116477659A (en) * 2023-04-25 2023-07-25 广东粤桥新材料科技有限公司 Method for co-producing artificial rutile and ferric phosphate

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MX2011001286A (en) * 2008-08-06 2011-03-21 Du Pont Processes for producing titanium dioxide.
CN115974140A (en) * 2021-11-27 2023-04-18 四川省有色矿冶科技有限公司 Method for producing titanium oxychloride by acidolysis of ilmenite with hydrochloric acid acidolysis solution

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008082384A1 (en) * 2006-12-28 2008-07-10 E. I. Du Pont De Nemours And Company Processes for producing titanium dioxide
US8137647B2 (en) 2006-12-28 2012-03-20 E. I. Du Pont De Nemours And Company Processes for producing titanium dioxide
CN101622198B (en) * 2006-12-28 2012-07-11 纳幕尔杜邦公司 Processes for producing titanium dioxide
CN114162861A (en) * 2021-12-30 2022-03-11 龙佰集团股份有限公司 Comprehensive utilization method of artificial rutile mother liquor
CN114162861B (en) * 2021-12-30 2024-03-08 龙佰集团股份有限公司 Synthetic rutile mother liquor comprehensive utilization method
CN116477659A (en) * 2023-04-25 2023-07-25 广东粤桥新材料科技有限公司 Method for co-producing artificial rutile and ferric phosphate
CN116477659B (en) * 2023-04-25 2024-04-26 广东粤桥新材料科技有限公司 Method for co-producing artificial rutile and ferric phosphate

Also Published As

Publication number Publication date
AU476816B2 (en) 1976-10-07
DE2405271C3 (en) 1979-10-04
DE2405271A1 (en) 1974-08-08
CA980979A (en) 1976-01-06
JPS49110517A (en) 1974-10-21
JPS547249B2 (en) 1979-04-05
AU6508374A (en) 1975-08-07
DE2405271B2 (en) 1979-02-08

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Legal Events

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