US3328280A - Electrically conductive cermet compositions - Google Patents
Electrically conductive cermet compositions Download PDFInfo
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- US3328280A US3328280A US358068A US35806864A US3328280A US 3328280 A US3328280 A US 3328280A US 358068 A US358068 A US 358068A US 35806864 A US35806864 A US 35806864A US 3328280 A US3328280 A US 3328280A
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- aluminum nitride
- titanium diboride
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- 239000000203 mixture Substances 0.000 title claims description 16
- 239000011195 cermet Substances 0.000 title description 8
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 53
- 229910052782 aluminium Inorganic materials 0.000 claims description 51
- PMHQVHHXPFUNSP-UHFFFAOYSA-M copper(1+);methylsulfanylmethane;bromide Chemical compound Br[Cu].CSC PMHQVHHXPFUNSP-UHFFFAOYSA-M 0.000 claims description 26
- 229910033181 TiB2 Inorganic materials 0.000 claims description 17
- QYEXBYZXHDUPRC-UHFFFAOYSA-N B#[Ti]#B Chemical compound B#[Ti]#B QYEXBYZXHDUPRC-UHFFFAOYSA-N 0.000 claims description 14
- 238000004519 manufacturing process Methods 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 7
- 235000010210 aluminium Nutrition 0.000 description 43
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 21
- 229910002804 graphite Inorganic materials 0.000 description 14
- 239000010439 graphite Substances 0.000 description 14
- 239000002131 composite material Substances 0.000 description 12
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000002184 metal Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 9
- 238000005245 sintering Methods 0.000 description 8
- 229910052799 carbon Inorganic materials 0.000 description 7
- 239000000470 constituent Substances 0.000 description 7
- 238000007731 hot pressing Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 229910052719 titanium Inorganic materials 0.000 description 5
- 239000010936 titanium Substances 0.000 description 5
- 229910001610 cryolite Inorganic materials 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000006698 induction Effects 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- SXRIPRHXGZHSNU-UHFFFAOYSA-N iridium rhodium Chemical compound [Rh].[Ir] SXRIPRHXGZHSNU-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052752 metalloid Inorganic materials 0.000 description 2
- 150000002738 metalloids Chemical class 0.000 description 2
- 150000004767 nitrides Chemical class 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 229910000629 Rh alloy Inorganic materials 0.000 description 1
- 229910001315 Tool steel Inorganic materials 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 229910052741 iridium Inorganic materials 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 238000005555 metalworking Methods 0.000 description 1
- 210000003205 muscle Anatomy 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/64—Burning or sintering processes
- C04B35/645—Pressure sintering
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/515—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
- C04B35/58—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides
- C04B35/5805—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides based on borides
- C04B35/58064—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides based on borides based on refractory borides
- C04B35/58071—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides based on borides based on refractory borides based on titanium borides
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/515—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
- C04B35/58—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides
- C04B35/581—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides based on aluminium nitride
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C29/00—Alloys based on carbides, oxides, nitrides, borides, or silicides, e.g. cermets, or other metal compounds, e.g. oxynitrides, sulfides
- C22C29/14—Alloys based on carbides, oxides, nitrides, borides, or silicides, e.g. cermets, or other metal compounds, e.g. oxynitrides, sulfides based on borides
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- 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
- C25C3/16—Electric current supply devices, e.g. bus bars
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2998/00—Supplementary information concerning processes or compositions relating to powder metallurgy
Definitions
- This invention relates to novel cermets composed of aluminum nitride and an electrically conductive constituent such as aluminum metal or a metallic refractory, or both, and to processes for their manufacture. More particularly, the invention concerns aluminum nitride-aluminum, aluminum nitride-refractory hard metal and aluminum nitride-aluminum-refractory hard metal cermets employed as cathode collector bars in electrolytic cells used for the production of aluminum.
- Aluminum metal is customarily produced by the electrolysis of alumina dissolved in molten cryolite in an electrolytic cell or pot.
- One form of such cell comprises a large tank lined with carbon which serves as the cathode and which contains the molten bath. Large carbon blocks inserted from the top act as the anode.
- Molten metallic aluminum collects at the bottom of the cell and is drained ofl? periodically. The liberated oxygen combines with the carbon at the anodes and passes off as carbon dioxide gas.
- the life of the carbon cell linings is short, and frequent shutdowns for repairs are necessary in commercial operation.
