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US3328280A - Electrically conductive cermet compositions - Google Patents

Electrically conductive cermet compositions Download PDF

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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
aluminum nitride
titanium diboride
weight
graphite
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US358068A
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Richards Nolan Earle
Jr James Simmons Berry
Johnston Thomas Joseph
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Reynolds Metals Co
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Reynolds Metals Co
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Priority to US358068A priority Critical patent/US3328280A/en
Priority to GB13713/65A priority patent/GB1083401A/en
Priority to GB13544/67A priority patent/GB1097000A/en
Priority to US649757A priority patent/US3408312A/en
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    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/64Burning or sintering processes
    • C04B35/645Pressure sintering
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/515Shaped 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
    • C04B35/58Shaped 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
    • C04B35/5805Shaped 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
    • C04B35/58064Shaped 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
    • C04B35/58071Shaped 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
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/515Shaped 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
    • C04B35/58Shaped 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
    • C04B35/581Shaped 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
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C29/00Alloys based on carbides, oxides, nitrides, borides, or silicides, e.g. cermets, or other metal compounds, e.g. oxynitrides, sulfides
    • C22C29/14Alloys based on carbides, oxides, nitrides, borides, or silicides, e.g. cermets, or other metal compounds, e.g. oxynitrides, sulfides based on borides
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/16Electric current supply devices, e.g. bus bars
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B1/00Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F2998/00Supplementary 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.
US358068A 1964-04-07 1964-04-07 Electrically conductive cermet compositions Expired - Lifetime US3328280A (en)

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

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Cited By (16)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

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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

Patent Citations (4)

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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)

* Cited by examiner, † Cited by third party
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

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GB1097000A (en) 1967-12-29

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