CA2330352A1 - Refractory hard metals in powder form for use in the manufacture of electrodes - Google Patents
Refractory hard metals in powder form for use in the manufacture of electrodes Download PDFInfo
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- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/06—Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
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Abstract
The invention relates to a refractory hard metal in powder form comprising particles having an average particle size of 0.1 to 30 µm and each formed of an agglomerate of refractory hard metals of the formula:
A x B y X z (I) wherein A is a transition metal, B is a metal selected from the group consisting of zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, manganese, tungsten and cobalt, X is boron or carbon, x ranges from 0.1 to 3, y ranges from 0 to 3 and z from 1 to 6. The refractory hard metal in powder form according to the invention is suitable for use in the manufacture of electrodes by thermal deposition or powder metallurgy.
A x B y X z (I) wherein A is a transition metal, B is a metal selected from the group consisting of zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, manganese, tungsten and cobalt, X is boron or carbon, x ranges from 0.1 to 3, y ranges from 0 to 3 and z from 1 to 6. The refractory hard metal in powder form according to the invention is suitable for use in the manufacture of electrodes by thermal deposition or powder metallurgy.
Description
REFRACTORY HARD METALS IN POWDER FORM FOR
USE IN THE MANUFACTURE OF ELECTRODES
The present invention pertains to improvements in the field of electrodes for metal electrolysis. More particularly, the invention relates to a refractory hard metals in powder form for use in the manufacture of such electrodes.
Aluminum is produced conventionally in a Hall-Heroult reduction cells by the electrolysis of alumina dissolved in molten cryolite (Na3A1F6) at temperatures of up to about 950 °C. A Hall-Heroult cell typically has a steel shell provided with an insulating lining of refractory material, which in turn has a lining made of prebaked carbon blocks contacting the molten constituents of the electrolyte. The carbon lining acts as the cathode substrate and the molten aluminum pool acts as the cathode. The anode is a consumable carbon electrode, usually prebaked carbon made by coke calcination.
During electrolysis, in Hall-Heroult cells, the carbon anode is consumed leading to the evolution of greenhouse gases such as CO and C02.
The anode has to be periodically changed and the erosion of the material modifies the anode-cathode distance, which increases the voltage due to the electrolyte resistance. On the cathode side, the carbon blocks are subjected to erosion and electrolyte penetration. A sodium intercalation in the graphitic structure occurs, which cause swelling and deformation of the cathode carbon blocks. The increase of voltage between the electrodes adversely affects the energy efficiency of the process.
Extensive research has been carried out with refractory hard metals such as TiBz, as electrode materials. TiB2 and other refractory hard metals are practically insoluble in aluminum, have a low electrical resistance and are wetted by aluminum. However, the shaping of TiB2 and similar refractory hard metals is difficult because these materials have high melting temperatures and are highly covalent.
It is therefore an object of the present invention to overcome the above drawbacks, and to provide a refractory hard metal in powder form suitable for the manufacture of electrode by thermal deposition or powder metallurgy.
According to one aspect of the invention, there is provided a refractory hard metal in powder form comprising particles having an average particle size of 0.1 to 30 dm and each formed of an agglomerate of grains with each grain comprising a nanocrystal of a refractory hard metal of the formula:
AXByXZ ~I) wherein A is a transition metal, B is a metal selected from the group consisting of zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, manganese, tungsten and cobalt, X is boron or carbon, x ranges from 0.1 to 3, y ranges from 0 to 3 and z from 1 to 6.
The term "nanocrystal" as used herein refers to a crystal having a size of 100 nanometers or less.
The expression "thermal deposition" as used herein refers to a technique in which powder particles are injected in a torch and sprayed on a substrate. The particles acquire a high velocity and are partially or totally melted during the flight path. The coating is budded by the solidification of the droplets on the substrate surface. Examples of such techniques include plasma spray, arc spray and high velocity oxy-fuel.
USE IN THE MANUFACTURE OF ELECTRODES
The present invention pertains to improvements in the field of electrodes for metal electrolysis. More particularly, the invention relates to a refractory hard metals in powder form for use in the manufacture of such electrodes.