- the carbon linings act as conducting layers but the porous character of the carbon permits molten cryolite and other bath constituents to penetrate the lining with subsequent damage to the cell casing.
- Materials which have been proposed for such current collectors include the borldes, nitrides, and carbides of metals of Groups IV, V and VI of the Periodic System, particularly compounds of titanium and zirconium.
- solid bars of such materials are expensive, brittle and tend to crack and swell In use.
- aluminum, nitride-aluminum and other cermet materials which fully meet the aforesaid stringent requireice ments.
- These comprise consolidated mixtures of aluminum nitride as the ceramic constituent, together with a metal or metalloid constituent, or both, as the conductive component.
- Suitable metalloid constituents are the refractory hard metals (RHM) such as titanium diboride.
- RHM refractory hard metals
- the proportion of aluminum nitride in the composite should be kept below about 60% by weight, since a greater amount produces a very hard dense product which cannot be cut or abraded by ordinary metal working tools. Moreover, a greater proportion of aluminum nitride in the composite adversely affects its electrical conductivity, and may eliminate it completely.
- the preferred proportion of aluminum nitride lies between about 50% and about 60% by weight.
- the upper limit for aluminum content is set by the condition that the cermet should not collapse at 1000 C. (by melting of the metal), and by the amount of free or void space remaining in the aluminum nitride matrix after sintering.
- a preferred composite contains about 57% AlN and about 43 Al metal, by weight.
- the composite of aluminum nitride and aluminum powder may be prepared, according to the invention, by any of the methods commonly employed in the preparation of cermets, including hot pressing and sintering, cold pressing, and by impregnation of the aluminum nitride with liquid aluminum metal.
- hot pressing and sintering cold pressing
- the preferred method is hot pressing and sintering, and the invention will be described within the context of this method.
- the calculated proportions of atomized aluminum powder and aluminum nitride powder are mixed by shaking with glass or ceramic balls in a rotary mixer.
- the resulting dry, free flowing mixture is introduced into a conventional type of hot pressing die mounted in a press and surrounded by insulation and induction heating coils.
- the die is made of graphite, and the mixture is initially compressed to a compact at about 1000 pounds per square inch, using a'graphite plunger, but this pressure is exemplary only, and not critical. Where several compacts are to be simultaneously prepared, thin graphite spacing discs may be inserted between each charge.
- the pressure is applied to the charge until the temperature, monitored by an iridium, iridiumrhodium thermocouple, reaches 1200 C.
- the pressure is then increased to about 1600 pounds per square inch and the temperature maintained at about 1750 C.i50 C. for about 30 minutes.
- the system is then allowed to cool under pressure at 600 C., below the melting point of aluminum.
- An additional class of cermets produced in accordance with the present invention are composites of aluminum nitride and a refractory hard metal such as titanium di boride; and composites of aluminum nitride, titanium diboride (or other RHM) and aluminum.
- the ceramic component is the aluminum nitride, and the electrically conducting phases are the titanium diboride and alumi num.
- the proportion of aluminum nitride in the composite should be between about 60% and about 25% by weight, preferably 35-45 percent.
- the upper limit for the aluminum nitride is set by the number of randomly contiguous and interlocking titanium diboride particles and the lower limit by the strength imparted to the composite by reason of the sintering and bonding between contiguous aluminum nitride particles.
- the proportion of aluminum is determined by the free space or voids between the interlocking and sintered particles of aluminum nitride and titanium diboride. Characteristically, the proportion of aluminum is 0 to 15 weight percent aluminum.
- the entrapped and electrically conducting aluminum serves to improve and increase the random contacts between titanium diboride particles and hence, the total electrical conductivity of the composite.
- the aluminum occupies the free space (approximately 15% of the total volume) due to the microscopic voids between interlocking aluminum nitride and titanium diboride particles. Furthermore, the presence of aluminum in the composite improves the mechanical strength and the resistance to thermal shock.
- a preferred composite contains about 42% aluminum nitride and 58% titanium diboride, while a preferred composition for an electrically conducting aluminum nitride-titanium diboride-aluminum cermet is about 10. 8% A1, 37.4% AlN by weight, and the balance, TiB
- the composites of aluminum nitride-titanium diboride and aluminum nitride-titanium diboride-aluminum may be prepared according to the invention by any of the methods commonly used in the preparation of cermets including cold pressing; and subsequent sintering and hot pressing and sintering. Of these, the preferred method is hot pressing and sintering.
