US3268304A - Cellular metal and method of making - Google Patents

Cellular metal and method of making Download PDF

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US3268304A
US3268304A US33456463A US3268304A US 3268304 A US3268304 A US 3268304A US 33456463 A US33456463 A US 33456463A US 3268304 A US3268304 A US 3268304A
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aluminum
metal
coating
particles
coated
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Leonard M Vaught
James H Enos
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Dow Chemical Co
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Dow Chemical Co
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/10Alloys containing non-metals
    • C22C1/1005Pretreatment of the non-metallic additives
    • 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
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/10Sintering only
    • B22F3/11Making porous workpieces or articles
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/10Alloys containing non-metals
    • C22C1/1036Alloys containing non-metals starting from a melt
    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12014All metal or with adjacent metals having metal particles
    • Y10T428/12153Interconnected void structure [e.g., permeable, etc.]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12479Porous [e.g., foamed, spongy, cracked, etc.]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/249921Web or sheet containing structurally defined element or component

Definitions

  • This invention relates to cellular metal and to a method for making the same and, more particularly, is concerned with a novel process for preparing void-containing structures of aluminum.
  • An additional object is to provide an aluminum base, open-void, cellular structure of relatively uniform cell size whose cells may be conveniently controlled by feed stock selection.
  • a further object is to provide a novel process for preparing an aluminum oxide-coated aluminum cellular structure.
  • Still another object is to provide an aluminum nitridecoated aluminum cellular structure and a method for its preparation.
  • the present invention comprises coating a metal particle with a material which has a substantially higher melting point than the metal particle itself by heating the metal and a second material to a temperature below the melting point of the metal particle thereby to provide a coating of the reaction product of said metal and said second material on said metal.
  • the so-coated metal particle is subsequently heated to a temperature above the melting point of the metal.
  • the pressure on the coating of said particle is reduced While maintaining the metal at a temperature where it is molten thereby rupturing the surface coating on the particle and allowing at least a portion of the molten metal therein to flow out from the interior of the coated particle thus creating a void space within the coating, i.e., forming a hollow cell.
  • Cell size of the cellular structure so formed by the process of the present invention is dependent on the size of metal particles employed.
  • metal particles e.g., powders
  • the surface tension of the molten metal may prevent its escape from the coating.
  • large particles as the metal core melts, the coating itself may collapse and no voids or cells are formed.
  • this void-containing product can be prepared as freeflo'win-g individual cells by substantial elimination of all the interstitial aluminum, which provides the cementing action joining the cells in the unitized cellular structure, from the external surfaces of the particle. Removal of a large portion of molten metal from the exterior of the ruptured cells can be readily achieved if agitation is applied during the cell-forming stage to shake the molten metal down. In addition, centrifugal force may be used to help separate the molten metal from the coated surface.
  • an aluminum nitride-coated aluminum cellular structure is obtained by placing particulate aluminum having a particle size within the range of from about 50 to about 4 mesh,
  • the aluminum nitride coating on the particles ruptures and molten aluminum flows out of the ruptured aluminum nitride coating. A part of this molten aluminum is retained in the interstices between the aluminum nitride-coated aluminum particles; the remainder flows to the bottom of the reactor vessel.
  • the temperature of the charge is reduced below the melting point of aluminum thereby providing an aluminum nitridecoated aluminum cellular metal structure.
  • Total shell thickness of the aluminum nitride-coated cells ordinarily ranges from 0.01 inch to 0.014 inch. This cellular structure readily can be separated from the substantially solid mass of aluminum in the bottom of the reactor.
  • Aluminum nitride is not stable in air or water and forms aluminum oxide and ammonia when exposed thereto. Therefore, as the so-formed cellular product is contacted with the normal atmosphere, reaction with aluminum nitride occurs thus giving a cellular product in the form of an aluminum oxide-coated aluminum cellular metal.