Aluminum is produced conventionally in a Hall-Heroult reduction cells by the electrolysis of alumina dissolved in molten cryolite (Na3A1F6) at temperatures of up to about 950 °C. A Hall-Heroult cell typically has a steel shell provided with an insulating lining of refractory material, which in turn has a lining made of prebaked carbon blocks contacting the molten constituents of the electrolyte. The carbon lining acts as the cathode substrate and the molten aluminum pool acts as the cathode. The anode is a consumable carbon electrode, usually prebaked carbon made by coke calcination.
During electrolysis, in Hall-Heroult cells, the carbon anode is consumed leading to the evolution of greenhouse gases such as CO and C02.
The anode has to be periodically changed and the erosion of the material modifies the anode-cathode distance, which increases the voltage due to the electrolyte resistance. On the cathode side, the carbon blocks are subjected to erosion and electrolyte penetration. A sodium intercalation in the graphitic structure occurs, which cause swelling and deformation of the cathode carbon blocks. The increase of voltage between the electrodes adversely affects the energy efficiency of the process.
Extensive research has been carried out with refractory hard metals such as TiBz, as electrode materials. TiB2 and other refractory hard metals are practically insoluble in aluminum, have a low electrical resistance and are wetted by aluminum. However, the shaping of TiB2 and similar refractory hard metals is difficult because these materials have high melting temperatures and are highly covalent.
It is therefore an object of the present invention to overcome the above drawbacks, and to provide a refractory hard metal in powder form suitable for the manufacture of electrode by thermal deposition or powder metallurgy.
According to one aspect of the invention, there is provided a refractory hard metal in powder form comprising particles having an average particle size of 0.1 to 30 dm and each formed of an agglomerate of grains with each grain comprising a nanocrystal of a refractory hard metal of the formula:
AXByXZ ~I) wherein A is a transition metal, B is a metal selected from the group consisting of zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, manganese, tungsten and cobalt, X is boron or carbon, x ranges from 0.1 to 3, y ranges from 0 to 3 and z from 1 to 6.
The term "nanocrystal" as used herein refers to a crystal having a size of 100 nanometers or less.
The expression "thermal deposition" as used herein refers to a technique in which powder particles are injected in a torch and sprayed on a substrate. The particles acquire a high velocity and are partially or totally melted during the flight path. The coating is budded by the solidification of the droplets on the substrate surface. Examples of such techniques include plasma spray, arc spray and high velocity oxy-fuel.
-2-The expression "powder metallurgy" as used herein refers to a technique in which the bulk powders are transformed into preforms of a desired shape by compaction or shaping followed by a sintering step. Compaction refers to techniques where pressure is applied to the powder, as, for example, cold uniaxial pressing, cold isostatic pressing or hot isostatic pressing. Shaping refers to techniques executed without the application of external pressure such as powder filling or slurry casting.
Typical examples of refractory hard metals of the formula (I) include TiBl.s, TiB2, TiC, Tio.sZro.sBz~ Tio.9Zro.~Bz~ Tio.sHfo.sBz and Zro.sVo.2B2~
TiB2 is preferred.
The present invention also provides, in another aspect thereof, a process for producing a refractory hard metal in powder form as defined above.
The process of the invention comprises the steps of:
a) providing a first reagent selected from the group consisting of transition metals and transition metal-containing compounds;
b) providing a second reagent selected from the group consisting of boron, boron-containing compounds, carbon and carbon-containing compounds;
c) providing an optional third reagent selected from the group consisting of zirconium, zirconium-containing compounds, hafnium, hafnium-containing compounds, vanadium, vanadium-containing compounds, niobium, niobium-containing compounds, chromium, chromium-containing compounds, molybdenum, molybdenum-containing compounds, manganese, manganese-containing compounds, tungsten, tungsten-containing compounds, cobalt and cobalt-containing compounds; and
Typical examples of refractory hard metals of the formula (I) include TiBl.s, TiB2, TiC, Tio.sZro.sBz~ Tio.9Zro.~Bz~ Tio.sHfo.sBz and Zro.sVo.2B2~
TiB2 is preferred.
The present invention also provides, in another aspect thereof, a process for producing a refractory hard metal in powder form as defined above.