- the aluminum nitride-cntaining cermets thus produced withstand cryolite attack and provide material suitable for aluminum reduction cell collector bars.
- the bars are electrically conductive, hard, dense, and stable at 1000 C. Conductances in the order of five times that of graphite are obtained, and the compacts have good resistance to thermal shock.
- the bars conduct current effectively at the temperatures of operation of aluminum reduction cells, and they have expansivities compatible with the graphite and cryolite-alumina cathode linings.
- a strong bond between the cermet and graphite can be made which remains stable at 1000 C. This bond can be used in fabricating a carbon-cermet bar or in coating graphite.
- Example 1 A mixture of about 57.2% by weight of 200 mesh aluminum nitride and 42.8% aluminum powder (Grade 120 plus 17, atomized) was prepared and thoroughly blended by shaking in a container with glass balls. The dry, free-flowing mixture was charged into a cylindrical graphite die surrounded by insulation and induction heating coils, which unit was then mounted in a press with a graphite plunger so that the plunger and die provided an enclosed cavity containing the mixture. Pressure of 1000 p.s.i. was applied to the charge until the temperature (monitored by a thermocouple in the die wall) reached about 1200 C. The pressure was then raised to 1600 p.s.i., after which the temperature was increased to 1750 C., and these conditions were maintained for approximately 30 minutes.
- the density was found to be 2.38 (or about 81% of theoretical), and the conductance was approximately 600 mho-cm.
- the weight loss in conductivity tests carried on at 700 C. for 75 hours was 1.33 weight percent.
- Example 2 In the fabrication of an aluminum nitride-titanium diboride cermet, the calculated proportions of particles in the range of 200 to 5 micron size were mixed in a rotary mixer or ball mixer.
- the dry free-flowing powder was placed in a conventional type of hot pressing die mounted in a press and surrounded by a susceptor, insulation and induction heating coils.
- the die was constructed of graphite. Pressure was applied to about 1000 p.s.i. and maintained while the temperature of the preparation was increased to about 1200 C. Then the pressure was increased to about 1800-2000 p.s.i. and the temperature (monitored by an iridium-rhodium alloy thermocouple) raised to 1850 C. The temperature and pressure conditions were maintained for about thirty minutes.
- the system was allowed to cool under a pressure of 1000 p.s.i. to room temperature.
- the hard, dense rod can be extruded with the graphite plunger since there is no adhesion to the die walls.
- the resulting rod produced from a mixture of about 42%AlN-58% titanium diboride had a specific electrical resistivity of 1.42X10" ohm-cm, density 3.35 gm.- cm? and withstood molten aluminum and cryolite.
- Example 3 Other bars were prepared by cold pressing the desired mixtures of aluminum nitride-titanium diboride,
- Example 4 of the die since it did not adhere to the graphite Walls. Its density was found to be 3.50 (or about of theoretical) and its resistivity was 1.1 10 ohm-cm.
- An electrolytic cell for the production of aluminum having a cathode comprising a solid contact element consisting essentially of a compressed mixture of from about 25% to about 60% by weight of aluminum nitride, from about 40% to about 60% of titanium diboride, and up to about 15% aluminum.
- An electrolytic cell for the production of aluminum having a cathode collector bar comprising a solid contact element consisting essentially of a compressed and integrally bonded mixture of about 35-45% by weight of aluminum nitride, about 10% aluminum, the balance substantially titanium diboride.
- An electrolytic cell for the production of aluminum having a cathode collectorbar comprising a solid contact element consisting essentially of a compressed and sintered mixture of about 50% to about 60% by weight 6 of aluminum nitride and from about 40% to about 50% References Cited 5 1 1 l c tr l t c z cell for the production of aluminum UNITED STATES PATENTS n e e y 1 having a cathode collector bar comprising a solid con- 3011982 12/1961 Maduk et a1 204 291 X tact element consisting essentially of a compressed and 5 g 12/1961 Rlcker et 204*243 X sintered mixture of about 57% by weight of aluminum 15 615 11/1965 Ransley 204 279 nitride and about 43% by weight of aluminum metal.
- An electrolytic cell for the production of aluminum, FOREIGN PATENTS having a cathode comprising a solid contact element 251,641 8/1926 Great Britain.
