CA2480865A1 - Acid beneficiation of ore - Google Patents
Acid beneficiation of ore Download PDFInfo
- Publication number
- CA2480865A1 CA2480865A1 CA002480865A CA2480865A CA2480865A1 CA 2480865 A1 CA2480865 A1 CA 2480865A1 CA 002480865 A CA002480865 A CA 002480865A CA 2480865 A CA2480865 A CA 2480865A CA 2480865 A1 CA2480865 A1 CA 2480865A1
- Authority
- CA
- Canada
- Prior art keywords
- process according
- iron
- ore
- titaniferous ore
- pretreated
- 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.)
- Granted
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
- C22B34/125—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 sulfur ion as active agent
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G23/00—Compounds of titanium
- C01G23/04—Oxides; Hydroxides
- C01G23/047—Titanium dioxide
- C01G23/053—Producing by wet processes, e.g. hydrolysing titanium salts
- C01G23/0532—Producing by wet processes, e.g. hydrolysing titanium salts by hydrolysing sulfate-containing salts
-
- 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
- C22B19/00—Obtaining zinc or zinc oxide
- C22B19/20—Obtaining zinc otherwise than by distilling
-
- 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
- C22B34/1204—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 preliminary treatment of ores or scrap to eliminate non- titanium constituents, e.g. iron, without attacking the titanium constituent
- C22B34/1213—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 preliminary treatment of ores or scrap to eliminate non- titanium constituents, e.g. iron, without attacking the titanium constituent by wet processes, e.g. using leaching methods or flotation techniques
-
- 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
Abstract
Processes for the efficient and economical beneficiation of titaniferous ore are provided. A unique process for beneficiating ore comprising pretreatment of the ore by oxidation and reduction, followed by acid leaching with sulfur ic acid has been developed. The acid used in this process may be recycled, whic h will thereby increase the efficiency of the process. Preferably the ore treated according to the present invention is ilmenite ore.
Claims (32)
1. A process for snaking a TiO2 product comprising:
a. leaching a pretreated titaniferous ore with sulfuric acid to form a liquid phase and an undissolved titanium oxide phase, wherein said pretreated titaniferous ore is comprised of iron and substantially all of the iron is ferrous iron and said pretreated ore is obtained by oxidizing and reducing a titaniferous ore; and b. separating a TiO2 product from said undissolved titanium oxide phase.
a. leaching a pretreated titaniferous ore with sulfuric acid to form a liquid phase and an undissolved titanium oxide phase, wherein said pretreated titaniferous ore is comprised of iron and substantially all of the iron is ferrous iron and said pretreated ore is obtained by oxidizing and reducing a titaniferous ore; and b. separating a TiO2 product from said undissolved titanium oxide phase.
2. The process according to claim 1, wherein said titaniferous ore is ilmenite ore.
3. The process according to claim 1, wherein said oxidizing occurs at a temperature of from about 800°C to about 1150°C.
4. The process according to claim 1, wherein said oxidizing of said titaniferous ore results in the formation of pseudobrookite.
5. The process according to claim 1, wherein said reducing occurs at a temperature of from about 800°C to about 1000°C.
6. The process according to claim 1, wherein less than about 1% of the iron is metallic iron.
7. The process according to claim 1, wherein said sulfuric acid is in a concentration of from about 5% to about 50%.
8. The process according to claim 1, wherein said leaching occurs between the temperatures of 110°C and 200°C.
9. A process for producing TiO2 feedstock comprising calcining the TiO2 product of claim 1 to produce a TiO2 feedstock.
10. A process for making a TiO2 product comprising:
a. leaching a pretreated titaniferous ore with sulfuric acid to form a liquid phase and an undissolved titanium oxide phase, wherein said pretreated titaniferous ore is comprised of iron and substantially all of the iron is ferrous iron, and wherein said liquid phase is comprised of fines; and b. separating a TiO2 product from said fines.
a. leaching a pretreated titaniferous ore with sulfuric acid to form a liquid phase and an undissolved titanium oxide phase, wherein said pretreated titaniferous ore is comprised of iron and substantially all of the iron is ferrous iron, and wherein said liquid phase is comprised of fines; and b. separating a TiO2 product from said fines.
11. The process according to claim 9, wherein said pretreated ore is obtained by oxidizing and reducing a titaniferous ore.