  • the rate of heating is controlled such that the reaction of aluminum and nitrogen ordinarily occurs within about 4 to about 20 minutes from the time heat is first applied and in any event, is such that formation of the aluminum nitride coating substantially is complete before the temperature reaches the melting point of the aluminum metal.
  • Nitrogen need be present only in amounts stoichiometrically needed to react with aluminum to form a substantially continuous surface coating of aluminum nitride on the particle. However, nitrogen in excess of this amount ordinarily is used as this assures formation of the desired coating and produces no detrimental eiiects in the operation of the instant invention.
  • substantially all metals which react with a second material to form a coating on said metal, said coating having a higher melting point then said metal, can be used in the instant method.
  • the term metal, as used here, is meant to include both the metallic element itself as well as alloys thereof.
  • Other materials which can be used to react with the metal particles of aluminum or magnesium to form a coating on said metal particle include, for example, iammonia to form a nitride coating; oxygen or water vapor to form an oxide coating; carbon dioxide to form an oxide coating on magnesium; sulfur-containing compounds to form sulfide coatings; and borax and other boron oxide source materials to form an oxide coating. Additional silicate-forming, sulfite-forming and sulfateforming materials can be used. With gaseous materials, the reactant can be passed between the particulate coatinducing metal .as described hereinbefore. With solid reactants, conveniently these can be blended with the particulate metal prior to heating to provide a mixture wherein the metal and coating material are in close contact. With such material, the total amount of coating material is to be less than that which reacts, on a stoichiometric basis, with all of the metal present.
  • the cellular structure of the instant invention finds utility as a sandwich core material wherein strength and lightness are desired, for example, for use in automobiles, aircraft, ships and the like.
  • this cellular structure may be used as a metallic filter which would have great particle retention power due to the large void volumes in such a filter.
  • Example I About 10 grams of particulated (-6/ +8 mesh, U.S.
  • tandard Sieve aluminum was placed in a crucible which was, in turn, placed in a vacuum furnace (3 kw. unit). The furnace was filled with nitrogen. The aluminum charge was heated within a 20 minute period to about 1100 C. range and held at that temperature for about 50 minutes. During this period, no molten metal was observed in the crucible, thereby indicating formation of an enveloping nitride coating on the surface of each of the particles. The furnace was de-energized and the pressure reduced to about 30 millimeters mercury absolute for about a 90 second period. The weight of the molten aluminum metal inside the sphere along with the decrease in external pressure burst holes in the shell wall of the particles. This molten metal flowed to the bottom of the charge.
  • the pressure was raised to about atmospheric and the temperature reduced to below the melting point of aluminum.
  • About 6 grams of residual metal in the form of an apparently solid mass remained in the bottom of the crucible.
  • the aluminum nitride-coated structure was separated from the residual solid residue. When contacted with water or air, this structure gave off ammonia indicating reaction with the aluminum nitride and formation of an oxide surface coating.
  • the cell wall did not disintegrate which indicated that a substantial percent of the shell is aluminum metal.
  • Example II In order to show that reactants other than nitrogen alone may be used in the method of this invention, a thoroughly mixed combination of about 10 grams of aluminum powder of 6/ +8 mesh size and about 5 grams of a mixture containing about 67 percent by weight H 80 about 18 percent by weight B and about 15 percent by weight Na B O- were placed in a crucible which was, in turn, placed in a vacuum furnace and heated at about atmospheric pressure from ambient temperature to about 850 C. over a period of 25 minutes in a nitrogen atmosphere. Following this heating, a reduced pressure of about 75 millimeters mercury absolute was pulled on the vessel during a 50 second period. At these conditions, the molten aluminum broke through the nitride shell of the particles and flowed downward to the bottom of the crucible. The residual void containing particles were substantially freeflowing and not cemented together.
  • Example III About 10 grams of particulated aluminum (-8/ +20 mesh) and grams of borax were placed in a crucible and thoroughly mixed. The crucible was then placed in a vacuum furnace. The furnace was filled with argon. The charge was then heated within a 30 minute period to about 800 C. The temperature in the furnace was then allowed to drop to 750 C. over a period of 15 minutes. The furnace pressure was reduced to about 50 mm. Hg whereupon the particles burst and molten aluminum gravity flowed to the bottom of the vessel.
  • particulate metal is aluminum and has a particle size within the range of from about 50 to about 4 mesh, US. Standard Sieve, and the second material is nitrogen.