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Description
United States Patent 3,328,280 ELECTRICALLY CUNDUCTWE CERNIET CQMPOSITHONS Nolan Earle Richards, Florence, Ala, James Simmons Berry, In, Savannah, Tenn, and Thomas Joseph Johnston, Muscle Shoals, Ala assignors to Reynolds Metals Company, Richmond, Va., a corporation of Delaware No Drawing. Filed Apr. 7, 1964, Ser. No. 358,068 6 Claims. (Cl. 204-243) ABSTRACT OF THE DISCLOURE Electrolytic cells for the production of aluminum, having a cathode contact element made essentially of about 25% to about 60% by weight of aluminum nitride and an electrically conductive constituent such as titanium diboride or aluminum or both aluminum and refractory hard metal.
This invention relates to novel cermets composed of aluminum nitride and an electrically conductive constituent such as aluminum metal or a metallic refractory, or both, and to processes for their manufacture. More particularly, the invention concerns aluminum nitride-aluminum, aluminum nitride-refractory hard metal and aluminum nitride-aluminum-refractory hard metal cermets employed as cathode collector bars in electrolytic cells used for the production of aluminum.
Aluminum metal is customarily produced by the electrolysis of alumina dissolved in molten cryolite in an electrolytic cell or pot. One form of such cell comprises a large tank lined with carbon which serves as the cathode and which contains the molten bath. Large carbon blocks inserted from the top act as the anode. Molten metallic aluminum collects at the bottom of the cell and is drained ofl? periodically. The liberated oxygen combines with the carbon at the anodes and passes off as carbon dioxide gas.
The life of the carbon cell linings is short, and frequent shutdowns for repairs are necessary in commercial operation. The carbon linings act as conducting layers but the porous character of the carbon permits molten cryolite and other bath constituents to penetrate the lining with subsequent damage to the cell casing. It is a desirable practice to employ current collectors made of materials which have good electrical conductivity but which are resistant to attack by bath constituents, and which extend into the molten aluminum layer on the bottom of the cell so as to minimize the fiow of electricity within the carbon layer. Materials which have been proposed for such current collectors include the borldes, nitrides, and carbides of metals of Groups IV, V and VI of the Periodic System, particularly compounds of titanium and zirconium. However, solid bars of such materials (and especially those of sufficient size to be practicable) are expensive, brittle and tend to crack and swell In use.
Experience has shown that among the prerequisites of a satisfactory material for collector bars in electrolytic reduction cells for aluminum production are: (a) the material should be hard and dense, (b) it should be an electrical conductor, (c) it should retain its dimensional stability at temperatures around 1000 C., and (d) it should be stable in contact with and resistant to attack by cryolite-alumina melts and liquid aluminum.
In accordance with the present invention, there are provided aluminum, nitride-aluminum and other cermet materials which fully meet the aforesaid stringent requireice ments. These comprise consolidated mixtures of aluminum nitride as the ceramic constituent, together with a metal or metalloid constituent, or both, as the conductive component. Suitable metalloid constituents are the refractory hard metals (RHM) such as titanium diboride. The proportion of aluminum nitride in the composite should be kept below about 60% by weight, since a greater amount produces a very hard dense product which cannot be cut or abraded by ordinary metal working tools. Moreover, a greater proportion of aluminum nitride in the composite adversely affects its electrical conductivity, and may eliminate it completely. In the case of AlN-Al cermets, the preferred proportion of aluminum nitride lies between about 50% and about 60% by weight. The upper limit for aluminum content is set by the condition that the cermet should not collapse at 1000 C. (by melting of the metal), and by the amount of free or void space remaining in the aluminum nitride matrix after sintering. A preferred composite contains about 57% AlN and about 43 Al metal, by weight.
The composite of aluminum nitride and aluminum powder may be prepared, according to the invention, by any of the methods commonly employed in the preparation of cermets, including hot pressing and sintering, cold pressing, and by impregnation of the aluminum nitride with liquid aluminum metal. Of these, the preferred method is hot pressing and sintering, and the invention will be described within the context of this method.