The process of the invention comprises the steps of:
a) providing a first reagent selected from the group consisting of transition metals and transition metal-containing compounds;
b) providing a second reagent selected from the group consisting of boron, boron-containing compounds, carbon and carbon-containing compounds;
c) providing an optional third reagent selected from the group consisting of zirconium, zirconium-containing compounds, hafnium, hafnium-containing compounds, vanadium, vanadium-containing compounds, niobium, niobium-containing compounds, chromium, chromium-containing compounds, molybdenum, molybdenum-containing compounds, manganese, manganese-containing compounds, tungsten, tungsten-containing compounds, cobalt and cobalt-containing compounds; and
-3-d) subjecting the first, second and third reagents to high-energy ball milling to cause solid state reaction therebetween and formation of particles having an average particle size of 0.1 to 30 Vim, each particle being formed of an agglomerate of grains with each grain comprising a nanocrystal of a refractory hard metal of formula (I) defined above.
The expression "high-energy ball milling" as used herein refers to a ball milling process capable of forming the aforesaid particles comprising nanocrystalline grains of the refractory hard metal of formula (I), within a period of time of about 40 hours.
Examples of suitable transition metals which may be used as the aforesaid first reagent include titanium, chromium, zirconium and vanadium.
Titanium is preferred. It is also possible to use a titanium-containing compound such as TiH2, TiAl3, TiB and TiCl2.
Examples of suitable boron-containing compounds which may be used as the aforesaid second reagent include A1B2, A1B,2, BH3, BN, VB, H2B03 and Na2B40~. It is also possible to use tetraboron carbide (B4C) as either a boron-containing compound or a carbon-containing compound.
Examples of suitable compounds which may be used as the aforesaid third reagent include HfB2, VBZ, NbB2, TaB2, CrB2, MoB2, MnB2, Mo2B5, W2B5, CoB, ZrC, TaC, WC and HfC.
According to a preferred embodiment, step (d) is carried out in a vibratory ball mill operated at a frequency of 8 to 25 Hz, preferably about 17 Hz. It is also possible to conduct step (d) in a rotary ball mill operated at a speed of 150 to 1500 r.p.m., preferably about 1000 r.p.m.
The expression "high-energy ball milling" as used herein refers to a ball milling process capable of forming the aforesaid particles comprising nanocrystalline grains of the refractory hard metal of formula (I), within a period of time of about 40 hours.
Examples of suitable transition metals which may be used as the aforesaid first reagent include titanium, chromium, zirconium and vanadium.
Titanium is preferred. It is also possible to use a titanium-containing compound such as TiH2, TiAl3, TiB and TiCl2.
Examples of suitable boron-containing compounds which may be used as the aforesaid second reagent include A1B2, A1B,2, BH3, BN, VB, H2B03 and Na2B40~. It is also possible to use tetraboron carbide (B4C) as either a boron-containing compound or a carbon-containing compound.
Examples of suitable compounds which may be used as the aforesaid third reagent include HfB2, VBZ, NbB2, TaB2, CrB2, MoB2, MnB2, Mo2B5, W2B5, CoB, ZrC, TaC, WC and HfC.
According to a preferred embodiment, step (d) is carried out in a vibratory ball mill operated at a frequency of 8 to 25 Hz, preferably about 17 Hz. It is also possible to conduct step (d) in a rotary ball mill operated at a speed of 150 to 1500 r.p.m., preferably about 1000 r.p.m.
-4-According to another preferred embodiment, step (d) is carried out under an inert gas atmosphere such as a gas atmosphere comprising argon or helium, or under a reactive gas atmosphere such as a gas atmosphere comprising hydrogen, ammonia or a hydrocarbon, in order to saturate dangling bonds and thereby prevent oxidation of the refractory hard metal. An atmosphere of argon, helium or hydrogen is preferred. It is also possible to coat the particles with a protective film or to admix a sacrificial element such as Mg or Ca with the reagents. In addition, a sintering aid such as Y203 can be added during step (d).
In the particular case of TiB2 or TiC wherein titanium and boron or carbon are present in stoichiometric quantities, these two compounds can be used as starting material. Thus, they can be directly subjected to high-energy ball milling to cause formation of particles having an average particle size of 0.1 to 30 Vim, each particle being formed of an agglomerate of grains with each grain comprising a nanocrystal of TiB2 or TiC.
