GB876672A - Improvements in or relating to the production of pigmentary titanium dioxide - Google Patents
Improvements in or relating to the production of pigmentary titanium dioxideInfo
- Publication number
- GB876672A GB876672A GB39559/57A GB3955957A GB876672A GB 876672 A GB876672 A GB 876672A GB 39559/57 A GB39559/57 A GB 39559/57A GB 3955957 A GB3955957 A GB 3955957A GB 876672 A GB876672 A GB 876672A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reaction
- oxygen
- per million
- titanium dioxide
- preheated
- 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
- 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
- C01G23/07—Producing by vapour phase processes, e.g. halide oxidation
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Pigmentary titanium dioxide is prepared by decomposing titanium tetrachloride with an oxygen containing gas in the vapour phase at an elevated temperature in the presence of from 0.01 to 10,000 parts by weight per million of alkali metal, especially potassium, based on the titanium dioxide being produced. Reaction temperatures may be from 800-1400 DEG C., and the preheated oxidizing gas may contain from 10-100% oxygen by volume. The reaction may be effected in the presence of small amounts of water vapour or aluminium. The alkali metal may be supplied in the elemental state or preferably as a water soluble inorganic or organic compound such as the nitrate, chloride or sulphate, halide, phosphate, alcoholate, acetate, benzoate, hydroxide or oxide, supplied as an aqueous solution charged to the reaction zone via a separate inlet. The reaction may be effected in the reactor described in Specification 757,703 where one reactant is discharged as a thin sheeted stream directly into the other reactant in the direction angular to the axis of flow thereof. The oxygen containing gas may be air, oxygen or mixtures thereof; inert gases such as nitrogen or carbon dioxide may be present. Thus for example, preheated vaporized anhydrous titanium tetrachloride containing 1% of aluminium chloride may be charged to a reaction zone maintained at 900-1400 DEG C., together with preheated air containing 50 to 100,000 parts per million of water vapour and 0.1 to 400 parts per million of potassium and in the form of an aqueous soluton of potassium chloride, nitrate or sulphate. The resulting gaseous suspension at 1150 DEG C. is quenched below 600 DEG C. for example by the method disclosed in Specification 776,419, and the resulting pigment subjected to mild calcination in air at 600 to 900 DEG C. to remove residual chlorine. The pigment may then be dry milled or disintegrated. Specification 707,560 also is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US876672XA | 1956-12-20 | 1956-12-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB876672A true GB876672A (en) | 1961-09-06 |
Family
ID=22206536
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB39559/57A Expired GB876672A (en) | 1956-12-20 | 1957-12-19 | Improvements in or relating to the production of pigmentary titanium dioxide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB876672A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5201949A (en) * | 1986-04-18 | 1993-04-13 | E. I. Du Pont De Nemours And Company | TiO2 manufacturing process |
US5536487A (en) * | 1995-02-27 | 1996-07-16 | Kronos, Inc. | Process for the use of rutile promoter and control additives in the manufacture of titanium dioxide by the chloride process |
-
1957
- 1957-12-19 GB GB39559/57A patent/GB876672A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5201949A (en) * | 1986-04-18 | 1993-04-13 | E. I. Du Pont De Nemours And Company | TiO2 manufacturing process |
US5536487A (en) * | 1995-02-27 | 1996-07-16 | Kronos, Inc. | Process for the use of rutile promoter and control additives in the manufacture of titanium dioxide by the chloride process |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
SE9002802L (en) | PROCEDURE FOR PREPARATION OF CHLORIDE Dioxide | |
US5201949A (en) | TiO2 manufacturing process | |
NO913343L (en) | PROCEDURE FOR THE PREPARATION OF CHLORODIOXIDE. | |
US4276274A (en) | Process for the production of finely divided oxides of metals or silicon | |
GB1031647A (en) | Method of making tio pigment | |
ES423320A1 (en) | Production of metal fluorides from fluosilicic acid | |
IE22729B1 (en) | Improvements in or relating to the thermal decomposition of certain chlorides and sulphates | |
US4113590A (en) | Photoreduction of nitrogen | |
GB876672A (en) | Improvements in or relating to the production of pigmentary titanium dioxide | |
GB1084096A (en) | ||
GB1038164A (en) | Process of producing sulphuric acid | |
GB1353361A (en) | Production of chromium-iii- oxide of low sulphur content | |
US2240344A (en) | Preparation of hypochlorous acid | |
US3329483A (en) | Fluidized bed process for producing pigmentary titanium dioxide with reduced accretion therein | |
US4355008A (en) | Chlorination process | |
GB707560A (en) | Improvements in and relating to the manufacture of pigmentary titanium dioxide | |
GB764084A (en) | Improvements in or relating to the production of metal oxides | |
GB867479A (en) | Process for improving titanium dioxide pigments | |
US2398891A (en) | Recovery of chlorine from magnesium chloride electrolysis | |
US3006726A (en) | Process for upgrading crude alkali metal sulfates | |
GB703954A (en) | A new or improved method for the preparation of alkyl titanates | |
GB760644A (en) | Improvements in method of preparing titanium dioxide | |
GB748610A (en) | Improvements in or relating to a method for treating alkali metal chromates | |
GB1087697A (en) | Production of titanium dioxide pigments | |
GB878101A (en) | Process for the manufacture of titanium disulphide |