In the fabrication of aluminum nitride-aluminum bars by hot pressing and sintering, the calculated proportions of atomized aluminum powder and aluminum nitride powder are mixed by shaking with glass or ceramic balls in a rotary mixer. The resulting dry, free flowing mixture is introduced into a conventional type of hot pressing die mounted in a press and surrounded by insulation and induction heating coils. The die is made of graphite, and the mixture is initially compressed to a compact at about 1000 pounds per square inch, using a'graphite plunger, but this pressure is exemplary only, and not critical. Where several compacts are to be simultaneously prepared, thin graphite spacing discs may be inserted between each charge. The pressure is applied to the charge until the temperature, monitored by an iridium, iridiumrhodium thermocouple, reaches 1200 C. The pressure is then increased to about 1600 pounds per square inch and the temperature maintained at about 1750 C.i50 C. for about 30 minutes. The system is then allowed to cool under pressure at 600 C., below the melting point of aluminum.
An additional class of cermets produced in accordance with the present invention are composites of aluminum nitride and a refractory hard metal such as titanium di boride; and composites of aluminum nitride, titanium diboride (or other RHM) and aluminum. The ceramic component is the aluminum nitride, and the electrically conducting phases are the titanium diboride and alumi num. The proportion of aluminum nitride in the composite should be between about 60% and about 25% by weight, preferably 35-45 percent. The upper limit for the aluminum nitride is set by the number of randomly contiguous and interlocking titanium diboride particles and the lower limit by the strength imparted to the composite by reason of the sintering and bonding between contiguous aluminum nitride particles. The proportion of aluminum is determined by the free space or voids between the interlocking and sintered particles of aluminum nitride and titanium diboride. Characteristically, the proportion of aluminum is 0 to 15 weight percent aluminum. The entrapped and electrically conducting aluminum serves to improve and increase the random contacts between titanium diboride particles and hence, the total electrical conductivity of the composite. The aluminum occupies the free space (approximately 15% of the total volume) due to the microscopic voids between interlocking aluminum nitride and titanium diboride particles. Furthermore, the presence of aluminum in the composite improves the mechanical strength and the resistance to thermal shock.
A preferred composite contains about 42% aluminum nitride and 58% titanium diboride, while a preferred composition for an electrically conducting aluminum nitride-titanium diboride-aluminum cermet is about 10. 8% A1, 37.4% AlN by weight, and the balance, TiB
The composites of aluminum nitride-titanium diboride and aluminum nitride-titanium diboride-aluminum may be prepared according to the invention by any of the methods commonly used in the preparation of cermets including cold pressing; and subsequent sintering and hot pressing and sintering. Of these, the preferred method is hot pressing and sintering.
The aluminum nitride-cntaining cermets thus produced withstand cryolite attack and provide material suitable for aluminum reduction cell collector bars. The bars are electrically conductive, hard, dense, and stable at 1000 C. Conductances in the order of five times that of graphite are obtained, and the compacts have good resistance to thermal shock. The bars conduct current effectively at the temperatures of operation of aluminum reduction cells, and they have expansivities compatible with the graphite and cryolite-alumina cathode linings. A strong bond between the cermet and graphite can be made which remains stable at 1000 C. This bond can be used in fabricating a carbon-cermet bar or in coating graphite.
The practice of the invention is illustrated by the following examples, which are not, however, to be regarded as limiting:
Example 1 A mixture of about 57.2% by weight of 200 mesh aluminum nitride and 42.8% aluminum powder (Grade 120 plus 17, atomized) was prepared and thoroughly blended by shaking in a container with glass balls. The dry, free-flowing mixture was charged into a cylindrical graphite die surrounded by insulation and induction heating coils, which unit was then mounted in a press with a graphite plunger so that the plunger and die provided an enclosed cavity containing the mixture. Pressure of 1000 p.s.i. was applied to the charge until the temperature (monitored by a thermocouple in the die wall) reached about 1200 C. The pressure was then raised to 1600 p.s.i., after which the temperature was increased to 1750 C., and these conditions were maintained for approximately 30 minutes.
This procedure was found to produce a very satisfactory cermet material which was hard, uniformly sintered and conducting, and did not stick to the graphite die. The material maintained its structure at 1000 C. well above the operating temperature of an aluminum reduction cell and, indeed, above the melting point of aluminum.
The density was found to be 2.38 (or about 81% of theoretical), and the conductance was approximately 600 mho-cm. The weight loss in conductivity tests carried on at 700 C. for 75 hours was 1.33 weight percent.
In a thermal expansivity test determined over the temperature interval 25950 C., based on vitreous,
to hydrolyze in cold water. Thus, bars and other shapes can be safely stored and shipped without stringent protection from the atmosphere.