Description

United States Patent 3,268,304 CELLULAR METAL AND METHOD OF MAKING Leonard M. Vaught, Lake Jackson, and James H. Enos,
Angleton, Tern, assignors to The Dow Chemical Company, Midland, Micln, a corporation of Delaware N0 Drawing. Filed Dec. 30, 1963, Ser. No. 334,564 6 Claims. (Cl. 29-183) This invention relates to cellular metal and to a method for making the same and, more particularly, is concerned with a novel process for preparing void-containing structures of aluminum.
It is an object of the instant invention to provide a novel process for preparing light weight, strong, cellular metals.
An additional object is to provide an aluminum base, open-void, cellular structure of relatively uniform cell size whose cells may be conveniently controlled by feed stock selection.
A further object is to provide a novel process for preparing an aluminum oxide-coated aluminum cellular structure.
Still another object is to provide an aluminum nitridecoated aluminum cellular structure and a method for its preparation.
Other objects and advantages Will become apparent from reading the detailed description of the invention disclosed hereinafter.
In general, the present invention comprises coating a metal particle with a material which has a substantially higher melting point than the metal particle itself by heating the metal and a second material to a temperature below the melting point of the metal particle thereby to provide a coating of the reaction product of said metal and said second material on said metal. The so-coated metal particle is subsequently heated to a temperature above the melting point of the metal. The pressure on the coating of said particle is reduced While maintaining the metal at a temperature where it is molten thereby rupturing the surface coating on the particle and allowing at least a portion of the molten metal therein to flow out from the interior of the coated particle thus creating a void space within the coating, i.e., forming a hollow cell.
Cell size of the cellular structure so formed by the process of the present invention is dependent on the size of metal particles employed. With extremely small particles of metal, e.g., powders, the surface tension of the molten metal may prevent its escape from the coating. With large particles, as the metal core melts, the coating itself may collapse and no voids or cells are formed. For optimum performance, particles in the size range of from about 4 to about 50 mesh, U.S. Standard Sieve, ordinarily are used. However, particles somewhat larger and smaller than from 4 to 50 mesh, U.S. Standard Sieve can satisfactorily be employed.
Although the resulting product ordinarily consists of a cellular structure having open, interconnected cells and a metal matrix coated with the high melting surface coating, this void-containing product can be prepared as freeflo'win-g individual cells by substantial elimination of all the interstitial aluminum, which provides the cementing action joining the cells in the unitized cellular structure, from the external surfaces of the particle. Removal of a large portion of molten metal from the exterior of the ruptured cells can be readily achieved if agitation is applied during the cell-forming stage to shake the molten metal down. In addition, centrifugal force may be used to help separate the molten metal from the coated surface.
In practicing one variation of the invention, an aluminum nitride-coated aluminum cellular structure is obtained by placing particulate aluminum having a particle size within the range of from about 50 to about 4 mesh,
"ice
U.S. Standard Sieve, in a vessel or reactor which permits gas flow around and between the particles. This metal is controllably heated to a temperature above about 660 C. and below the melting point of aluminum nitride (about 2000 C.), with a preferred temperature being about 800 C., in a nitrogen atmosphere at about at-mospheric pressure, employing a rate of heating such that a coating of aluminum nitride forms on the particulate aluminum prior to the metal reaching its melting point, i.e., about 660 C. When the temperature of the coated pellets reaches the predetermined operating temperature range, the pressure on the entire charge in the furnace is reduced to an absolute pressure of from about 730 millimeters mercury to about 0.001 millimeter mercury. As the pressure is reduced, the aluminum nitride coating on the particles ruptures and molten aluminum flows out of the ruptured aluminum nitride coating. A part of this molten aluminum is retained in the interstices between the aluminum nitride-coated aluminum particles; the remainder flows to the bottom of the reactor vessel. The temperature of the charge is reduced below the melting point of aluminum thereby providing an aluminum nitridecoated aluminum cellular metal structure. Total shell thickness of the aluminum nitride-coated cells ordinarily ranges from 0.01 inch to 0.014 inch. This cellular structure readily can be separated from the substantially solid mass of aluminum in the bottom of the reactor.
Aluminum nitride is not stable in air or water and forms aluminum oxide and ammonia when exposed thereto. Therefore, as the so-formed cellular product is contacted with the normal atmosphere, reaction with aluminum nitride occurs thus giving a cellular product in the form of an aluminum oxide-coated aluminum cellular metal.
The rate of heating is controlled such that the reaction of aluminum and nitrogen ordinarily occurs within about 4 to about 20 minutes from the time heat is first applied and in any event, is such that formation of the aluminum nitride coating substantially is complete before the temperature reaches the melting point of the aluminum metal.
Nitrogen need be present only in amounts stoichiometrically needed to react with aluminum to form a substantially continuous surface coating of aluminum nitride on the particle. However, nitrogen in excess of this amount ordinarily is used as this assures formation of the desired coating and produces no detrimental eiiects in the operation of the instant invention.
In general, substantially all metals which react with a second material to form a coating on said metal, said coating having a higher melting point then said metal, can be used in the instant method.
Examples of other metals which can be used in the instant invention include, for example, magnesium, tin, zinc, lead, copper and iron. The term metal, as used here, is meant to include both the metallic element itself as well as alloys thereof.
Other materials which can be used to react with the metal particles of aluminum or magnesium to form a coating on said metal particle include, for example, iammonia to form a nitride coating; oxygen or water vapor to form an oxide coating; carbon dioxide to form an oxide coating on magnesium; sulfur-containing compounds to form sulfide coatings; and borax and other boron oxide source materials to form an oxide coating. Additional silicate-forming, sulfite-forming and sulfateforming materials can be used. With gaseous materials, the reactant can be passed between the particulate coatinducing metal .as described hereinbefore. With solid reactants, conveniently these can be blended with the particulate metal prior to heating to provide a mixture wherein the metal and coating material are in close contact. With such material, the total amount of coating material is to be less than that which reacts, on a stoichiometric basis, with all of the metal present.
