GB1191767A - Method of Chlorinating Titanium-Bearing Materials - Google Patents

Method of Chlorinating Titanium-Bearing Materials

Info

Publication number
GB1191767A
GB1191767A GB55506/68A GB5550668A GB1191767A GB 1191767 A GB1191767 A GB 1191767A GB 55506/68 A GB55506/68 A GB 55506/68A GB 5550668 A GB5550668 A GB 5550668A GB 1191767 A GB1191767 A GB 1191767A
Authority
GB
United Kingdom
Prior art keywords
titanium
source
rutile
reductant
amount
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
GB55506/68A
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.)
PPG Industries Inc
Original Assignee
PPG Industries Inc
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 PPG Industries Inc filed Critical PPG Industries Inc
Publication of GB1191767A publication Critical patent/GB1191767A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B34/00Obtaining refractory metals
    • C22B34/10Obtaining titanium, zirconium or hafnium
    • C22B34/12Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
    • C22B34/1218Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by dry processes
    • C22B34/1222Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by dry processes using a halogen containing agent

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Metallurgy (AREA)
  • Mechanical Engineering (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

1,191,767. Chlorinating titanium bearing materials. PPG INDUSTRIES Inc. 22 Nov., 1968 [7 Dec., 1967], No. 55506/68. Heading C1A. Titanium tetrachloride is prepared by chlorinating a titanium-bearing material in a fluidized bed, in the presence of a carbonaceous reductant and a metal source selected from magnesium, calcium, strontium, barium, cadmium and mixtures thereof. Amounts may be sufficient to increase the ratio of CO 2 to CO, both of which are produced during the reaction, but less than an agglutinating amount. Any fluidizable source of titanium is suitable for this process, especially a source containing in excess of 90% by weight of titanium dioxide. Rutile, especially Sierra Leone rutile, is particularly suitable for treatment. Particle size may be between 75 and 500 Á. The reductant may be coke, carbon monoxide, graphite, charcoal, carbon tetrachloride or phosgene. Carbon content may be 10-50% by weight of the total composition of the bed. The average particle size of the reductant may be between 100 and 900 Á. The temperature of the reaction is preferably above 500‹ C. The additives may be introduced as carbonates, sulphates, chlorides, oxides, phosphates, carbides or as the free metal. They may also be introduced in a second titanium-bearing material, provided that this material contains more of the additive than is present in the original titanium source. For example, Australian rutile may be added to Sierra-Leone rutile as a source of calcium and magnesium. The amount of additive may be between 0À001 and 0À35 weight per cent, based on the amount of titanium dioxide in the titanium-bearing material.
GB55506/68A 1967-12-07 1968-11-22 Method of Chlorinating Titanium-Bearing Materials Expired GB1191767A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US68867767A 1967-12-07 1967-12-07

Publications (1)

Publication Number Publication Date
GB1191767A true GB1191767A (en) 1970-05-13

Family

ID=24765346

Family Applications (1)

Application Number Title Priority Date Filing Date
GB55506/68A Expired GB1191767A (en) 1967-12-07 1968-11-22 Method of Chlorinating Titanium-Bearing Materials

Country Status (5)

Country Link
BE (1) BE725067A (en)
DE (1) DE1813082A1 (en)
FR (1) FR1591467A (en)
GB (1) GB1191767A (en)
NL (1) NL6816404A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111874943B (en) * 2020-06-22 2023-04-07 河南佰利联新材料有限公司 Control method for CO content in boiling chlorination reaction tail gas

Also Published As

Publication number Publication date
DE1813082A1 (en) 1969-06-19
FR1591467A (en) 1970-04-27
NL6816404A (en) 1969-06-10
BE725067A (en) 1969-06-06

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Legal Events

Date Code Title Description
PS Patent sealed
PLNP Patent lapsed through nonpayment of renewal fees