Example 2 In the fabrication of an aluminum nitride-titanium diboride cermet, the calculated proportions of particles in the range of 200 to 5 micron size were mixed in a rotary mixer or ball mixer. The dry free-flowing powder was placed in a conventional type of hot pressing die mounted in a press and surrounded by a susceptor, insulation and induction heating coils. The die was constructed of graphite. Pressure was applied to about 1000 p.s.i. and maintained while the temperature of the preparation was increased to about 1200 C. Then the pressure was increased to about 1800-2000 p.s.i. and the temperature (monitored by an iridium-rhodium alloy thermocouple) raised to 1850 C. The temperature and pressure conditions were maintained for about thirty minutes. The system was allowed to cool under a pressure of 1000 p.s.i. to room temperature. The hard, dense rod can be extruded with the graphite plunger since there is no adhesion to the die walls.
The resulting rod produced from a mixture of about 42%AlN-58% titanium diboride had a specific electrical resistivity of 1.42X10" ohm-cm, density 3.35 gm.- cm? and withstood molten aluminum and cryolite.
Example 3 Other bars were prepared by cold pressing the desired mixtures of aluminum nitride-titanium diboride,
aluminum nitride-titanium diboride-aluminum in a tool steel die at 208,000 p.s.i. The cold pressed bars were then sintered in a graphite die inductively heated at 1850 C. for 25 minutes. The hard, dense and electrically conducting bars had densities in the range 2.9 to 3.1.
Example 4 of the die, since it did not adhere to the graphite Walls. Its density was found to be 3.50 (or about of theoretical) and its resistivity was 1.1 10 ohm-cm.
While present preferred embodiments of the inven-. tion have been described, it will be apparent that the invention may be otherwise variously embodied and practiced within the scope of the following claims.
What is claimed is:
1. An electrolytic cell for the production of aluminum, having a cathode comprising a solid contact element consisting essentially of a compressed mixture of from about 25% to about 60% by weight of aluminum nitride, from about 40% to about 60% of titanium diboride, and up to about 15% aluminum.
2. An electrolytic cell according to claim 1, in which said contact element consists essentially of about 42% aluminum nitride and about 58% titanium diboride.
3. An electrolytic cell for the production of aluminum, having a cathode collector bar comprising a solid contact element consisting essentially of a compressed and integrally bonded mixture of about 35-45% by weight of aluminum nitride, about 10% aluminum, the balance substantially titanium diboride.
4. An electrolytic cell for the production of aluminum, having a cathode collectorbar comprising a solid contact element consisting essentially of a compressed and sintered mixture of about 50% to about 60% by weight 6 of aluminum nitride and from about 40% to about 50% References Cited 5 1 1 l c tr l t c z cell for the production of aluminum UNITED STATES PATENTS n e e y 1 having a cathode collector bar comprising a solid con- 3011982 12/1961 Maduk et a1 204 291 X tact element consisting essentially of a compressed and 5 g 12/1961 Rlcker et 204*243 X sintered mixture of about 57% by weight of aluminum 15 615 11/1965 Ransley 204 279 nitride and about 43% by weight of aluminum metal.
6. An electrolytic cell for the production of aluminum, FOREIGN PATENTS having a cathode comprising a solid contact element 251,641 8/1926 Great Britain.
consisting essentially of a compressed mixture of from 10 about to about 60% by weight of aluminum nitride, JOHN H ACK P a E from about to about of refractory hard metal, M "m U xammer' and about 10% aluminum. D. R. JORDAN, Assistant Examiner.
