GB805730A - Process for the production of titanium - Google Patents

Process for the production of titanium

Info

Publication number
GB805730A
GB805730A GB17283/57A GB1728357A GB805730A GB 805730 A GB805730 A GB 805730A GB 17283/57 A GB17283/57 A GB 17283/57A GB 1728357 A GB1728357 A GB 1728357A GB 805730 A GB805730 A GB 805730A
Authority
GB
United Kingdom
Prior art keywords
titanium
sodium
halide
reactor
molten
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
GB17283/57A
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.)
Union Carbide Corp
Original Assignee
Union Carbide Corp
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 Union Carbide Corp filed Critical Union Carbide Corp
Publication of GB805730A publication Critical patent/GB805730A/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
    • C22B34/1263Obtaining 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 metallic titanium from titanium compounds, e.g. by reduction
    • C22B34/1268Obtaining 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 metallic titanium from titanium compounds, e.g. by reduction using alkali or alkaline-earth metals or amalgams
    • C22B34/1272Obtaining 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 metallic titanium from titanium compounds, e.g. by reduction using alkali or alkaline-earth metals or amalgams reduction of titanium halides, e.g. Kroll process

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)
  • Manufacture And Refinement Of Metals (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

Titanium is produced in a cyclic process by the reduction of a titanium halide, such as the tetrachloride, with molten sodium at 800-1000 DEG C. by placing a small proportion, e.g. 5 per cent by weight, of the sodium to be used in a reactor under an inert atmosphere such as argon and then adding the sodium and titanium halide simultaneously in stoichiometric proportions followed by the remainder of the titanium halide. The titanium halide is introduced into the reactor at a low velocity and the molten sodium is introduced through a multiorificed nozzle; the temperature is kept below 1000 DEG C. but sufficient to maintain molten all the contents of the reactor except the titanium. The reactor is allowed to cool to 400 DEG C., is removed from the furnace and allowed to cool to 60 DEG C. when it is opened and the product removed by drilling, leaving a half inch layer of product round the reactor walls. The product mixture is crushed, leached with 1 per cent hydrochloric acid (pH not more than 5) at a temperature not greater than 60 DEG C. to remove the sodium halide, and the titanium is washed with water and dried. The pH of the leaching liquid is raised to 7 by the addition of sodium hydroxide, to remove any dissolved titanium and other metals, and after filtering the precipitate and evaporating with water, the sodium halide is fused and electrolyzed to produce sodium and halogen. The molten sodium is filtered through a micro-metallic filter having a mesh with 5 micron holes and is used to reduce more titanium halide, whilst the halogen is reacted with further titaniferous material, the resultant titanium halide purified by fractional distillation and subsequently reduced to titanium metal.
GB17283/57A 1956-05-31 1957-05-31 Process for the production of titanium Expired GB805730A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US805730XA 1956-05-31 1956-05-31

Publications (1)

Publication Number Publication Date
GB805730A true GB805730A (en) 1958-12-10

Family

ID=22158244

Family Applications (1)

Application Number Title Priority Date Filing Date
GB17283/57A Expired GB805730A (en) 1956-05-31 1957-05-31 Process for the production of titanium

Country Status (2)

Country Link
BE (1) BE557987A (en)
GB (1) GB805730A (en)

Also Published As

Publication number Publication date
BE557987A (en)

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