The high-energy ball milling described above enables one to obtain refractory hard metals in powder form having either non-stoichiometric or stoichiometric compositions.
The refractory hard metals in powder form according to the invention are suitable for use in the manufacture of electrodes by thermal deposition or powder metallurgy. Due to the properties of refractory hard metals, the emission of toxic and greenhouse effect gases during metal electrolysis is lowered and the lifetime of the electrodes is increased, thus lowering maintenance costs. A lower and constant inter-electrode distance is also possible, thereby decreasing the electrolyte ohmic drop.
In the particular case of TiB2 or TiC wherein titanium and boron or carbon are present in stoichiometric quantities, these two compounds can be used as starting material. Thus, they can be directly subjected to high-energy ball milling to cause formation of particles having an average particle size of 0.1 to 30 Vim, each particle being formed of an agglomerate of grains with each grain comprising a nanocrystal of TiB2 or TiC.
The high-energy ball milling described above enables one to obtain refractory hard metals in powder form having either non-stoichiometric or stoichiometric compositions.
The refractory hard metals in powder form according to the invention are suitable for use in the manufacture of electrodes by thermal deposition or powder metallurgy. Due to the properties of refractory hard metals, the emission of toxic and greenhouse effect gases during metal electrolysis is lowered and the lifetime of the electrodes is increased, thus lowering maintenance costs. A lower and constant inter-electrode distance is also possible, thereby decreasing the electrolyte ohmic drop.
-5-The following non-limiting examples illustrate the invention, reference being made to the accompanying drawing in which the sole figure shows the X-ray diffraction of the refractory hard metal in powder form obtained in Example 1.
EXAMPLE 1.
A TiB2 powder was produced by ball milling 3.45g of titanium and I.SSg of boron in a hardened steel crucible with a ball-to-powder mass ratio of 4.5:1 using a SPEX 8000 (trademark) vibratory ball mill operated at a frequency of about 17 Hz. The operation was performed under a controlled argon atmosphere to prevent oxidization. The crucible was closed and sealed with a rubber O-ring. After 5 hours of high-energy ball milling, a TiB2 structure was formed, as shown on the X-ray diffraction pattern in the accompanying drawing. The structure of TiB2 is hexagonal with the space group P6/mmm ( 191 ). The particle size varied between 1 and 5 pm and the crystallite size, measured by X-ray diffraction, was about 30 nm.
EXAMPLE 2.
A TiB2 powder was produced according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that the ball milling was carried out for 20 hours instead of 5 hours.
The resulting powder was similar to that obtained in Example 1. The crystallite size, however, was lower (about 16 nm).
EXAMPLE 1.
A TiB2 powder was produced by ball milling 3.45g of titanium and I.SSg of boron in a hardened steel crucible with a ball-to-powder mass ratio of 4.5:1 using a SPEX 8000 (trademark) vibratory ball mill operated at a frequency of about 17 Hz. The operation was performed under a controlled argon atmosphere to prevent oxidization. The crucible was closed and sealed with a rubber O-ring. After 5 hours of high-energy ball milling, a TiB2 structure was formed, as shown on the X-ray diffraction pattern in the accompanying drawing. The structure of TiB2 is hexagonal with the space group P6/mmm ( 191 ). The particle size varied between 1 and 5 pm and the crystallite size, measured by X-ray diffraction, was about 30 nm.
EXAMPLE 2.
A TiB2 powder was produced according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that the ball milling was carried out for 20 hours instead of 5 hours.
The resulting powder was similar to that obtained in Example 1. The crystallite size, however, was lower (about 16 nm).
-6-EXAMPLE 3.
A TiC powder was produced according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that titanium and graphite were milled.
EXAMPLE 4.
A TiB2 powder was produced by ball milling titanium diboride under the same operating conditions as in Example 1, with the exception that the ball milling was carried out for 20 hours instead of 5 hours. The starting structure was maintained, but the crystallite size decreased to 15 nm.
EXAMPLE 5.