Claims (1)
1. AN ELECTROLYTIC CELL FOR THE PRODUCTION OF ALUMINUM, HAVING A CATHODE COMPRISING A SOLID CONTACT ELEMENT CONSISTING ESSENTIALLY OF A COMPRESSED MIXTURE OF FROM ABOUT 25% TO ABOUT 60% BY WEIGHT OF ALUMINUM NITRIDE, FROM ABOUT 40% TO ABOUT 60% OF TITANIUM DIBORIDE, AND UP TO ABOUT 15% ALUMINUM.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US358068A US3328280A (en) | 1964-04-07 | 1964-04-07 | Electrically conductive cermet compositions |
| GB13713/65A GB1083401A (en) | 1964-04-07 | 1965-03-31 | Electrically conductive cermet compositions |
| GB13544/67A GB1097000A (en) | 1964-04-07 | 1965-03-31 | Electrically conductive cermet compositions |
| US649757A US3408312A (en) | 1964-04-07 | 1967-05-03 | Electrically conductive cermet compositions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US358068A US3328280A (en) | 1964-04-07 | 1964-04-07 | Electrically conductive cermet compositions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3328280A true US3328280A (en) | 1967-06-27 |
Family
ID=23408157
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US358068A Expired - Lifetime US3328280A (en) | 1964-04-07 | 1964-04-07 | Electrically conductive cermet compositions |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US3328280A (en) |
| GB (2) | GB1097000A (en) |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3408312A (en) * | 1964-04-07 | 1968-10-29 | Reynolds Metals Co | Electrically conductive cermet compositions |
| US4333813A (en) * | 1980-03-03 | 1982-06-08 | Reynolds Metals Company | Cathodes for alumina reduction cells |
| WO1983000171A1 (en) * | 1981-07-01 | 1983-01-20 | De Nora, Vittorio | Electrolytic production of aluminum |
| WO1983004271A1 (en) * | 1982-06-03 | 1983-12-08 | Great Lakes Carbon Corporation | Cathodic component for aluminum reduction cell |
| US4443314A (en) * | 1983-03-16 | 1984-04-17 | Great Lakes Carbon Corporation | Anode assembly for molten salt electrolysis |
| WO1984002723A1 (en) * | 1982-12-30 | 1984-07-19 | Eltech Systems Corp | Aluminum production cell components |
| US4514268A (en) * | 1982-12-30 | 1985-04-30 | Corning Glass Works | Electrolytic Al production with reaction sintered cermet component |
| US4534835A (en) * | 1982-12-30 | 1985-08-13 | Corning Glass Works | Electrolytic Al production with reaction sintered multiphase ceramic |
| EP0115177A3 (en) * | 1982-12-30 | 1986-06-11 | Corning Glass Works | Reaction sintered multiphase ceramic body and use thereof in electrolytic cell in aluminum production |
| EP0117366A3 (en) * | 1982-12-30 | 1986-07-02 | Alcan International Limited | Refractory lining material for electrolytic reduction cell for aluminium production and method of making the same |
| US4876941A (en) * | 1987-12-31 | 1989-10-31 | Eltech Systems Corporation | Composite for protection against armor-piercing projectiles |
| WO1991012350A1 (en) * | 1990-02-15 | 1991-08-22 | Sinvent As | Method for the preparation of articles of composite materials |
| US6132574A (en) * | 1997-05-30 | 2000-10-17 | Aluminium-Salzschalcke Aufbereitungs Gmbh | Bottom lining for electrolytic cells and process for its manufacture |
| CN103484893A (en) * | 2012-06-11 | 2014-01-01 | 内蒙古联合工业有限公司 | Novel electrolytic bath for aluminum electrolysis and electrolysis technology thereof |
| CN103484894B (en) * | 2012-06-11 | 2016-08-17 | 内蒙古联合工业有限公司 | A kind of electrolgtic aluminium inert cathode and preparation method thereof |
| EP4407073A1 (en) * | 2023-01-27 | 2024-07-31 | Vsca As | Cathode component for an electrolytic aluminium production cell |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB8926164D0 (en) * | 1989-11-20 | 1990-01-10 | Rtz Chemicals Borides Limited | Process for the production of refractory composite article |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB251641A (en) * | 1925-05-04 | 1926-08-12 | Henri Dolter | |
| US3011983A (en) * | 1959-03-16 | 1961-12-05 | Aluminum Co Of America | Refractory and method of making the same |
| US3011982A (en) * | 1959-02-04 | 1961-12-05 | Aluminum Co Of America | Refractory and method of making the same |
| US3215615A (en) * | 1951-05-04 | 1965-11-02 | British Aluminium Co Ltd | Current conducting element for aluminum production cells |
