US3131049A - Production of chromium lamella on a molten supporting vehicle - Google Patents
Production of chromium lamella on a molten supporting vehicle Download PDFInfo
- Publication number
- US3131049A US3131049A US253756A US25375663A US3131049A US 3131049 A US3131049 A US 3131049A US 253756 A US253756 A US 253756A US 25375663 A US25375663 A US 25375663A US 3131049 A US3131049 A US 3131049A
- Authority
- US
- United States
- Prior art keywords
- chromium
- molten
- lamella
- metallo
- supporting vehicle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/003—Coating on a liquid substrate
-
- 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
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/16—Making metallic powder or suspensions thereof using chemical processes
- B22F9/30—Making metallic powder or suspensions thereof using chemical processes with decomposition of metal compounds, e.g. by pyrolysis
- B22F9/305—Making metallic powder or suspensions thereof using chemical processes with decomposition of metal compounds, e.g. by pyrolysis of metal carbonyls
Definitions
- Chromium lamella have been unavailable for commercial use because of the inability to produce the lamella 'with a small cross sectional area and the desired physical properties required by the electronics, paint, etc., indus- This close packed crystal structure of chromium which permits a minimum absorption of distortional energy before the lattice ruptures.
- Foils of many metals are mechanically produced by and ingots these mechanical processes the decrease in thickness of the element is accompanied by a storing of distortional energywhich manifests itself as stresses within the material.
- Chromium is not readily amenable to treatment by mechanical means because the slight ability of the metal to absorb distortional stress without fracture is completely exploited before the cross-section is reduced to a dimension small enough for commercial value.
- chromium lamella Prior to the inception of the present invention, chromium lamella could not be manufactured in thickness of less than 0.015 inch. This minimum thickness was accompanied by brittleness and consequently the surface area of the lamella was very small.
- the above-mentioned objects are achieved by introducing a chromium metallo-organic compound which is in a gaseous state into intimate contact with a molten supporting vehicle for a time sufiicient to cause thermal decomposition of the chromium metallo-organic compound, the molten support being maintained at a temperature suflicient to cause thermal decomposition of the metalloorganic compound and being chemically inert and not wetting with regard to the chromium metal which nucleates and deposits on the molten support, and subsequently removing the chromium metal which is in lamella form from the molten support.
- a typical metallo-organic compound suitable to the invention process is chromium dicumene, although any compound which decomposes freeing chromium in the ele-
- Other preferred metallo-organic compounds fufilling the chemical and physical requirements are chromium acetylacetonate results from the characteristic hexagonal (volatization temperature C. and decomposition temperature 350 C.), chromium carbonyl (volatization temperature 100 C. and decomposition temperature 140 C.).
- Chromium dicumene is preferable with respect to the acetylacetonate and the carbonyl because: the chromium acetylacetonate, being originally bonded to oxygen, tends to form oxy-compound impurities and in the carbonyl, the chromium being originally bonded to carbon, tends to precipitate chromium'carbide impurities. Contamination of the chromium hexagonal close packed latice by carbon, oxygen, or nitrogen tends to decrease the metals inherent inability to withstand distortional stress thereby rendering the metal slightly more brittle.
- Additional chromium metallo-organic compounds which are amendable to the process of the invention include dicyclopentadienyl chromium, dibenzene chromium, tricyclopentadienyl chromium hexamine, and cyclopentadienyl chromium carbonyl hydride.
- Supporting vehicles employed in the process should have low melting points, boiling points higher than the decomposition temperature of the particular chromium metallo-organic compound which, is being employed, should not alloy with or react with the elemental chromium which is deposited, nor wet it in any way.
- Examples of the preferred supporting vehicles are pure indium; Woods metal which consists of 50 weight percent bismuth, 25 weight percent lead, 12.5 weight percent tin, and 12.5 weight percent cadmium, and Rose metal which consists of 50 weight percent bismuth, 27.1 weight percent lead, and 22.9 weight percent tin.
- Additional supporting vehicles which may be employed include mercury and tricresyl phosphate.
