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ES2035498T3 - Procedimiento y dispositivo para la preparacion de dioxido de titanio. - Google Patents

Procedimiento y dispositivo para la preparacion de dioxido de titanio.

Info

Publication number
ES2035498T3
ES2035498T3 ES198989120996T ES89120996T ES2035498T3 ES 2035498 T3 ES2035498 T3 ES 2035498T3 ES 198989120996 T ES198989120996 T ES 198989120996T ES 89120996 T ES89120996 T ES 89120996T ES 2035498 T3 ES2035498 T3 ES 2035498T3
Authority
ES
Spain
Prior art keywords
heated
reaction chamber
oxygen
ticl
procedure
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 - Lifetime
Application number
ES198989120996T
Other languages
English (en)
Inventor
Achim Dipl.-Ing. Hartmann
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.)
Kronos Titan GmbH
Original Assignee
Kronos Titan GmbH
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 Kronos Titan GmbH filed Critical Kronos Titan GmbH
Application granted granted Critical
Publication of ES2035498T3 publication Critical patent/ES2035498T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • B01J12/02—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor for obtaining at least one reaction product which, at normal temperature, is in the solid state
    • 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

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)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Compositions Of Oxide Ceramics (AREA)

Abstract

EL OBJETIVO DE LA INVENCION LO CONFORMAN UN PROCEDIMIENTO PARA LA PRODUCCION DE OXIDO DE TITANIO MEDIANTE REACCION CON TICL SUB 4 EN FORMA DE VAPOR CON OXIGENO BAJO PRESION DE 2,4 A 3,4 BAR Y UN DISPOSITIVO CORRESPONDIENTE. EL OXIGENO NECESARIO SE CALIENTA INDIRECTAMENTE ENTRE 850 Y 1000 GRADOS C DE TEMPERATURA. LA CAMARA DE REACCION EN QUE SE CALIENTA ESTA CERRADA POR UN LADO Y ACONDICIONADA EN SU INTERIOR PARA UN FLUJO FAVORABLE DE GASES Y RESISTENTE EN PARTE AL FUEGO QUE SE CALIENTA A TRAVES DEL CONTACTO DIRECTO CON GASES MUY CALIENTES PROVENIENTES DE UN FUEGO AUXILIAR. SE CALIENTA HASTA TAL GRADO COMO SEA NECESARIO PARA UNA TRANSFORMACION ESPONTANEA CON EL TICL SUB 4 INTRODUCIDO, CORRIENTE ABAJO, EN LA CAMARA DE REACCION. AL MISMO TIEMPO, EL OXIGENO CALENTADO INDIRECTAMENTE SE DIFUNDE INMEDIATAMENTE EN EL LADO FRONTAL DE LA CAMARA DE REACCION A TRAVES DE UNA TOBERA ANULAR EN CUYO REVESTIMIENTO INTERIOR SE DISTRIBUYE HOMOGENEAMENTE EN TODO SU PERIMETRO EL OXIGENO QUE SE INTRODUCIRA EN LACAMARA. EL FLUJO DEL OXIGENO SE REGULA DE MODO QUE, EN LA TOBERA ANULAR, EL NUMERO REYNOLD OSCILA ENTRE 15000 Y 20000 Y LA RELACION DE DICHO NUMERO AL DIAMETRO INTERIOR DE LA CAMARA DE REACCION, MEDIDA EN MILIMETROS EN LA TOBERA ANULAR, VARIA ENTRE 25 Y 50. SE OBTIENEN TIEMPOS DE FUNCIONAMIENTO PERMANENTE MAS LARGOS.
ES198989120996T 1989-11-13 1989-11-13 Procedimiento y dispositivo para la preparacion de dioxido de titanio. Expired - Lifetime ES2035498T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP89120996A EP0427878B1 (de) 1989-11-13 1989-11-13 Verfahren und Vorrichtung zur Herstellung von Titandioxid

Publications (1)

Publication Number Publication Date
ES2035498T3 true ES2035498T3 (es) 1993-04-16

Family

ID=8202119

Family Applications (1)

Application Number Title Priority Date Filing Date
ES198989120996T Expired - Lifetime ES2035498T3 (es) 1989-11-13 1989-11-13 Procedimiento y dispositivo para la preparacion de dioxido de titanio.