-
1964
- 1964-04-07 US US358068A patent/US3328280A/en not_active Expired - Lifetime
-
1965
- 1965-03-31 GB GB13544/67A patent/GB1097000A/en not_active Expired
- 1965-03-31 GB GB13713/65A patent/GB1083401A/en not_active Expired
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB251641A (en) * | 1925-05-04 | 1926-08-12 | Henri Dolter | |
| US3215615A (en) * | 1951-05-04 | 1965-11-02 | British Aluminium Co Ltd | Current conducting element for aluminum production cells |
| US3011982A (en) * | 1959-02-04 | 1961-12-05 | Aluminum Co Of America | Refractory and method of making the same |
| US3011983A (en) * | 1959-03-16 | 1961-12-05 | Aluminum Co Of America | Refractory and method of making the same |
Cited By (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3408312A (en) * | 1964-04-07 | 1968-10-29 | Reynolds Metals Co | Electrically conductive cermet compositions |
| US4333813A (en) * | 1980-03-03 | 1982-06-08 | Reynolds Metals Company | Cathodes for alumina reduction cells |
| WO1983000171A1 (en) * | 1981-07-01 | 1983-01-20 | De Nora, Vittorio | Electrolytic production of aluminum |
| EP0072043A1 (en) * | 1981-07-01 | 1983-02-16 | Eltech Systems Corporation | Electrolytic production of aluminum |
| US4650552A (en) * | 1981-07-01 | 1987-03-17 | Eltech Systems Corporation | Electrolytic production of aluminum |
| US4526669A (en) * | 1982-06-03 | 1985-07-02 | Great Lakes Carbon Corporation | Cathodic component for aluminum reduction cell |
| WO1983004271A1 (en) * | 1982-06-03 | 1983-12-08 | Great Lakes Carbon Corporation | Cathodic component for aluminum reduction cell |
| EP0115177A3 (en) * | 1982-12-30 | 1986-06-11 | Corning Glass Works | Reaction sintered multiphase ceramic body and use thereof in electrolytic cell in aluminum production |
| US4514268A (en) * | 1982-12-30 | 1985-04-30 | Corning Glass Works | Electrolytic Al production with reaction sintered cermet component |
| EP0115742A1 (en) * | 1982-12-30 | 1984-08-15 | Eltech Systems Corporation | Aluminum production cell components |
| US4534835A (en) * | 1982-12-30 | 1985-08-13 | Corning Glass Works | Electrolytic Al production with reaction sintered multiphase ceramic |
| WO1984002723A1 (en) * | 1982-12-30 | 1984-07-19 | Eltech Systems Corp | Aluminum production cell components |
| EP0117366A3 (en) * | 1982-12-30 | 1986-07-02 | Alcan International Limited | Refractory lining material for electrolytic reduction cell for aluminium production and method of making the same |
| US4600481A (en) * | 1982-12-30 | 1986-07-15 | Eltech Systems Corporation | Aluminum production cell components |
| WO1984003721A1 (en) * | 1983-03-16 | 1984-09-27 | Great Lakes Carbon Corp | Anode assembly for molten salt electrolysis |
| US4443314A (en) * | 1983-03-16 | 1984-04-17 | Great Lakes Carbon Corporation | Anode assembly for molten salt electrolysis |
| US4876941A (en) * | 1987-12-31 | 1989-10-31 | Eltech Systems Corporation | Composite for protection against armor-piercing projectiles |
| WO1991012350A1 (en) * | 1990-02-15 | 1991-08-22 | Sinvent As | Method for the preparation of articles of composite materials |
| US6132574A (en) * | 1997-05-30 | 2000-10-17 | Aluminium-Salzschalcke Aufbereitungs Gmbh | Bottom lining for electrolytic cells and process for its manufacture |
| CN103484893A (en) * | 2012-06-11 | 2014-01-01 | 内蒙古联合工业有限公司 | Novel electrolytic bath for aluminum electrolysis and electrolysis technology thereof |
| CN103484894B (en) * | 2012-06-11 | 2016-08-17 | 内蒙古联合工业有限公司 | A kind of electrolgtic aluminium inert cathode and preparation method thereof |
| CN103484893B (en) * | 2012-06-11 | 2016-09-07 | 内蒙古联合工业有限公司 | A kind of electrolgtic aluminium electrolytic cell and electrolysis process thereof |
| EP4407073A1 (en) * | 2023-01-27 | 2024-07-31 | Vsca As | Cathode component for an electrolytic aluminium production cell |
| WO2024156802A1 (en) * | 2023-01-27 | 2024-08-02 | Vsca As | Cathode component for an electrolytic aluminium production cell |
Also Published As
| Publication number | Publication date |
|---|---|
| GB1083401A (en) | 1967-09-13 |
| GB1097000A (en) | 1967-12-29 |
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