A TiB 1.g powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 3.6 g of titanium and 1.4 g of boron were milled.
EXAMPLE 6.
A TiB2.2 powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 3.4 g of titanium and 1.7 g of boron were milled.
EXAMPLE 7.
A TiBo.SZro.5B2 powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the _7_ exception that 1.9 g of titanium, 3.1 g of zirconium diboride and 0.8 g of boron were milled.
EXAMPLE 8.
A TiBo.9Zro,lBz powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 2.9 g of titanium, 0.6 g of zirconium and 1.5 g of boron were milled.
EXAMPLE 9.
A TiBo.SHfo,5B2 powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 0.9 g of titanium, 3.3 g of hafnium and 0.8 g of boron were milled.
EXAMPLE 10.
A Zro,gVo.2B2 powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 3.5 g of zirconium, 0.5 g of vanadium and 1.0 g of boron were milled.
_g_
A TiC powder was produced according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that titanium and graphite were milled.
EXAMPLE 4.
A TiB2 powder was produced by ball milling titanium diboride under the same operating conditions as in Example 1, with the exception that the ball milling was carried out for 20 hours instead of 5 hours. The starting structure was maintained, but the crystallite size decreased to 15 nm.
EXAMPLE 5.
A TiB 1.g powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 3.6 g of titanium and 1.4 g of boron were milled.
EXAMPLE 6.
A TiB2.2 powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 3.4 g of titanium and 1.7 g of boron were milled.
EXAMPLE 7.
A TiBo.SZro.5B2 powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the _7_ exception that 1.9 g of titanium, 3.1 g of zirconium diboride and 0.8 g of boron were milled.
EXAMPLE 8.
A TiBo.9Zro,lBz powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 2.9 g of titanium, 0.6 g of zirconium and 1.5 g of boron were milled.
EXAMPLE 9.
A TiBo.SHfo,5B2 powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 0.9 g of titanium, 3.3 g of hafnium and 0.8 g of boron were milled.
EXAMPLE 10.
A Zro,gVo.2B2 powder was according to the same procedure as described in Example 1 and under the same operating conditions, with the exception that 3.5 g of zirconium, 0.5 g of vanadium and 1.0 g of boron were milled.
_g_
Claims (45)
1. A refractory hard metal in powder form comprising particles having an average particle size of 0.1 to 30 µm and each formed of an agglomerate of refractory hard metals of the formula:
A x B y X z (I) wherein A is a transition metal, B is a metal selected from the group consisting of zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, manganese, tungsten and cobalt, X is boron or carbon, x ranges from 0.1 to 3, y ranges from 0 to 3 and z from 1 to 6.
A x B y X z (I) wherein A is a transition metal, B is a metal selected from the group consisting of zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, manganese, tungsten and cobalt, X is boron or carbon, x ranges from 0.1 to 3, y ranges from 0 to 3 and z from 1 to 6.
2. A refractory hard metal in powder form according to claim 1, wherein A is a transition metal selected from the group consisting of titanium, chromium, zirconium and vanadium.
3. A refractory hard metal in powder form according to claim 2, wherein A is titanium, X is boron and y is 0.
4. A refractory hard metal in powder form according to claim 3, wherein x is 1 and z is 1.8.
5. A refractory hard metal in powder form according to claim 3, wherein x is 1 and z is 2.
6. A refractory hard metal in powder form according to claim 3, wherein x is 1 and z is 2.2.
7. A refractory hard metal in powder form according to claim 2, wherein A is titanium, X is carbon and y is 0.
8. A refractory hard metal in powder form according to claim 8, wherein x is 1 and z is 1.
9. A refractory hard metal in powder form according to claim 2, wherein A is titanium, B is zirconium or hafnium, X is boron and y is other than 0.
10. A refractory hard metal in powder form according to claim 9, wherein B is zirconium, x is 0.5, y is 0.5 and z is 2.
11. A refractory hard metal in powder form according to claim 9, wherein B is zirconium, x is 0.9, y is 0.1 and z is 2.
12. A refractory hard metal in powder form according to claim 2, wherein B is hafnium, x is 0.5, y is 0.5 and z is 2.
13. A refractory hard metal in powder form according to claim 2, wherein A is zirconium, B is vanadium, X is boron and y is other than 0.