12. The process according to claim 9, wherein said titaniferous ore is ilmenite ore.
13. The process according to claim 10, wherein said oxidizing occurs at a temperature of from about 800°C to about 1150°C.
14. The process according to claim 10, wherein said oxidizing of said titaniferous ore results in the formation of pseudobrookite.
15. The process according to claim 10, wherein said reducing occurs at a temperature of from about 800°C to about 1000°C.
16. The process according to claim 9, wherein less than about 1% of the iron is metallic iron.
17. The process according to claim 9, wherein said sulfuric acid is in a concentration of from about 5% to about 50%.
18. The process according to claim 10, wherein said leaching occurs between the temperatures of 110°C and 200°C.
19. The process according to claim 9, wherein said fines comprise titanium dioxide or titanium hydrolysate.
20. The process according to claim 17, wherein said fines further comprise iron sulfate.
21. The process according to claim 18, wherein said separating further comprises a. re-slurrying and dissolving said iron sulfate to form dissolved iron sulfate; and b. filtering said dissolved iron sulfate to form a titanium dioxide or titanium hydrolysate product.
22. The process according to claim 19, wherein said re-slurrying and dissolving is performed in the presence of acid.
23. A process for making a first TiO2 product and second TiO2 product comprising:
a. leaching pretreated titaniferous ore with sulfuric acid to form a liquid phase and an undissolved titanium oxide phase, wherein said pretreated titaniferous ore is comprised of iron and substantially all of the iron is ferrous iron;
b. separating a first TiO2 product from said undissolved titanium oxide phase; and c. separating a second TiO2 product from said liquid phase.
a. leaching pretreated titaniferous ore with sulfuric acid to form a liquid phase and an undissolved titanium oxide phase, wherein said pretreated titaniferous ore is comprised of iron and substantially all of the iron is ferrous iron;
b. separating a first TiO2 product from said undissolved titanium oxide phase; and c. separating a second TiO2 product from said liquid phase.
24. A process for recycling acid during the production of a TiO2 product, the process comprising the steps of:
a. treating a first titaniferous ore with a leaching agent to form a liquid phase and a coarse particle phase, wherein said liquid phase comprises dissolved iron salts;
b. separating the liquid phase from the coarse particle phase;
c. crystallizing and removing said dissolved iron salts from said liquid phase to yield a residual acid; and d. recycling said residual acid to treat a second titaniferous ore.
a. treating a first titaniferous ore with a leaching agent to form a liquid phase and a coarse particle phase, wherein said liquid phase comprises dissolved iron salts;
b. separating the liquid phase from the coarse particle phase;
c. crystallizing and removing said dissolved iron salts from said liquid phase to yield a residual acid; and d. recycling said residual acid to treat a second titaniferous ore.
25. The process according to claim 22, wherein said first titaniferous ore and said second titaniferous ore are both ilmenite.
26. The process according to claim 22 further comprising pretreating said first titaniferous ore prior to treating said first titaniferous ore with said leaching agent, wherein said pretreating forms a pretreated ore that is comprised of iron and substantially all of the iron is ferrous iron.
27. The process according to claim 22, wherein said leaching agent is sulfuric acid.
28. The process according to claim 22, wherein said crystallizing and removing is accomplished by vacuum crystallization.
29. The process according to claim 22, wherein said crystallizing and removing is accomplished by cooling crystallization.
30. The process according to claim 22, wherein said crystallizing and removing is accomplished by adding virgin or high concentration waste acid.
31. The process according to claim 22, wherein during said crystallizing and removing, iron sulfate monohydrate or tetrahydrate are added.