The cellular structure of the instant invention finds utility as a sandwich core material wherein strength and lightness are desired, for example, for use in automobiles, aircraft, ships and the like. In addition, this cellular structure may be used as a metallic filter which would have great particle retention power due to the large void volumes in such a filter.
The following examples are merely illustrative of the invention and are in no way meant to limit it thereto.
Example I About 10 grams of particulated (-6/ +8 mesh, U.S.
tandard Sieve) aluminum was placed in a crucible which was, in turn, placed in a vacuum furnace (3 kw. unit). The furnace was filled with nitrogen. The aluminum charge was heated within a 20 minute period to about 1100 C. range and held at that temperature for about 50 minutes. During this period, no molten metal was observed in the crucible, thereby indicating formation of an enveloping nitride coating on the surface of each of the particles. The furnace was de-energized and the pressure reduced to about 30 millimeters mercury absolute for about a 90 second period. The weight of the molten aluminum metal inside the sphere along with the decrease in external pressure burst holes in the shell wall of the particles. This molten metal flowed to the bottom of the charge. The pressure was raised to about atmospheric and the temperature reduced to below the melting point of aluminum. This produced a unitized cellular structure having interconnected cells which weighed only about 4 grams. About 6 grams of residual metal in the form of an apparently solid mass remained in the bottom of the crucible. The aluminum nitride-coated structure was separated from the residual solid residue. When contacted with water or air, this structure gave off ammonia indicating reaction with the aluminum nitride and formation of an oxide surface coating. The cell wall did not disintegrate which indicated that a substantial percent of the shell is aluminum metal.
Example II In order to show that reactants other than nitrogen alone may be used in the method of this invention, a thoroughly mixed combination of about 10 grams of aluminum powder of 6/ +8 mesh size and about 5 grams of a mixture containing about 67 percent by weight H 80 about 18 percent by weight B and about 15 percent by weight Na B O- were placed in a crucible which was, in turn, placed in a vacuum furnace and heated at about atmospheric pressure from ambient temperature to about 850 C. over a period of 25 minutes in a nitrogen atmosphere. Following this heating, a reduced pressure of about 75 millimeters mercury absolute was pulled on the vessel during a 50 second period. At these conditions, the molten aluminum broke through the nitride shell of the particles and flowed downward to the bottom of the crucible. The residual void containing particles were substantially freeflowing and not cemented together.
About 90 percent of the resulting particles were hollow and had about a 0.013 inch wall thickness. The material was not as reactive when brought into contact with water which indicated that the aforementioned boron oxide-containing materials had reacted with the aluminum to form aluminum oxide which became a part of the shell.
Example III About 10 grams of particulated aluminum (-8/ +20 mesh) and grams of borax were placed in a crucible and thoroughly mixed. The crucible was then placed in a vacuum furnace. The furnace was filled with argon. The charge was then heated within a 30 minute period to about 800 C. The temperature in the furnace was then allowed to drop to 750 C. over a period of 15 minutes. The furnace pressure was reduced to about 50 mm. Hg whereupon the particles burst and molten aluminum gravity flowed to the bottom of the vessel.
When the material was cooled below the melting point of aluminum, a cellular structure composed of hollow spheres of aluminum coated with said aluminum oxide was obtained.
In a manner similar to the foregoing examples, cellular structures of magnesium, tin, zinc, lead, copper and iron coated with various second materials having a higher melting point than the base itself can be obtained.
Various modifications may be made in the present invention without departing from the spirit or scope thereof, and it is to be understood that we limit ourselve only as defined in the appended claims.
What is claimed is:
1. The method of making a cellular met-a1 structure which comprises:
(a) reacting a particulate metal with a second material at a temperature below the melting point of the metal particle to provide a coating of the reaction product of said metal and said second material on said metal, said coating having a substantially higher melting point than the metal particle; V
(b) heating the so-coated particulate metal to a temperature above the melting point of said metal but below the melting point of said coating;
(c) reducing the external pressure on the coated surface of said metal thereby rupturing the coating;
(d) allowing a portion of molten metal to flow out of the coating through the ruptures of said coating thus creating a void space within the coating; and
(e) cooling the residual void-containing structure of said metal and said coating material below the melting point of said metal.
2. The method in accordance with claim 1 wherein the particulate metal is aluminum and has a particle size within the range of from about 50 to about 4 mesh, US. Standard Sieve, and the second material is nitrogen.
3. The method of making an aluminum nitride-coated aluminum cellular structure which comprises:
(a) heating aluminum particles having a particle size within the range of from about 50 to about 4 mesh, US. Standard Sieve, to a temperature below about 660 C. in a nitrogen atmosphere thereby coating the aluminum particles with aluminum nitride;
(b) heating said coated aluminum particles to a temperature above about 660 C. and below about about 2000 C. thereby melting the aluminum within said coating;
(c) reducing the external pressure on said coated aluminum particles and rupturing the coating;
(d) allowing a portion of the molten aluminum from the interior of said coated particles to flow through the rupture in said coating, thereby creating a voided space within said coating; and
(e) cooling the residual void containing aluminum nitride-coated aluminum cellular structure below 660 C.
4. The method in accordance with claim 3 and including the step of exposing the aluminum nitride-coated aluminum cellular structure to the atmosphere.
5'. The method of making an aluminum oxide-coated aluminum cellular structure which comprises:
(a) admixing aluminum particles having a particle size within the range of from about 50 to about 4 mesh, U.S. Standard Sieve, with a quantity of a boron oxide-containing material which is less than that stoichiometrically needed to react with said (f) cooling the residual void containing aluminum aluminum; oxide-coated aluminum structure below 660 C. (b) heating the above admixture to a temperature 6. An article of manufacture comprising a cellular below about 660 C. thereby coating t e alllmimetal structure composed of cells of aluminum nitridenum particles with aluminum oxide; 5 o t d alumi (c) heating said coated aluminum particles to a temperature above about 660 C. and below about References Cited by the Examiner 2050 C. thereby melting the aluminum within said UNITED STATES PATENTS coating; (d) reducing the pressure on said oxide coating there- 10 2,434,775 1/1948 Sosnick 29-192 by rupturing the coating; 2,985,411 5/1961 Madden 29192 (e) allowing a portion of the molten aluminum to 3,135,044 6/1964 M 75 2() flow through said oxide coating through the rupture in said coating thereby creating a void space HYLAND BIZOT, Primary Examiner. within said coating; and 15