- the chromium metallo-organic compound (chromium dicumene, for example) is heated in one vessel to a temperature suflicient to volatize said compound (approximately C. for chromium dicumene) and transported in the gaseous state, either alone or by means of an inert gas carrier such as argon, to the entrance orifice of a second vessel in which a suitable supporting vehicle (Woods metal, for example) is maintained in a molten condition at a temperature at least equivalent to the thermal decomposition temperature of the metalloorganic compound (approximately 300 C. in the case of chromium dicumene) but below the boiling point of the molten supporting vehicle.
- a suitable supporting vehicle Wideods metal
- the deposited layer of chromium may, subsequently, be separated from the solidified mass by remelting the supporting vehicle in a suitable inert liquid (for example, boiling toluene), thus recovering the uncontaminated material for further use and withdrawing the chromium metal in the form of a thin uniform foil. With proper care, the chromium foil may be withdrawn directly from the molten supporting vehicle without cooling and subsequent remelting.
- a suitable inert liquid for example, boiling toluene
- Example I Approximately 100 ml. of chromium dicumene were heated to 120 C. in a vessel, and the gaseous compound was transported by means of an argon stream into a sep arate vessel in which about 1000 grams of Woods metal was maintained in the molten state at about 300 C. The gaseous molecules of chromium dicumene were forced to impinge, without substantial mixing, on the surface of the molten supporting vehicle, whereon the chromium dicumene thermally decomposed, leaving a thin foil of chromium metal on the vehicle surface. Decomposition of the metallo-organic compound in other parts of the vessel other than the proximity of the supporting vehicle surface was prevented by maintaining the upper surface of the vessel below 300 C. by means of external cooling.
- the dicumene component of the decomposed chromium dicumene compound was collected in a separate trap.
- a suflicient and uniform layer of chromium metal was deposited on the alloy, the mass was cooled, solidified, removed and immersed in boiling toluene, thus remelting the supporting vehicle and recovering the foil of chro mium metal.
- the foil was found to average about 0.002 inch in thickness and approximately 98% pure chromium. The surface area was approximately 3 square inches.
- Example 11 Approximately 100 ml. of chromium dicumene were heated to 120 C., in a vessel, and the gaseous compound was transported by means of an argon stream into a second vessel, in which about 1000 grams of Woods metal was maintained in the molten metal state at about 300 C. The gaseous molecules of chromium dicumene were forced into the molten Woods metal by means of a pipe, Where the chromium dicumene thermally decomposed, leaving a multitude of thin chromium flakes dispersed in the molten metal. The dicumene component of the decomposed chromium dicumene was allowed to bubble through the molten Woods metal together with the carrier gas and was collected in a separate trap.
- the agitation caused by the escaping gases further improved the formation and dispersion of chromium lamella flakes in the Woods metal.
- the vehicle and lamella were cooled, thus solidifying the entire mass, which, after removal, was immersed in boiling toluene, thus remelting the Woods metal and recovering the metallic chromium flakes. In this manner, powdered chromium lamella of less than 1 mil in thickness and substantially stress free were produced.
- a process for the production of chromium lamella comprising introducing a chromium metallo-organic compound which is in the gaseous state into intimate contact with a molten supporting vehicle, and said molten supporting vehicle being characterized as possessing a boiling point higher than the decomposition temperature of said chromium metallo-organic compound and chemically inert and non-Wetting to chromium metal; and maintaining said supporting vehicle at a temperature sufiicient to cause thermal decomposition of said gaseous chromium metallo-organic compound; and maintaining said intimate contact between said molten supporting vehicle and said chromium metallo-organic compound for a time suflicient to cause thermal decomposition of said chromium metalloorganic compound, whereby said thermal decomposition of said chromium metallo-organic compound produces elemental chromium metal which nucleates to form a lamella on said molten supporting vehicle; and removing said lamella.
Description
tries.
processes essentially based on rolling of fillets -or swagging on accurately machined surfaces. In all of mental state is amendable to the process.