32. The process according to claim 22 further comprising evaporating and reconcentrating said residual acid.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/126,241 US7008602B2 (en) | 2002-04-19 | 2002-04-19 | Beneficiation of titaniferous ore with sulfuric acid |
US10/126,241 | 2002-04-19 | ||
PCT/US2003/012656 WO2003089674A2 (en) | 2002-04-19 | 2003-04-15 | Acid beneficiation of ore |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2480865A1 true CA2480865A1 (en) | 2003-10-30 |
CA2480865C CA2480865C (en) | 2011-07-26 |
Family
ID=29214980
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2480865A Expired - Lifetime CA2480865C (en) | 2002-04-19 | 2003-04-15 | Acid beneficiation of ore |
Country Status (9)
Country | Link |
---|---|
US (1) | US7008602B2 (en) |
EP (1) | EP1499752B1 (en) |
AT (1) | ATE435309T1 (en) |
AU (1) | AU2003239166B2 (en) |
BR (1) | BRPI0309330B1 (en) |
CA (1) | CA2480865C (en) |
DE (1) | DE60328178D1 (en) |
NO (1) | NO20044509L (en) |
WO (1) | WO2003089674A2 (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BR0304443B1 (en) * | 2003-10-28 | 2012-08-21 | process for obtaining high thio2 and low radionuclide titanium concentrates from mechanical anatase concentrates. | |
JP5102770B2 (en) * | 2005-10-11 | 2012-12-19 | ヨマ インターナショナル アーエス | Titanium product manufacturing process |
US7625536B2 (en) * | 2005-10-18 | 2009-12-01 | Millennium Inorganic Chemicals, Inc. | Titaniferous ore beneficiation |
IL200860A (en) * | 2009-09-10 | 2015-07-30 | Green Future Ltd | Galvanic waste sludge treatment and manufacturing of nano-sized iron oxides |
GB2480439A (en) * | 2010-05-17 | 2011-11-23 | Tioxide Europe Ltd | A process for forming ferrous sulphate monohydrate |
DE102012104717A1 (en) * | 2011-05-31 | 2012-12-06 | Sachtleben Chemie Gmbh | Process for the production of titanium dioxide |
CN102336433A (en) * | 2011-08-04 | 2012-02-01 | 四川龙蟒钛业股份有限公司 | Pretreatment method in the process of preparing titanium dioxide by reusing acidolysis residues |
US10287176B2 (en) | 2014-07-08 | 2019-05-14 | Avertana Limited | Extraction of products from titanium-bearing minerals |
CN104803415B (en) | 2015-05-15 | 2016-06-15 | 云南民族大学 | A kind of method being prepared rutile by acid-dissolved titanium slag |
CN105296771B (en) * | 2015-11-23 | 2018-05-22 | 沈阳理工大学 | A kind of method using ilmenite concentrate production rich-titanium material |
CN106745229B (en) * | 2017-02-02 | 2018-07-31 | 徐州钛白化工有限责任公司 | A kind of manufacture craft of pharmaceutical grade titanium dioxide |
US10116224B1 (en) | 2017-06-14 | 2018-10-30 | Northrop Grumman Systems Corporation | Switching power converter circuit |
CN111910089A (en) * | 2020-07-21 | 2020-11-10 | 山东鲁北企业集团总公司 | Preparation method of titanium-rich raw material for producing titanium dioxide and titanium-rich raw material produced by using method |
CN117396435A (en) * | 2020-10-06 | 2024-01-12 | 美盛公司 | Method for producing titanium dioxide from anatase ore by digestion with sulfuric acid and subsequent leaching, hydrolysis and calcination |
CN114752772A (en) * | 2022-03-16 | 2022-07-15 | 中南大学 | Method for preparing fluidized chlorination furnace charge by upgrading titanium slag |
Family Cites Families (69)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2899278A (en) | 1959-08-11 | lewis | ||
US542749A (en) * | 1895-07-16 | Robert bateson | ||
US2127247A (en) | 1935-06-15 | 1938-08-16 | Du Pont | Preparation of compounds of titanium |
US2488439A (en) | 1946-03-09 | 1949-11-15 | Du Pont | Production of titanium oxide pigments |
US2488440A (en) | 1946-11-30 | 1949-11-15 | Du Pont | Titanium dioxide pigment production |
US2559638A (en) | 1947-07-25 | 1951-07-10 | Du Pont | Production of titanium dioxide |
US2721626A (en) | 1951-12-15 | 1955-10-25 | Du Pont | Cooling and separating by condensation of hot gaseous suspensions |