Country Status (6)

Country Link
US (1) US5196181A (es)
EP (1) EP0427878B1 (es)
JP (1) JPH03170331A (es)
CA (1) CA2029360C (es)
DE (1) DE58902214D1 (es)
ES (1) ES2035498T3 (es)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5698177A (en) * 1994-08-31 1997-12-16 University Of Cincinnati Process for producing ceramic powders, especially titanium dioxide useful as a photocatalyst
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
DE19514663A1 (de) * 1995-04-20 1996-10-24 Kronos Titan Gmbh Metallchloridgenerator
US5840112A (en) * 1996-07-25 1998-11-24 Kerr Mcgee Chemical Corporation Method and apparatus for producing titanium dioxide
US6350427B1 (en) * 1999-07-27 2002-02-26 Kerr-Mcgee Chemical Llc Processes for reacting gaseous reactants containing solid particles
KR100376247B1 (ko) * 2000-04-07 2003-03-15 삼화페인트공업주식회사 화염을 이용한 기상산화반응에 의한 나노사이즈이산화티타늄 초미분체 제조 방법
DE10210189B4 (de) * 2002-03-07 2013-09-19 Kronos International, Inc. Verfahren zum Beeinflussen der Pigmenteigenschaften von Titandioxid durch Salzzugabe in der Brennkammer
US7416697B2 (en) 2002-06-14 2008-08-26 General Electric Company Method for preparing a metallic article having an other additive constituent, without any melting
US7001443B2 (en) * 2002-12-23 2006-02-21 General Electric Company Method for producing a metallic alloy by the oxidation and chemical reduction of gaseous non-oxide precursor compounds
US20050220702A1 (en) * 2004-04-02 2005-10-06 Martin Robert O High flow rate gaseous reactant supply
US7531021B2 (en) 2004-11-12 2009-05-12 General Electric Company Article having a dispersion of ultrafine titanium boride particles in a titanium-base matrix
WO2006126987A1 (en) * 2005-05-20 2006-11-30 Tronox Llc Fluid mixing apparatus and method
US20080069764A1 (en) 2006-09-18 2008-03-20 Tronox Llc Process for making pigmentary titanium dioxide
WO2008154275A2 (en) * 2007-06-06 2008-12-18 North Carolina State University Process for combustion of high viscosity low heating value liquid fuels
DE102007049297A1 (de) 2007-10-12 2009-04-23 Kronos International, Inc. Verfahren zur Herstellung von Titandioxid
DE102009009780A1 (de) 2009-02-20 2010-08-26 Kronos International, Inc. Mehrstufiges Verfahren zur Herstellung von Titandioxid
CN107128972B (zh) * 2017-06-30 2018-12-28 攀钢集团研究院有限公司 一种用于钛白粉的生产系统
CN110817953B (zh) * 2019-10-29 2022-02-18 山东鲁北企业集团总公司 一种氧化反应器的防疤和除疤系统及其方法

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2760846A (en) * 1954-06-18 1956-08-28 Laporte Titanium Ltd Process for the manufacture of titanium dioxide
GB1111411A (en) * 1964-06-03 1968-04-24 Laporte Titanium Ltd Improvements in and relating to the manufacture of titanium dioxide
GB1097762A (en) * 1963-12-12 1968-01-03 British Titan Products Device for use in oxidation of metal halides
GB1170924A (en) * 1965-10-19 1969-11-19 Laporte Titanium Ltd Improvements in and relating to the Manufacture of Titanium Dioxide.
US3449076A (en) * 1966-10-10 1969-06-10 Du Pont Preheating oxidizing gas reactant in tio2 pigment manufacture
DE1592529B2 (de) * 1967-06-03 1971-09-02 Titangesellschaft mbH, 5090 Leverku sen Verfahren zur herstellung eines rutil pigmentes durch umsetzung von titantetrachlorid mit sauerstoff in einem heissen gasgemisch
US3493342A (en) * 1968-02-16 1970-02-03 Cabot Corp Collection of pyrogenic titanium dioxide pigments
US3505091A (en) * 1968-07-29 1970-04-07 Du Pont Production of titanium dioxide pigments
CH527890A (it) * 1969-07-31 1972-09-15 Sir Soc Italiana Resine Spa Procedimento per la preparazione di titanio biossido
US4170630A (en) * 1969-10-31 1979-10-09 American Cyanamid Company Method for producing particulate solids in a turbulent wake burner
BE792503A (fr) * 1971-12-10 1973-06-08 Montedison Spa Procede de preparation d'un bioxyde de titane d'une taille de particules controlee
CA1043982A (en) * 1974-11-25 1978-12-12 Kronos Titan G.M.B.H. Process for the manufacture of fine particle size metal oxides
US4214913A (en) * 1979-03-05 1980-07-29 E. I. Du Pont De Nemours And Company Process for producing rutile TiO2

Also Published As

Publication number Publication date
CA2029360C (en) 1998-07-14
CA2029360A1 (en) 1991-05-14
EP0427878B1 (de) 1992-09-02
DE58902214D1 (de) 1992-10-08
US5196181A (en) 1993-03-23
EP0427878A1 (de) 1991-05-22
JPH03170331A (ja) 1991-07-23

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