GB970885A - Preparation of high purity titanium dioxide - Google Patents
Preparation of high purity titanium dioxideInfo
- Publication number
- GB970885A GB970885A GB302664A GB302664A GB970885A GB 970885 A GB970885 A GB 970885A GB 302664 A GB302664 A GB 302664A GB 302664 A GB302664 A GB 302664A GB 970885 A GB970885 A GB 970885A
- Authority
- GB
- United Kingdom
- Prior art keywords
- titanium
- alkyl
- acid
- orthophosphoric acid
- extracted
- 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G23/00—Compounds of titanium
- C01G23/001—Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Pigment grade titanium dioxide is prepared by treating a titaniferous material with sulphuric acid at 40-80 DEG C., leaching with water, selectively extracting titanium values with a liquid mono- or di-alkyl orthophosphoric acid, or contaminants with an alkyl phosphate or alkyl amine; recovering titanium as the hydrated oxide, and calcining at above 800 DEG C. At least one equivalent of acid, preferably 90% or stronger, per equivalent of metal is used, and the material may be pretreated with an inorganic base. Contaminants are extracted if a trialkyl phosphate having alkyl groups with 4-8 carbon atoms, e.g. tributylphosphate, or an alkylamine having alkyl groups with 6-12 carbon atoms, e.g. triisooctylamine, is used as extractant; titanium is then precipitated from the acid leachate by digestion at 80-100 DEG C., preferably with an inorganic base, to give the hydrated oxide. Alternatively, titanium may be extracted from the leach liquor using a mono- or di-alkyl orthophosphoric acid having alkyl groups with 4-18 carbon atoms, e.g. di-(2-ethyl hexyl)-orthophosphoric acid, monododecyl orthophosphoric acid, and monoheptadecyl orthophosphoric acid; and any iron also extracted may be removed by scrubbing with 3-12M. HCl. Titanium is then recovered by adding an aqueous solution of either (1) an alkali metal or ammonium hydroxide or carbonate, or a mixture of ammonium hydroxide and carbonate, to precipitate hydrated titanium oxide; or (2) hydrogen fluoride or an alkali metal or ammonium fluoride or bifluoride, to precipitate a titanium-ammonium double fluoride, which is converted into the hydrated oxide by reaction with ammonia. The organic extractant is preferably carried in a water-immiscible solvent, e.g. kerosenes, toluene, benzene and halogenated and other aromatics, in 0.3-3.5M concentration. The organic/aqueous phase ratio may be from 1/10 to 1/1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB302664A GB970885A (en) | 1962-02-02 | 1962-02-02 | Preparation of high purity titanium dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB302664A GB970885A (en) | 1962-02-02 | 1962-02-02 | Preparation of high purity titanium dioxide |
Publications (1)
Publication Number | Publication Date |
---|---|
GB970885A true GB970885A (en) | 1964-09-23 |
Family
ID=9750566
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB302664A Expired GB970885A (en) | 1962-02-02 | 1962-02-02 | Preparation of high purity titanium dioxide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB970885A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4082832A (en) * | 1975-05-06 | 1978-04-04 | Solex Research Corporation | Treatment of raw materials containing titanium |
US4269809A (en) * | 1979-12-19 | 1981-05-26 | Uop Inc. | Recovery in titanium metal values by solvent extraction |
US4499058A (en) * | 1982-03-19 | 1985-02-12 | Rhone-Poulenc S.A. | Liquid/liquid extraction of acidic aqueous streams comprising sulfate/titanium/iron values |
EP0298763A2 (en) * | 1987-07-08 | 1989-01-11 | Solex Research Corporation of Japan | Method for recovering titanium |
-
1962
- 1962-02-02 GB GB302664A patent/GB970885A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4082832A (en) * | 1975-05-06 | 1978-04-04 | Solex Research Corporation | Treatment of raw materials containing titanium |
US4269809A (en) * | 1979-12-19 | 1981-05-26 | Uop Inc. | Recovery in titanium metal values by solvent extraction |
US4499058A (en) * | 1982-03-19 | 1985-02-12 | Rhone-Poulenc S.A. | Liquid/liquid extraction of acidic aqueous streams comprising sulfate/titanium/iron values |
EP0298763A2 (en) * | 1987-07-08 | 1989-01-11 | Solex Research Corporation of Japan | Method for recovering titanium |
EP0298763A3 (en) * | 1987-07-08 | 1990-01-10 | Solex Research Corporation of Japan | Method for recovering titanium |
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