US2833627A (en) | 1956-01-03 | 1958-05-06 | Du Pont | Method for cooling the hot, gas-containing reaction products resulting from the oxidation of titanium tetrachloride |
DE1111403B (en) | 1958-01-11 | 1961-07-20 | Sueddeutsche Kalkstickstoff | Process for separating the alkaline earth metals and alkaline earth oxides from the reaction product of the metallo-thermal production of titanium or zirconium |
GB980864A (en) | 1960-01-15 | 1965-01-20 | Laporte Titanium Ltd | Improved process for the beneficiation of ores |
GB1026691A (en) | 1961-04-21 | 1966-04-20 | Laporte Titanium Ltd | Improvements in or relating to the treatment of titanium bearing ores |
BE661424A (en) | 1963-06-11 | 1900-01-01 | ||
US3467414A (en) * | 1966-09-30 | 1969-09-16 | Ronald T Downing | Tube joint having buckled locking means |
US3446590A (en) | 1966-10-21 | 1969-05-27 | Nat Lead Co | Titanium dioxide concentrate and method for producing the same |
AU416143B2 (en) | 1967-05-01 | 1969-11-06 | COMMONWEALTH SCIENTIFIC AND INDUSTRIAL RESEARCH ORGANIZATION and MURPHYORES INCORPORATED PTY. LTD | A process forthe beneficiation of titaniferous ores |
US3457037A (en) | 1967-08-15 | 1969-07-22 | Nat Lead Co | Method for producing titanium dioxide concentrate from massive ilmenite ores |
GB1243798A (en) | 1968-08-14 | 1971-08-25 | British Titan Ltd Formerly Bri | Process of beneficiation |
JPS4918330B1 (en) | 1969-02-08 | 1974-05-09 | ||
GB1282506A (en) | 1969-07-31 | 1972-07-19 | British Titan Ltd | A process for the removal of iron in the beneficiation of an iron-containing titaniferous material |
GB1282504A (en) | 1969-07-31 | 1972-07-19 | British Titan Ltd | Purification process for an iron-containing titaniferous material |
BE754202A (en) | 1969-07-31 | 1970-12-31 | Titangesellschaft Mbg | PROCESS FOR EXTRACTING IRON FROM TITANIUM ORE |
US3877929A (en) | 1969-07-31 | 1975-04-15 | Jack Whitehead | Process for reducing iron content of titaniferous material |
GB1282507A (en) | 1969-07-31 | 1972-07-19 | British Titan Ltd | Heat treatment of beneficiated titaniferous material |
GB1282324A (en) | 1969-07-31 | 1972-07-19 | British Titan Ltd | Process for the benification of iron-containing titaniferous materials |
GB1282505A (en) | 1969-07-31 | 1972-07-19 | British Titan Ltd | Beneficiation process for iron-containing titaniferous materials |
CA923711A (en) | 1969-09-12 | 1973-04-03 | Ishihara Sangyo Kaisha | Titanium dioxide concentrate and its manufacturing process |
DE2004878C3 (en) | 1969-10-15 | 1975-09-18 | Benilite Corp. Of America, New York, N.Y. (V.St.A.) | Process for enriching the titanium oxide content in titanium ores |
US3825419A (en) | 1969-10-15 | 1974-07-23 | Benilite Corp | Beneficiation of titaniferous ores |
BE759753A (en) | 1969-12-02 | 1971-06-02 | Bayer Ag | PROCESS FOR PREPARING TITANIUM DIOXIDE CONCENTRATES FROM ILMENITE |
DE2024907C3 (en) | 1970-05-22 | 1978-07-06 | Bayer Ag, 5090 Leverkusen | Process for the production of titanium dioxide concentrates from materials containing ilmenite |
US3897537A (en) | 1971-04-05 | 1975-07-29 | Laporte Industries Ltd | Beneficiation of ilmenite ores |
GB1392441A (en) | 1971-04-05 | 1975-04-30 | Laporte Industries Ltd | Beneficiation of ilmenite ores |
US3660029A (en) | 1971-04-09 | 1972-05-02 | Edith W Carpenter | Process for beneficiating ilmenite |
US3743996A (en) * | 1971-10-21 | 1973-07-03 | Gen Electric | Protective pads for electrical devices |
GB1431552A (en) | 1972-01-07 | 1976-04-07 | Laporte Industries Ltd | Beneficiation of weathered ilmenite ore materials |
GB1431551A (en) | 1972-01-07 | 1976-04-07 | Laporte Industries Ltd | Beneficiation of weathered ilmenite ore materials |
US3875286A (en) | 1972-02-14 | 1975-04-01 | Laporte Industries Ltd | Beneficiation of ilmenite ores |
