GB1425779A - Recovery of titanium dioxide from ores - Google Patents
Recovery of titanium dioxide from oresInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1236—Obtaining 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
- C22B34/124—Obtaining 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
- C22B34/1245—Obtaining 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
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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.
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)
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)
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 |
-
1973
- 1973-02-02 CA CA163,317A patent/CA980979A/en not_active Expired
-
1974
- 1974-01-29 GB GB413874A patent/GB1425779A/en not_active Expired
- 1974-02-01 AU AU65083/74A patent/AU476816B2/en not_active Expired
- 1974-02-02 JP JP1331674A patent/JPS547249B2/ja not_active Expired
- 1974-02-04 DE DE2405271A patent/DE2405271C3/en not_active Expired
Cited By (7)
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 |