using the armstrong method described in the above three identified patents and application ser . no . 11 / 186 , 724 filed jul . 21 , 2005 , the entire application is herein incorporated by reference . the equipment used to produce the 6 / 4 alloy with submicron titanium boride substantially uniformly dispersed therein is similar to that disclosed in the aforementioned patents disclosing the armstrong process with the exception that instead of only having a titanium tetrachloride boiler 22 as illustrated in those patents , there is also a boiler for each constituent of the alloy connected to the reaction chamber by suitable valves . boron addition is from a boiler for bcl 3 . the piping acts as a manifold so that the gases are completely mixed as they enter the reaction chamber and are introduced subsurface to the flowing liquid sodium , preferably at least at sonic velocity , as disclosed in the incorporated patents . upon subsurface contact with the liquid metal the halides immediately and completely react exothermically to form a reaction zone in which the reaction products are produced . the flowing liquid metal preferably sodium , sweeps the reaction products away from the reaction zone maintaining the reaction products at a temperature below the sintering temperatures of the reaction products . it was determined during production of the 6 / 4 alloy that aluminum trichloride is corrosive and required special materials not required for handling either titanium tetrachloride or vanadium tetrachloride . therefore , hastelloy c - 276 was used for the aluminum trichloride boiler and the piping to the reaction chamber . the bcl 3 is not as corrosive as alcl 3 . during most of the runs the steady state temperature of the reactor was maintained at about 400 ° c . by the use of sufficient excess sodium . other operating conditions for the production of the 6 / 4 alloy powder with submicron titanium boride dispersed in most , if not substantially all , of the particles forming the powder were as follows : a device similar to that described in the incorporated armstrong patents was used except that a vcl 4 boiler , a alcl 3 boiler and a bcl 3 boiler were provided and all three gases were fed into the line feeding ticl 4 into the liquid na . the typical boiler pressures and system parameters are listed hereafter in table 1 . the reactor was generally operated for approximately 250 seconds injecting approximately 11 kg of ticl 4 . the salt and titanium alloy solids were captured on a wedge wire filter and free sodium metal was drained away . the product cake containing titanium alloy , sodium chloride and sodium was distilled at approximately 100 milli - torr at 550 to 575 ° c . vessel wall temperatures for 20 hours . once all the sodium metal was removed via distillation , the trap was re - pressurized with argon gas and heated to 750 ° c . and held at temperature for 48 hours . the vessel containing the salt and titanium alloy cake was cooled and the cake was passivated with a 0 . 7 wt % oxygen / argon mixture . after passivation , the cake was washed with deionized water and subsequently dried in a vacuum oven at less than 100 ° c . table 2 below sets forth a chemical analysis of various runs for both ti as well as 6 / 4 alloy with submicron titanium boride substantially uniformly dispersed therein from an experimental loop running the armstrong process . as used herein , titanium boride means principally tib but does not exclude minor amounts of tib 2 or other borides . similarly , the process described herein produces a novel powder in which most , if not substantially all , of the particles forming the powder have submicron titanium boride dispersed therein . while the boride dispersion may not always be perfect in every particle , the titanium boride is very small , submicron , and generally uniformly dispersed within the particles forming the powder , whether the powder is titanium or a titanium alloy . as seen from table 2 below , the sodium levels for 6 / 4 with submicron titanium boride are very low while the sodium level for ti with submicron titanium boride are somewhat higher , but still less than commercially pure titanium , without submicron titanium boride dispersed therein , made by the armstrong process , as described in the incorporated application . as stated in the referenced application , the surface area of the 6 / 4 alloy compared to the cp titanium , as determined using bet specific surface area analysis with krypton as the adsorbate is much larger than the cp titanium . the surface area of the 6 / 4 alloy with titanium boride is even greater , that is the alloy powder with titanium boride was smaller in average diameter and more difficult to grow into larger particles than ti alloy without titanium boride . the sems of fig1 - 8 show that the 6 / 4 powder and / or ti powder with submicron titanium boride distributed therein is “ frillier ” than the previously made 6 / 4 powder in the referenced application . each of the figures references a run disclosed in table 1 and represents samples taken from that run at different magnifications . as stated in the referenced application and as reported by moxson et al ., innovations in titanium powder processing in the journal of metallurgy may 2000 , it is clear that by - product fines from the kroll or hunter processes contain large amounts of undesirable chlorine which is not present in the cp titanium powder or alloy made by the armstrong process . moreover , the morphology of the hunter and kroll fines , as previously discussed , is different from the cp powder or the 6 / 4 alloy powder or either with submicron titanium boride therein made by the armstrong process . neither the kroll nor the hunter process has been adapted to produce 6 / 4 alloy or any alloy . alloy powders have been produced by melting prealloyed stock and thereafter using either gas atomization or a hydride - dehydride process ( mhr ). the moxson et al . article discloses 6 / 4 powder made in tula , russia and as seen from fig2 in that article , particularly fig2 c and 2d the powders made by tula hydride reduction process are significantly different than those made by the armstrong process . moreover , referring to the moxson et al . article in the 1998 issue of the international journal of powder metallurgy , vol . 4 , no . 5 , pages 45 - 47 , it is seen that the chemical analysis for the pre - alloy 6 / 4 powder produced by the metal - hydride reduction ( mhd ) process contains exceptional amounts of calcium and also is not within astm specifications for aluminum . as is well known in the art , solid objects can be made by forming 6 / 4 or cp titanium powders into a near net shapes and thereafter sintering , see the moxson et al . article and can also be formed by hot isostatic pressing , laser deposition , metal injecting molding , direct powder rolling or various other well known techniques . therefore , the titanium alloy powder or titanium powder with submicron titanium boride dispersed substantially uniformly therein made by the armstrong method may be formed into a consolidated or a consolidated and sintered product or may be formed into a solid object by well known methods in the art and the subject invention is intended to cover all such products made from the powder of the subject invention . there has been disclosed herein a titanium metal powder or a titanium base alloy powder having submicron titanium boride substantially uniformly dispersed therein . the specific titanium alloy of the type set forth wherein al and v are present in a minor amount by weight , but preferably astm grade 5 , as well as commercially pure titanium , astm grade 2 , both as disclosed in the incorporated patent application , table 1 therein , with submicron titanium boride substantially uniformly dispersed therein have been disclosed , wherein boron is present up to about 4 % by weight . the invention however , includes any weight of boron added . preferably , alloys have at least 50 % by weight titanium with titanium boride , preferably tib , present in any required amount . any halide may be used in the process , as previously described , but chlorides are preferred because they are readily available and less expensive than other halides . various alkali or alkaline earth metals may be used , i . e . na , k , mg , ca , but na is preferred . solid products are routinely made by a variety of processes from the powders described herein . products made from powder produced by the armstrong method including bcl 3 introduced into flowing liquid reducing metal prod uce superior hardness and other desirable physical properties are within the scope of this invention . while the invention has been particularly shown and described with reference to a preferred embodiment thereof , it will be understood by those skilled in the art that several changes in form and detail may be made without departing from the spirit and scope of the invention .