14. A refractory hard metal in powder form according to claim 13, wherein x is 0.8, y is 0.2 and z is 2.
15. A refractory hard metal in powder form according to claim 1, wherein said average particle size ranges from 1 to 5 µm.
16. A process for producing a refractory hard metal in powder form as defined in claim 1, comprising the steps of:
a) providing a first reagent selected from the group consisting of transition metals and transition metal-containing compounds;
b) providing a second reagent selected from the group consisting of boron, boron-containing compounds, carbon and carbon-containing compounds;
c) providing an optional third reagent selected from the group consisting of zirconium, zirconium-containing compounds, hafnium, hafnium-containing compounds, vanadium, vanadium-containing compounds, niobium, niobium-containing compounds, chromium, chromium-containing compounds, molybdenum, molybdenum-containing compounds, manganese, manganese-containing compounds, tungsten, tungsten-containing compounds, cobalt and cobalt-containing compounds; and d) subjecting said first, second and third reagents to high-energy ball milling to cause solid state reaction therebetween and formation of particles having an average particle size of 0.1 to 30 µm, each particle being formed of an agglomerate of grains with each grain comprising a nanocrystal of a refractory hard metal of the formula (I) as defined in claim 1.
a) providing a first reagent selected from the group consisting of transition metals and transition metal-containing compounds;
b) providing a second reagent selected from the group consisting of boron, boron-containing compounds, carbon and carbon-containing compounds;
c) providing an optional third reagent selected from the group consisting of zirconium, zirconium-containing compounds, hafnium, hafnium-containing compounds, vanadium, vanadium-containing compounds, niobium, niobium-containing compounds, chromium, chromium-containing compounds, molybdenum, molybdenum-containing compounds, manganese, manganese-containing compounds, tungsten, tungsten-containing compounds, cobalt and cobalt-containing compounds; and d) subjecting said first, second and third reagents to high-energy ball milling to cause solid state reaction therebetween and formation of particles having an average particle size of 0.1 to 30 µm, each particle being formed of an agglomerate of grains with each grain comprising a nanocrystal of a refractory hard metal of the formula (I) as defined in claim 1.
17. A process according to claim 16, wherein said first reagent comprises a transition metal selected from the group consisting of titanium, chromium, zirconium and vanadium.
18. A process according to claim 17, wherein said transition metal is titanium.
19. A process according to claim 16, wherein said first reagent comprises a titanium-containing compound selected from the group TiH2, TiA13, TiB and TiC12.
20. A process according to claim 16, wherein said second reagent comprises boron.
21. A process according to claim 16, wherein said second reagent comprises a boron-containing compound selected from the group consisting of A1B2, A1B12, BH3, BN, VB2, H2BO3 and Na2BO7.
22. A process according to claim 16, wherein said second reagent comprises carbon.
23. A process according to claim 16, wherein said second reagent comprises tetraboron carbide.
24. A process according to claim 16, wherein said third reagent is a compound selected from the group consisting of HfB2, VB2, NbB2, TaB2, CrB2, MoB2, MnB2, Mo2B5, W2B5, CoB, ZrC, TaC, WC and HfC.
25. A process according to claim 16, wherein step (d) is carried out in a vibratory ball mill operated at a frequency of 8 to 25 Hz.
26. A process according to claim 25, wherein said vibratory ball mill is operated at a frequency of about 17 Hz.
27. A process according to claim 16, wherein step (d) is carried out in a rotary ball mill operated at a speed of 150 to 1500 r.p.m.
28. A process according to claim 27, wherein said rotary ball mill is operated at a speed of about 1000 r.p.m.
29. A process according to claim 16, wherein step (d) is carried out under an inert gas atmosphere.
30. A process according to claim 29, wherein said inert gas atmosphere comprises argon or helium.
31. A process according to claim 16, wherein step (d) is carried out under a reactive gas atmosphere.
32. A process according to claim 31, wherein said reactive gas atmosphere comprises hydrogen, ammonia or a hydrocarbon.
33. A process according to claim 16, wherein step (d) is carried out for a period of time of about 5 hours.
34. A process according to claim 16, wherein a sintering aid is added during step (d).
35. A processd of preparing a grain refining agent as defined in claim or 8, comprising subjecting TiB2 or TiC to high-energy ball milling to cause formation of particles having an average particle size of 0.1 to 30 µm, each particle being formed of an agglomerate of grains with each grain comprising a nanocrystal of TiB2 or TiC.
