GB876672A - Improvements in or relating to the production of pigmentary titanium dioxide - Google Patents

Improvements in or relating to the production of pigmentary titanium dioxide

Info

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
Application number
GB39559/57A
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.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Publication of GB876672A publication Critical patent/GB876672A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G23/00Compounds of titanium
    • C01G23/04Oxides; Hydroxides
    • C01G23/047Titanium dioxide
    • C01G23/07Producing by vapour phase processes, e.g. halide oxidation
    • 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
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

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.
GB39559/57A 1956-12-20 1957-12-19 Improvements in or relating to the production of pigmentary titanium dioxide Expired GB876672A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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

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