DE2234843A1 (en) | 1972-07-15 | 1974-01-31 | Bayer Ag | PROCESS FOR THE MANUFACTURING OF TITANIUM DIOXIDE CONCENTRATES |
DE2402464A1 (en) | 1973-01-25 | 1974-11-14 | Commw Scient Ind Res Org | PROCESS FOR REFINING ILMENIT |
US4038363A (en) | 1975-10-21 | 1977-07-26 | Quebec Iron & Titanium Corporation-Fer Et Titane Due Quebec, Inc. | Upgrading sorelslag for production of synthetic rutile |
US4019898A (en) | 1976-04-30 | 1977-04-26 | Benilite Corporation Of America | Beneficiation of ilmenite ore |
US4097574A (en) | 1976-06-16 | 1978-06-27 | United States Steel Corporation | Process for producing a synthetic rutile from ilmentite |
DE2630196A1 (en) | 1976-07-05 | 1978-01-19 | Bayer Ag | METHOD FOR PRODUCING SULFURIC ACID FROM WASTE ACID AND IRON SULFATE |
US4089675A (en) | 1976-10-05 | 1978-05-16 | American Cyanamid Company | Combination beneficiation ilmenite digestion liquor reduction process |
US4120694A (en) | 1977-09-06 | 1978-10-17 | The United States Of America As Represented By The Secretary Of The Interior | Process for purifying a titanium-bearing material and upgrading ilmenite to synthetic rutile with sulfur trioxide |
US4199552A (en) | 1978-05-26 | 1980-04-22 | Kerr-Mcgee Corporation | Process for the production of synthetic rutile |
US4288418A (en) * | 1979-08-10 | 1981-09-08 | Nl Industries, Inc. | Process for manufacturing titanium dioxide |
US4272343A (en) | 1980-01-09 | 1981-06-09 | Kerr-Mcgee Corporation | Process for the electrolytic reductive leaching of ilmenite ore |
US4321236A (en) | 1981-02-05 | 1982-03-23 | Kerr-Mcgee Chemical Corporation | Process for beneficiating titaniferous materials |
US4562048A (en) | 1984-04-30 | 1985-12-31 | Kerr-Mcgee Chemical Corporation | Process for the treatment of metal-bearing ores |
BR8701481A (en) | 1986-04-03 | 1988-01-19 | Du Pont | PROCESS FOR PURIFICATION OF TIO2 ORE AND TIO2 PIGMENT OBTAINED BY THE PROCESS |
DE3635010A1 (en) | 1986-10-10 | 1988-04-14 | Gock Eberhard Priv Doz Prof Dr | Production of synthetic anatase from ilmenites using dilute acid |
EP0265551B1 (en) | 1986-10-31 | 1990-02-21 | KRONOS TITAN-Gesellschaft mbH | Process for the preparation of large scrubbing aggregates of titanium dioxide particles by the vapour phase oxidation of titanium tetrachloride, and its use in the prevention of scale formation in the same process |
DE3843846C1 (en) | 1988-12-24 | 1990-04-12 | Bayer Ag, 5090 Leverkusen, De | |
MY106846A (en) * | 1989-09-12 | 1995-08-30 | Ishihara Sangyo Kaisha | Process for producing titanium oxide concentrates. |
JPH06501741A (en) | 1990-03-02 | 1994-02-24 | ウィメラ インダストリアル ミネラルズ プロプライアタリー リミティド | Production of synthetic rutile |
US5181956A (en) | 1990-03-08 | 1993-01-26 | E. I. Du Pont De Nemours And Company | Method for purifying TiO2 ore |
JP2968877B2 (en) | 1991-11-08 | 1999-11-02 | 日鉄鉱業株式会社 | Method for recovering sulfuric acid from waste sulfuric acid containing metal sulfate |
WO1993018192A1 (en) | 1992-03-09 | 1993-09-16 | Pivot Mining Nl | Continuous leaching of treated titaniferous ores with alcohol solutions |
WO1993018191A1 (en) | 1992-03-09 | 1993-09-16 | Pivot Mining Nl | Continuous leaching of treated titaniferous ores with inter-stage evaporation |
US5266108A (en) | 1992-04-22 | 1993-11-30 | E. I. Du Pont De Nemours And Company | Using compacted titanium dioxide pigment particles in the cooling section of the chloride process for making TiO2 |
CZ22695A3 (en) | 1992-07-31 | 1996-01-17 | Rgc Mineral Sands Ltd | Process of treating titanium-containing materials |
US5910621A (en) | 1992-07-31 | 1999-06-08 | Rgc Mineral Sands | Treatment of titaniferous materials |
US5378438A (en) | 1992-11-30 | 1995-01-03 | E. I. Du Pont De Nemours And Company | Benefication of titaniferous ores |
DE69415566T2 (en) | 1993-02-23 | 1999-07-15 | Boc Gases Australia Ltd | Process for the production of synthetic rutile |
