GB760644A - Improvements in method of preparing titanium dioxide - Google Patents

Improvements in method of preparing titanium dioxide

Info

Publication number
GB760644A
GB760644A GB22683/54A GB2268354A GB760644A GB 760644 A GB760644 A GB 760644A GB 22683/54 A GB22683/54 A GB 22683/54A GB 2268354 A GB2268354 A GB 2268354A GB 760644 A GB760644 A GB 760644A
Authority
GB
United Kingdom
Prior art keywords
tetrachloride
employed
titanium
subchloride
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
GB22683/54A
Inventor
Holger Heinrich Schaumann
Ignace Joseph Krchma
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
Priority to GB22683/54A priority Critical patent/GB760644A/en
Publication of GB760644A publication Critical patent/GB760644A/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
    • 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

In the production of titanium dioxide by vapour phase oxidation of the tetrachloride at 800 to 1,350 DEG C., 0.1 to 10 per cent of a subchloride of titanium is added to the tetrachloride as a nucleating agent. The subchloride is preferably formed by passing a portion of the tetrachloride feed over a reducing agent such as a metal or a hydride, or by contact with hydrogen, and the resulting vaporous or finely divided solid lower chloride/tetrachloride mixture is reunited with the main tetrachloride stream. The temperature of the lower chloride generator is preferably 136 to 400 DEG C. The halide oxidation may be effected with air or oxygen, mixed, if desired, with inert gases and 0.05 to 5 per cent of water vapour, the oxygen preferably being present in excess. Atmospheric, lower or higher pressures may be employed and the reactant retention time may be from 0.01 to 5 seconds. The reaction products are preferably quickly cooled and subsequently the titanium dioxide may be calcined and ground. According to a typical example, a titanium tetrachloride vapour stream, preheated in a nickel heat exchanger to 400 DEG C., was split and a minor portion contacted with pulverized titanium metal sponge to generate subchloride, after which this side stream rejoined the main stream and was fed to an elongated reactor. Air, preheated to 1100 DEG C. was injected through a separate inlet. The dioxide reaction product was calcined and ground in the usual manner. Another example relates to tetrachloride, preheated to 200 DEG C. and a diverted portion reacted with molten sodium to generate the lower chlorides. In this case oxygen preheated to 850 DEG C. was employed as oxidant. If metals are employed as reducing agents in the subchloride generator, their chlorides may be carried into the main reactor. Thus tin or aluminium may be employed and their chlorides oxidized with the titanium tetrachloride. Alternatively, aluminium chloride may be added in small amounts as in Specification 707,560. Other nucleating agents such as water vapour, nitrogen oxides or normally unstable metal subhalides may also be employed.
GB22683/54A 1954-08-04 1954-08-04 Improvements in method of preparing titanium dioxide Expired GB760644A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB22683/54A GB760644A (en) 1954-08-04 1954-08-04 Improvements in method of preparing titanium dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB22683/54A GB760644A (en) 1954-08-04 1954-08-04 Improvements in method of preparing titanium dioxide

Publications (1)

Publication Number Publication Date
GB760644A true GB760644A (en) 1956-11-07

Family

ID=10183420

Family Applications (1)

Application Number Title Priority Date Filing Date
GB22683/54A Expired GB760644A (en) 1954-08-04 1954-08-04 Improvements in method of preparing titanium dioxide

Country Status (1)

Country Link
GB (1) GB760644A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011059938A1 (en) * 2009-11-10 2011-05-19 E. I. Du Pont De Nemours And Company Process for in-situ formation of chlorides of silicon and aluminum in the preparation of titanium dioxide
WO2012039731A1 (en) * 2010-09-21 2012-03-29 E. I. Du Pont De Nemours And Company Process for in-situ formation of chlorides in the preparation of titanium dioxide
CN102686516A (en) * 2010-09-21 2012-09-19 纳幕尔杜邦公司 Tungsten containing inorganic particles with improved photostability
US8734755B2 (en) 2010-02-22 2014-05-27 E I Du Pont De Nemours And Company Process for in-situ formation of chlorides of silicon, aluminum and titanium in the preparation of titanium dioxide

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011059938A1 (en) * 2009-11-10 2011-05-19 E. I. Du Pont De Nemours And Company Process for in-situ formation of chlorides of silicon and aluminum in the preparation of titanium dioxide
US8741257B2 (en) 2009-11-10 2014-06-03 E I Du Pont De Nemours And Company Process for in-situ formation of chlorides of silicon and aluminum in the preparation of titanium dioxide
US8734755B2 (en) 2010-02-22 2014-05-27 E I Du Pont De Nemours And Company Process for in-situ formation of chlorides of silicon, aluminum and titanium in the preparation of titanium dioxide
WO2012039731A1 (en) * 2010-09-21 2012-03-29 E. I. Du Pont De Nemours And Company Process for in-situ formation of chlorides in the preparation of titanium dioxide
CN102686516A (en) * 2010-09-21 2012-09-19 纳幕尔杜邦公司 Tungsten containing inorganic particles with improved photostability
US8734756B2 (en) 2010-09-21 2014-05-27 E I Du Pont De Nemours And Company Process for in-situ formation of chlorides in the preparation of titanium dioxide
US9260319B2 (en) 2010-09-21 2016-02-16 The Chemours Company Tt, Llc Process for in-situ formation of chlorides in the preparation of titanium dioxide

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