36. A process according to claim 35, wherein said high-energy ball milling is carried out in a vibratory ball mill operated at a frequency of 8 to 25 Hz.
37. A process according to claim 36, wherein said vibratory ball mill is operated at a frequency of about 17 Hz.
38. A process according to claim 35, wherein said high-energy ball milling is carried out in a rotary ball mill operated at a speed of 150 to r.p.m.
39. A process according to claim 38, wherein said rotary ball mill is operated at a speed of about 1000 r.p.m.
40. A process according to claim 35, wherein said high-energy ball milling is carried out under an inert gas atmosphere.
41. A process according to claim 35, wherein said inert gas atmosphere comprises argon or helium.
42. A process according to claim 35, wherein said high-energy ball milling is carried out under a reactive gas atmosphere.
43. A process according to claim 42, wherein said reactive gas atmosphere comprises hydrogen, ammonia or a hydrocarbon.
44. A process according to claim 35, wherein said high-energy ball milling is carried out for a period of time of about 20 hours.
45. A process according to claim 35, wherein a sintering aid is added during said high-enery bal milling.
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002330352A CA2330352A1 (en) | 2001-01-05 | 2001-01-05 | Refractory hard metals in powder form for use in the manufacture of electrodes |
PCT/CA2002/000013 WO2002053495A1 (en) | 2001-01-05 | 2002-01-02 | Refractory hard metals in powder form for use in the manufacture of electrodes |
RU2003124183/15A RU2003124183A (en) | 2001-01-05 | 2002-01-02 | Refractory solid alloys in the form of powder for use in the manufacture of electrodes |
US10/250,499 US20040052713A1 (en) | 2001-01-05 | 2002-01-02 | Refractory hard metals in powder form for use in the manufacture of electrodes |
EP02726977A EP1347939A1 (en) | 2001-01-05 | 2002-01-02 | Refractory hard metals in powder form for use in the manufacture of electrodes |
CNA028035011A CN1484613A (en) | 2001-01-05 | 2002-01-02 | Refractory hard metals in powder form for use in the manufacture of electrodes |
BR0206306-9A BR0206306A (en) | 2001-01-05 | 2002-01-02 | Refractory powdered hard metals for use in electrode manufacturing |
JP2002554621A JP2004516226A (en) | 2001-01-05 | 2002-01-02 | Refractory hard alloy in powder form for electrode production |
NO20033076A NO20033076L (en) | 2001-01-05 | 2003-07-04 | Refractory powdered hard metals for use in electrode production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CA002330352A CA2330352A1 (en) | 2001-01-05 | 2001-01-05 | Refractory hard metals in powder form for use in the manufacture of electrodes |
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CA2330352A1 true CA2330352A1 (en) | 2002-07-05 |
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CA002330352A Abandoned CA2330352A1 (en) | 2001-01-05 | 2001-01-05 | Refractory hard metals in powder form for use in the manufacture of electrodes |
Country Status (9)
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US (1) | US20040052713A1 (en) |
EP (1) | EP1347939A1 (en) |
JP (1) | JP2004516226A (en) |
CN (1) | CN1484613A (en) |
BR (1) | BR0206306A (en) |
CA (1) | CA2330352A1 (en) |
NO (1) | NO20033076L (en) |
RU (1) | RU2003124183A (en) |
WO (1) | WO2002053495A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102430757A (en) * | 2011-11-25 | 2012-05-02 | 天津大学 | Method for preparing TiB2/TiC (titanium diboride/titanium carbide) ultrafine powder for surface spraying of engine piston ring by means of high energy ball milling |
Families Citing this family (11)