EP0741802A4 (en) | 1994-03-08 | 1997-05-21 | Rgc Mineral Sands Ltd | Leaching of titaniferous materials |
GB9607743D0 (en) * | 1996-04-13 | 1996-06-19 | Tioxide Group Services Ltd | Production of titanium oxide |
CA2182123C (en) | 1996-07-26 | 1999-10-05 | Graham F. Balderson | Method for the production of synthetic rutile |
US6471743B1 (en) | 1999-02-19 | 2002-10-29 | Mbx Systems, Inc. | Methods for leaching of ores |
-
2002
- 2002-04-19 US US10/126,241 patent/US7008602B2/en not_active Expired - Lifetime
-
2003
- 2003-04-15 BR BRPI0309330A patent/BRPI0309330B1/en not_active IP Right Cessation
- 2003-04-15 AU AU2003239166A patent/AU2003239166B2/en not_active Ceased
- 2003-04-15 WO PCT/US2003/012656 patent/WO2003089674A2/en not_active Application Discontinuation
- 2003-04-15 AT AT03733883T patent/ATE435309T1/en not_active IP Right Cessation
- 2003-04-15 EP EP03733883A patent/EP1499752B1/en not_active Expired - Lifetime
- 2003-04-15 CA CA2480865A patent/CA2480865C/en not_active Expired - Lifetime
- 2003-04-15 DE DE60328178T patent/DE60328178D1/en not_active Expired - Lifetime
-
2004
- 2004-10-21 NO NO20044509A patent/NO20044509L/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
DE60328178D1 (en) | 2009-08-13 |
US20030198591A1 (en) | 2003-10-23 |
ATE435309T1 (en) | 2009-07-15 |
WO2003089674A2 (en) | 2003-10-30 |
NO20044509L (en) | 2004-11-05 |
EP1499752A2 (en) | 2005-01-26 |
WO2003089674A3 (en) | 2003-12-24 |
BRPI0309330B1 (en) | 2016-07-26 |
AU2003239166B2 (en) | 2008-08-14 |
US7008602B2 (en) | 2006-03-07 |
BR0309330A (en) | 2005-02-01 |
CA2480865C (en) | 2011-07-26 |
AU2003239166A1 (en) | 2003-11-03 |
EP1499752B1 (en) | 2009-07-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2480865A1 (en) | Acid beneficiation of ore | |
US7625536B2 (en) | Titaniferous ore beneficiation | |
Liu et al. | Combined production of synthetic rutile in the sulfate TiO2 process | |
US4089675A (en) | Combination beneficiation ilmenite digestion liquor reduction process | |
CN108675344A (en) | A kind of sulfate process titanium dioxide acidolysis production technology | |
WO2019137542A1 (en) | Method for selectively leaching and upgrading high-titanium slag | |
EP1957408B1 (en) | A process for the production of titanium products | |
JPH09504828A (en) | Improving the quality of titanium-containing raw materials | |
US2774650A (en) | Method for decomposition of titaniferous ores | |
US3416885A (en) | Process for producing a titanium sulfate solution and a tio2 concentrate from a titaniferous ore | |
EP0801030A2 (en) | Production of titanium oxide | |
EP0719346A1 (en) | Ilmenite processing using cold milling | |
KR940006034B1 (en) | Method of producing titanium dioxide | |
JP2569197B2 (en) | Recycling method of low concentration waste sulfuric acid | |
CA1157230A (en) | Process for manufacturing titanium compounds | |
JPS61209916A (en) | Preparation of synthetic rutile | |
CN107459058B (en) | Method for producing synthetic rutile by using titanium concentrate | |
SU1444340A1 (en) | Method of producing titanium dioxide pigment | |
CN117568628A (en) | Method for cleanly extracting and utilizing valuable elements in perovskite | |
JPH09124318A (en) | Method for removing radioactive nuclide from titanium-containing ore | |
RU1816739C (en) | Method of reprocessing technical melted vanadium pentoxide | |
US1852510A (en) | Process of treating titaniferous materials with acid | |
AU7689294A (en) | Ilmenite processing using cold milling | |
EP4046964A1 (en) | Method for the production of a titanium-containing feedstock for the chloride process | |
FI71544C (en) | Process for the preparation of titanium sulfate solution. |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKEX | Expiry |
Effective date: 20230417 |