GB916250A - Manufacture of titanium dioxide pigment - Google Patents

Manufacture of titanium dioxide pigment

Info

Publication number
GB916250A
GB916250A GB3942159A GB3942159A GB916250A GB 916250 A GB916250 A GB 916250A GB 3942159 A GB3942159 A GB 3942159A GB 3942159 A GB3942159 A GB 3942159A GB 916250 A GB916250 A GB 916250A
Authority
GB
United Kingdom
Prior art keywords
gas
gases
oxygen
mixture
fed
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
GB3942159A
Inventor
Earl William Nelson
James Ellison Bondurant
John Peter Wikswo
Guy Christopher Marcot
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.)
Wyeth Holdings LLC
Original Assignee
American Cyanamid 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 American Cyanamid Co filed Critical American Cyanamid Co
Priority to GB3942159A priority Critical patent/GB916250A/en
Publication of GB916250A publication Critical patent/GB916250A/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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/62Submicrometer sized, i.e. from 0.1-1 micrometer
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/60Optical properties, e.g. expressed in CIELAB-values

Abstract

<PICT:0916250/III/1> <PICT:0916250/III/2> Titanium dioxide is formed by supplying a preformed homogeneous mixture of titanium tetrachloride and oxygen at a temperature below 700 DEG C. to a combustion space through which it flows substantially uniformly so that the average speed of the combustion mixture is between two thirds and four thirds of its axial speed. The walls of the reaction chamber are preferably formed of porous refractory and an inert gas or chlorinating is passed transversely therethrough to prevent adhesion of titanium dioxide particles. According to a modification, the preformed homogeneous mixture of titanium tetrachloride and oxygen is fed into a reaction chamber directly against an opposing column of gas, which may be inert or combustible or the same, and the combined stream of gas is withdrawn at their junction. As shown in Fig. 1, a reaction vessel is provided with porous walls 5 through which a purge gas can be passed from line 10. Above is a smaller nucleating section provided with porous walls 3 through which a purge gas is fed through line 9. A reacting gas mixture is fed through a line 12 into a turbulence suppressor 13 formed of nesting aluminium tubes. The nucleating zone and the reaction zone are joined by a porous disc 4 which is flushed on its inside by purging gas. Suitable purge gases are ammonia, nitrogen oxide, water vapour or gases forming water vapour on combustion, such as ethyl acetate, butane, butanol, diethyl ether or diethyl ketone or preferably carbon monoxide. Purge gas, admitted through the pipe 10 to the lower reaction zone, may be titanium tetrachloride, (liquid or gaseous), chlorine, carbon monoxide, carbon dioxide or the noble gases. A sight port 21 is provided, alternatively an apparatus as shown in Fig. 3 may be employed where two opposing tubes 123 and 124 are supplied, by tangentially arranged pipes 105 and 106, with fuel or reactant gases which move with a slow rotary motion. Screens 111 to 122 ensure a uniform gas velocity. The gases meet in a cooled reaction space bounded by a jacket 129. The gases fed to the opposing tubes 123 and 124 may be the same, i.e. a mixture of titanium tetrachloride and oxygen, or the opposing stream may be a mixture of chlorine and carbon dioxide, carbon monoxide and oxygen, or an inert gas such as nitrogen. Fuel gases referred to include hydrogen, volatile hydrocarbons, esters, ketones and alcohols, but carbon monoxide is preferred. The necessary oxygen for combustion is also supplied and it is suggested that ozone be included. Rutile production, favoured by a high flame temperature, may be promoted by the addition of aluminium chloride, and other metal chlorides such as silicon, vanadium, nickel, zinc, antimony or zirconium chlorides; lower titanium chlorides may be added. Reference has been directed by the Comptroller to Specification 764,084.
GB3942159A 1959-11-20 1959-11-20 Manufacture of titanium dioxide pigment Expired GB916250A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB3942159A GB916250A (en) 1959-11-20 1959-11-20 Manufacture of titanium dioxide pigment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB3942159A GB916250A (en) 1959-11-20 1959-11-20 Manufacture of titanium dioxide pigment

Publications (1)

Publication Number Publication Date
GB916250A true GB916250A (en) 1963-01-23

Family

ID=10409451

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3942159A Expired GB916250A (en) 1959-11-20 1959-11-20 Manufacture of titanium dioxide pigment

Country Status (1)

Country Link
GB (1) GB916250A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996006803A1 (en) * 1994-08-31 1996-03-07 University Of Cincinnati Process for producing ceramic powders, especially titanium dioxide useful as a photocatalyst
WO2013132225A1 (en) 2012-03-08 2013-09-12 Reckitt & Colman (Overseas) Limited Polymer treatment method
WO2013132223A1 (en) 2012-03-08 2013-09-12 Reckitt & Colman (Overseas) Limited Cleaning method with polymeric particles
WO2013150265A1 (en) 2012-04-05 2013-10-10 Reckitt & Colman (Overseas) Limited Detergent dispensing cartridge
US11926532B2 (en) 2021-01-11 2024-03-12 University Of Kansas Processes for the production of metal oxides

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996006803A1 (en) * 1994-08-31 1996-03-07 University Of Cincinnati Process for producing ceramic powders, especially titanium dioxide useful as a photocatalyst
US5861132A (en) * 1994-08-31 1999-01-19 University Of Cincinnati Vapor phase flame process for making ceramic particles using a corona discharge electric field
WO2013132225A1 (en) 2012-03-08 2013-09-12 Reckitt & Colman (Overseas) Limited Polymer treatment method
WO2013132223A1 (en) 2012-03-08 2013-09-12 Reckitt & Colman (Overseas) Limited Cleaning method with polymeric particles
WO2013150265A1 (en) 2012-04-05 2013-10-10 Reckitt & Colman (Overseas) Limited Detergent dispensing cartridge
US11926532B2 (en) 2021-01-11 2024-03-12 University Of Kansas Processes for the production of metal oxides

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