Method for removing oxide contamination from titanium diboride powder

Abstract

A method for removing oxide contamination from titanium diboride powder involves the direct chemical treatment of TiB.sub.2 powders with a gaseous boron halide, such as BCl.sub.3, at temperatures in the range of 500.degree.-800.degree. C. The BCl.sub.3 reacts with the oxides to form volatile species which are removed by the BCl.sub.3 exit stream.

Description

BACKGROUND OF THE INVENTION

This invention, which was made under a contract with the U.S. Department of Energy, relates to titanium diboride powder and, more particularly, to a method for purifying such powder.

Titanium diboride (TiB.sub.2), an extremely hard refractory solid with very high resistance to oxidation and very low electrical resistance, is commonly commercially produced by the carbothermic reduction of a mixture of the oxides of titanium and boron. The TiB.sub.2 product from this process is always contaminated with oxides. Another method for producing TiB.sub.2 involves chemical vapor deposition from a mixture of titanium tetrachloride (TiCl.sub.4), boron trichloride (BCl.sub.3), and hydrogen (H.sub.2) on a hot surface. This method produces macrosize crystals of pure TiB.sub.2 which must be mechanically ground into powder and which consequently become contaminated, usually with metal oxides (Al.sub.2 O.sub.3,SiO.sub.2) from the grinding apparatus. It is suspected that this oxide contamination has a deleterious effect on the sintering of the powders and furthermore on integrity of sintered products.

Modifications to existing processes that would result in the direct production of pure TiB.sub.2 powders could be costly. It is therefore desirable to have a method for removing oxide contamination from TiB.sub.2 powders produced by existing processes.

SUMMARY OF THE INVENTION

It is the object of this invention to provide a method whereby oxide contamination can be removed from TiB.sub.2 powders. This is accomplished by chemically treating TiB.sub.2 powders with a gaseous boron halide such as boron trichloride (BCl.sub.3) at temperatures in the range of 500.degree.-800.degree. C. The BCl.sub.3 reacts with the contained oxides to form volatile species which are removed by the BCl.sub.3 exit stream. Typical reactions, depending on which oxides are present, are represented by the following equations: ##STR1##

Equilibrium constants for the above equations show favorable values at 1000K indicating that all of the reactions are spontaneously effective. Thus, the oxide-contaminated TiB.sub.2 obtained from the aforementioned commercial processes can readily be purified by treating the product with BCl.sub.3 in accordance with the method of the invention.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS OF THE INVENTION

A number of 1.25 g samples of commercially available TiB.sub.2 were treated with BCl.sub.3 at temperatures in the range of 500.degree. C. to 850.degree. C. Each sample was analyzed for oxygen content and placed in a gold combustion boat. The boat was inserted into a nickel tube which had been passivated by a pretreatment with BCl.sub.3. A flow of BCl.sub.3 (40 ml/min.) was directed through the tube as the tube and sample were heated to the desired temperature by a tube furnace. Each sample was treated for two hours and then cooled to room temperature in an argon atmosphere. The system was then transferred to a glove box with an inert atmosphere for weighing and sampling the TiB.sub.2. Oxide content of the samples was based on the oxygen content as determined by neutron activation analysis (NAA). Results are shown in Table I below.

TABLE I______________________________________% Oxygen (by NAA) TemperatureAs received After BCl.sub.3 Treatment .degree.C.______________________________________4.1 0.68 8500.75 0.57 8504.1 1.5 5004.2 1.5 6004.2 1.3 700______________________________________

EXAMPLE II

A second group of samples of TiB.sub.2 of the same size and origin used in Example I was exposed to BCl.sub.3 at temperatures ranging from 600.degree. C. to 800.degree. C. Each sample was placed in a previously BCl.sub.3 -passivated vertical nickel tube equipped with a nickel frit at its bottom end to retain the TiB.sub.2 and allow passage of BCl.sub.3. As the system was heated under argon to a desired temperature, a flow of BCl.sub.3 (40 ml/min.) was directed upward into the bottom of the tube and through the nickel frit. The particles of TiB.sub.2 were dispersed and suspended in the flowing BCl.sub.3, providing an improved solid-to-gas contact. Each sample was treated at a specific temperature for four hours and then processed according to the cooling, weighing, sampling, and analyzing procedure of Example I. Results are shown in Table II.

TABLE II______________________________________% Oxygen (by NAA) TemperatureAs received After BCl.sub.3 Treatment .degree.C.______________________________________4.2 1.7 7004.2 1.3 6000.58 0.37 6501.7 0.3 6502.2 0.8 6502.0 0.8 6500.8 0.64 8002.7 0.63 700______________________________________

Claims

1. A method for purifying titanium diboride powder contaminated with an oxide selected from the group consisting of TiO.sub.2, Ti.sub.2 O.sub.3, Al.sub.2 O.sub.3, SiO.sub.2, and B.sub.2 O.sub.3, comprising:

contacting the contaminated titanium diboride powder with an excess amount of gaseous BCl.sub.3 to thereby form gaseous (BOCl).sub.3 by reaction of said BCl.sub.3 with said oxide; and

separating the gaseous (BOCl).sub.3 from the titanium diboride powder.

2. The method of claim 1 wherein said gaseous BCl.sub.3 is contacted with said contaminated titanium diboride powder at a temperature in the range of about 500.degree. C. to about 850.degree. C.