Claims (1)

  1. 6. AN ARTICLE OF MANUFACTURE COMPRISING A CELLULAR METAL STRUCTURE COMPOSED OF CELLS OF ALUMINUM NITRIDECOATED ALUMINUM.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3448513A (en) * 1966-02-02 1969-06-10 Dow Chemical Co Method for making long holes in foam bodies
US3839080A (en) * 1971-06-21 1974-10-01 Ethyl Corp Plastic coated metallic foams
US20110274942A1 (en) * 2010-04-13 2011-11-10 Alcoa Inc. Corrosion resistant aluminum foam products

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434775A (en) * 1943-05-08 1948-01-20 Sosnick Benjamin Process for making foamlike mass of metal
US2985411A (en) * 1957-06-25 1961-05-23 Jr Baxter C Madden Structural element having sphericallike filling
US3135044A (en) * 1959-06-04 1964-06-02 United Aircraft Corp Lightwight porous structures and methods of making same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434775A (en) * 1943-05-08 1948-01-20 Sosnick Benjamin Process for making foamlike mass of metal
US2985411A (en) * 1957-06-25 1961-05-23 Jr Baxter C Madden Structural element having sphericallike filling
US3135044A (en) * 1959-06-04 1964-06-02 United Aircraft Corp Lightwight porous structures and methods of making same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3448513A (en) * 1966-02-02 1969-06-10 Dow Chemical Co Method for making long holes in foam bodies
US3839080A (en) * 1971-06-21 1974-10-01 Ethyl Corp Plastic coated metallic foams
US20110274942A1 (en) * 2010-04-13 2011-11-10 Alcoa Inc. Corrosion resistant aluminum foam products

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