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KR100546041B1 (en) * | 2005-05-31 | 2006-01-26 | 가야에이엠에이 주식회사 | Method for manufacturing titanium carbide using a rotary kiln furnace |
AU2007215394B2 (en) * | 2006-02-17 | 2013-06-27 | Gravitas Technologies Pty Ltd | Crystalline ternary ceramic precursors |
US8142749B2 (en) * | 2008-11-17 | 2012-03-27 | Kennametal Inc. | Readily-densified titanium diboride and process for making same |
EP2459775B1 (en) * | 2009-07-28 | 2018-09-05 | Alcoa USA Corp. | Composition for making wettable cathode in aluminum smelting |
JP5780540B2 (en) * | 2010-12-24 | 2015-09-16 | 国立研究開発法人物質・材料研究機構 | Zirconium diboride powder and synthesis method thereof |
JP2015174046A (en) * | 2014-03-17 | 2015-10-05 | Jfeマテリアル株式会社 | Manufacturing method of chromium for powder metallurgy |
KR101659823B1 (en) * | 2014-12-17 | 2016-09-27 | 한국기계연구원 | A HfC Composites and A Manufacturing method of the same |
CN105297069A (en) * | 2015-11-18 | 2016-02-03 | 上海大学 | Electrochemical method for directly preparing metal carbide accurately and controllably |
CN108165858B (en) * | 2017-11-15 | 2022-03-25 | 常德永 | High-temperature sensitive nano material and preparation method thereof |
CN109896861A (en) * | 2019-04-11 | 2019-06-18 | 哈尔滨工业大学 | A kind of high-purity, the small grain size hafnium boride raw powder's production technology of resistance to ablation |
CN110655408B (en) * | 2019-11-13 | 2021-10-08 | 哈尔滨工业大学 | Preparation method of single-phase carborundum solid solution ceramic material |
Family Cites Families (4)
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FR2634475B1 (en) * | 1988-07-22 | 1990-10-12 | Centre Nat Rech Scient | PROCESS FOR THE PREPARATION OF POWDERS OF COMPONENTS OF COLUMN IV A COMPONENTS AND PRODUCTS OBTAINED |
JPH0674126B2 (en) * | 1989-11-20 | 1994-09-21 | 科学技術庁金属材料技術研究所長 | Method for producing transition metal carbide |
CN1147478A (en) * | 1996-05-17 | 1997-04-16 | 浙江大学 | Normal-temp composition process of ultrafine tungsten carbide and titanium carbide powder |
US6214309B1 (en) * | 1997-09-24 | 2001-04-10 | University Of Connecticut | Sinterable carbides from oxides using high energy milling |
-
2001
- 2001-01-05 CA CA002330352A patent/CA2330352A1/en not_active Abandoned
-
2002
- 2002-01-02 JP JP2002554621A patent/JP2004516226A/en active Pending
- 2002-01-02 BR BR0206306-9A patent/BR0206306A/en not_active Application Discontinuation
- 2002-01-02 RU RU2003124183/15A patent/RU2003124183A/en not_active Application Discontinuation
- 2002-01-02 EP EP02726977A patent/EP1347939A1/en not_active Withdrawn
- 2002-01-02 CN CNA028035011A patent/CN1484613A/en active Pending
- 2002-01-02 US US10/250,499 patent/US20040052713A1/en not_active Abandoned
- 2002-01-02 WO PCT/CA2002/000013 patent/WO2002053495A1/en not_active Application Discontinuation
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2003
- 2003-07-04 NO NO20033076A patent/NO20033076L/en not_active Application Discontinuation
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102430757A (en) * | 2011-11-25 | 2012-05-02 | 天津大学 | Method for preparing TiB2/TiC (titanium diboride/titanium carbide) ultrafine powder for surface spraying of engine piston ring by means of high energy ball milling |
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Publication number | Publication date |
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NO20033076L (en) | 2003-09-05 |
US20040052713A1 (en) | 2004-03-18 |
NO20033076D0 (en) | 2003-07-04 |
BR0206306A (en) | 2004-02-17 |
CN1484613A (en) | 2004-03-24 |
RU2003124183A (en) | 2005-01-10 |
EP1347939A1 (en) | 2003-10-01 |
WO2002053495A1 (en) | 2002-07-11 |
JP2004516226A (en) | 2004-06-03 |
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