United States Patent 01 Patented Apr. 28, 1964 3 131,049 PRDDUCTION F CIiROh IIUM LAMELLA ON A MGLTEN SUPPORTKNG VEHICLE Bruno R. Miccioli, North Tonawanda, N. assignor to Union Carbide Corporation, a corporation of New York No Drawing. Fiied Jan. 24, 1963, Ser. No. 253,756 7 Claims. (Cl. 75-.5)
wrapping, electronic apparatus, paints, corrosion protection, light reflecting pigments and abrasives.
Chromium lamella have been unavailable for commercial use because of the inability to produce the lamella 'with a small cross sectional area and the desired physical properties required by the electronics, paint, etc., indus- This close packed crystal structure of chromium which permits a minimum absorption of distortional energy before the lattice ruptures.
Foils of many metals are mechanically produced by and ingots these mechanical processes the decrease in thickness of the element is accompanied by a storing of distortional energywhich manifests itself as stresses within the material. Chromium is not readily amenable to treatment by mechanical means because the slight ability of the metal to absorb distortional stress without fracture is completely exploited before the cross-section is reduced to a dimension small enough for commercial value.
. Prior to the inception of the present invention, chromium lamella could not be manufactured in thickness of less than 0.015 inch. This minimum thickness was accompanied by brittleness and consequently the surface area of the lamella was very small.
It is an object of the present invention to provide thin chromium lamella having a thickness of less than mils and of large surface area.
It is further an object of the present invention to provide thin powered chromium lamella having thickness less than 2 mils.
It is another object of this invention to provide a process whereby chromium lamella are produced.
The above-mentioned objects are achieved by introducing a chromium metallo-organic compound which is in a gaseous state into intimate contact with a molten supporting vehicle for a time sufiicient to cause thermal decomposition of the chromium metallo-organic compound, the molten support being maintained at a temperature suflicient to cause thermal decomposition of the metalloorganic compound and being chemically inert and not wetting with regard to the chromium metal which nucleates and deposits on the molten support, and subsequently removing the chromium metal which is in lamella form from the molten support.
' A typical metallo-organic compound suitable to the invention process is chromium dicumene, although any compound which decomposes freeing chromium in the ele- Other preferred metallo-organic compounds fufilling the chemical and physical requirements are chromium acetylacetonate results from the characteristic hexagonal (volatization temperature C. and decomposition temperature 350 C.), chromium carbonyl (volatization temperature 100 C. and decomposition temperature 140 C.). Chromium dicumene is preferable with respect to the acetylacetonate and the carbonyl because: the chromium acetylacetonate, being originally bonded to oxygen, tends to form oxy-compound impurities and in the carbonyl, the chromium being originally bonded to carbon, tends to precipitate chromium'carbide impurities. Contamination of the chromium hexagonal close packed latice by carbon, oxygen, or nitrogen tends to decrease the metals inherent inability to withstand distortional stress thereby rendering the metal slightly more brittle. Additional chromium metallo-organic compounds which are amendable to the process of the invention include dicyclopentadienyl chromium, dibenzene chromium, tricyclopentadienyl chromium hexamine, and cyclopentadienyl chromium carbonyl hydride.
Supporting vehicles employed in the process should have low melting points, boiling points higher than the decomposition temperature of the particular chromium metallo-organic compound which, is being employed, should not alloy with or react with the elemental chromium which is deposited, nor wet it in any way. Examples of the preferred supporting vehicles are pure indium; Woods metal which consists of 50 weight percent bismuth, 25 weight percent lead, 12.5 weight percent tin, and 12.5 weight percent cadmium, and Rose metal which consists of 50 weight percent bismuth, 27.1 weight percent lead, and 22.9 weight percent tin. Additional supporting vehicles which may be employed include mercury and tricresyl phosphate.
