Process for producing tantalum and columbium powder
AssigneeFansteel Inc.
InventorCarlos F. Rerat
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AssigneeFansteel Inc.
InventorCarlos F. Rerat
Estimating the term…
A method of producing tantalum or columbium powder is described for producing a selected desired particle size powder under controlled conditions with a high rate of production and yield of usable powder. A molten salt bath of an alkali metal tantalum fluoride or an alkali metal columbium fluoride and a relatively large amount of diluent salt to act as a heat sink is initially maintained at a low temperature in the liquidus range, an addition of liquid alkali metal reducing metal is added at a very fast rate to the continuously stirred bath to create a rapid temperature rise to the reaction temperature, and liquid alkali metal is thereafter fed at a fast rate to complete the reaction quickly at the final reaction temperature. Cooling is used for at least a portion of the reaction cycle at a rate sufficient to maintain the final reaction temperature within a desired range.
The process of producing a metal powder of the group consisting of tantalum and columbium powders which comprises maintaining a liquid bath of a double salt of the formula
The process of producing a tantalum powder which comprises maintaining a liquid bath of potassium fluotantalate and from about 0.6 to about 1.0 parts by a diluent comprising sodium chloride at a temperature above the liquidus temperature of said salt mixture but not exceeding 660.degree. C. in a closed reaction vessel, adding molten sodium to said bath at a rate of at least 0.2 kg per kg of said potassium fluotantalate per hour during a nucleation period until a desired reaction temperature between 760.degree. C. and 850.degree. C. is reached, the temperature rise during said nucleation period being at a rate of at least 20.degree. C. per minute, thereafter adding additional molten sodium to said bath at a rate of at least 0.1 kg per kg of said potassium fluotantalate per hour during a growth period while providing forced cooling to said bath by means of a high velocity air stream applied to the exterior of said vessel to extract heat at a rate of at least 10 kilocalories per minute per kilogram of said potassium fluotantalate, continuously agitating said liquid bath with an agitator maintained within said bath, continuously producing crystals of tantalum and collecting said crystals in a lower portion of said reaction vessel, said rate of alkali metal addition and said rate of forced cooling being balanced to maintain the reaction temperature in said growth period within 25.degree. C. of said desired reaction temperature but in excess of 760.degree. C.
Dependencies are inferred from the claim text.