A procedure embodying the proces of this invention and illustrating the method of obtaining novel forms of chromium is conducted as follows:
The chromium metallo-organic compound (chromium dicumene, for example) is heated in one vessel to a temperature suflicient to volatize said compound (approximately C. for chromium dicumene) and transported in the gaseous state, either alone or by means of an inert gas carrier such as argon, to the entrance orifice of a second vessel in which a suitable supporting vehicle (Woods metal, for example) is maintained in a molten condition at a temperature at least equivalent to the thermal decomposition temperature of the metalloorganic compound (approximately 300 C. in the case of chromium dicumene) but below the boiling point of the molten supporting vehicle.
Beginning from the above-mentioned entrance orifice, two alternate techniques may be employed each one of which results in a difierent novel chromium product.
Alternate (1 .--The gaseous metallo-organic chromium compound is permitted to enter the vessel containing the molten supporting vehicle. At the interface between the smooth, mirror-like surface of the molten vehicle and the thermally decomposing gaseous molecules of the metallo-organic compound, the liberated elemental chromium nucleates and deposits as a thin lamella and the dicumene and inert gases remaining are permitted to leave the vessel to be recovered elsewhere. When a sufliciently thick foil of chromium metal having a large surface area has deposited on the vehicles surface, cooling and solidification of the entire mass is accomplished to stabilize and retain its physical appearance. The deposited layer of chromium may, subsequently, be separated from the solidified mass by remelting the supporting vehicle in a suitable inert liquid (for example, boiling toluene), thus recovering the uncontaminated material for further use and withdrawing the chromium metal in the form of a thin uniform foil. With proper care, the chromium foil may be withdrawn directly from the molten supporting vehicle without cooling and subsequent remelting.
Alternate (2).-The gaseous metallo-organic chromium compound is conducted from the entrance orifice of the vessel containing the molten supporting vehicle to an exit within the molten vehicle and thermally decomposing the gaseous molecules of the metallo-organic compound therein, thus liberating elemental chromium which nucleates and deposits as powdered lamella. Introduction of the gaseous metallo-organic compound under pressure produces a finer lamellar powder. After suflicient decomposition the vehicle is cooled and caused to solidify. Subsequent remelting in a liquid (for example, boiling toluene which is inert to the solid intermediate) permits recovery of the product and the uncontaminated vehicle.
The adaptation of the present process to continuous deposition and recovery of lamella is feasibile when common engineering knowledge is employed and is well within the realm of a person skilled in the art.
Following are examples of the novel processes and products.
Example I Approximately 100 ml. of chromium dicumene were heated to 120 C. in a vessel, and the gaseous compound was transported by means of an argon stream into a sep arate vessel in which about 1000 grams of Woods metal was maintained in the molten state at about 300 C. The gaseous molecules of chromium dicumene were forced to impinge, without substantial mixing, on the surface of the molten supporting vehicle, whereon the chromium dicumene thermally decomposed, leaving a thin foil of chromium metal on the vehicle surface. Decomposition of the metallo-organic compound in other parts of the vessel other than the proximity of the supporting vehicle surface was prevented by maintaining the upper surface of the vessel below 300 C. by means of external cooling. The dicumene component of the decomposed chromium dicumene compound was collected in a separate trap. When a suflicient and uniform layer of chromium metal was deposited on the alloy, the mass was cooled, solidified, removed and immersed in boiling toluene, thus remelting the supporting vehicle and recovering the foil of chro mium metal. The foil was found to average about 0.002 inch in thickness and approximately 98% pure chromium. The surface area was approximately 3 square inches.
Example 11 Approximately 100 ml. of chromium dicumene were heated to 120 C., in a vessel, and the gaseous compound was transported by means of an argon stream into a second vessel, in which about 1000 grams of Woods metal was maintained in the molten metal state at about 300 C. The gaseous molecules of chromium dicumene were forced into the molten Woods metal by means of a pipe, Where the chromium dicumene thermally decomposed, leaving a multitude of thin chromium flakes dispersed in the molten metal. The dicumene component of the decomposed chromium dicumene was allowed to bubble through the molten Woods metal together with the carrier gas and was collected in a separate trap. The agitation caused by the escaping gases further improved the formation and dispersion of chromium lamella flakes in the Woods metal. When the chromium dicumene decomposition was terminated, the vehicle and lamella were cooled, thus solidifying the entire mass, which, after removal, was immersed in boiling toluene, thus remelting the Woods metal and recovering the metallic chromium flakes. In this manner, powdered chromium lamella of less than 1 mil in thickness and substantially stress free were produced.
From the description of the invention, it can readily be seen that chromium foil and powdered chromium lamella of various areas, minute thicknesses and essentially free of internal stress can be produced by this novel process.
This application is a continuation-in-part of US. Serial No. 852,949, filed November 16, 1959, and now abandoned.
What is claimed is:
1. A process for the production of chromium lamella comprising introducing a chromium metallo-organic compound which is in the gaseous state into intimate contact with a molten supporting vehicle, and said molten supporting vehicle being characterized as possessing a boiling point higher than the decomposition temperature of said chromium metallo-organic compound and chemically inert and non-Wetting to chromium metal; and maintaining said supporting vehicle at a temperature sufiicient to cause thermal decomposition of said gaseous chromium metallo-organic compound; and maintaining said intimate contact between said molten supporting vehicle and said chromium metallo-organic compound for a time suflicient to cause thermal decomposition of said chromium metalloorganic compound, whereby said thermal decomposition of said chromium metallo-organic compound produces elemental chromium metal which nucleates to form a lamella on said molten supporting vehicle; and removing said lamella.
2. A process for producing chromium foil by the thermal decomposition of a chromium metallo-organic compound which is in the gaseous state as delineated in claim 1, wherein said compound is brought into intimate contact with the surface of said molten supporting vehicle and whereby said thermal decomposition produces elemental chromium which nucleates and deposits as a foil on said molten supporting vehicle.
3. A process for producing lamellar chromium powder by the thermal decomposition of a chromium metalloorganic compound which is in the gaseous state as delineated in claim 1, wherein said compound is brought into intimate contact with the body of said molten supporting vehicle from within and whereby said thermal decomposition produces elemental chromium which nucleates and disperses throughout the molten supporting vehicle as said lamellar chromium powder.
4. A process for the production of chromium foil as delineated in claim 2 wherein said metallo-organic compound is chosen from the group consisting of chromium dicumene, chromium acetylacetone, chromium carbonyl, dicyclopentadienyl chromium, dibenzene chromium, tricyclopentadienyl chromium hexamine, and cyclopentadienyl chromium carbonyl hydride, and said molten supporting vehicle is chosen from the group consisting of Woods metal, Rose metal, pure indium, mercury and tricresyl phosphate.
5. A process for the production of lamellar chromium powder as delineated in claim 3 wherein said metalloorganic compound is chosen from the group consisting of chromium dicumene, chromium acetylacetone, chromium carbonyl, dicyclopentadienyl chromium, dibenzene chromium, tricyclopentadienyl chromium hexamine, and cyclopentadienyl chromium carbonyl hydride, and said molten supporting vehicle is chosen from the group consisting of Woods metal, Rose metal, pure indium, mercury and tricresyl phosphate.
6. A process for the production of chromium foil as delineated in claim 4 wherein said metallo-organic compound is chromium dicumene, and said molten supporting vehicle is Woods metal.
7. A process for the production of lamellar chromium powder as delineated in claim 5 wherein said metalloorganic compound is chromium dicumene, and said molten supporting vehicle is Woods metal.
(References on following page) References Cited in the file of this patent FOREIGN PATENTS UNITED STATES PATENTS 683,459 Great Britain Nov. 26, 1952 Re. 24,821 Stauffer May 3, 1960 OTHER REFERENCES 1759661 Mung! et May 1930 5 Newton: Introduction to Metallurgy, 2nd Edition, John Pawlyk 1956 Wiley & Sons, New York, 1948, page 355. 2,732,292 Jordan 1956 Handbook of Chemistry and Physics, 41st Edition, 2807532 Hahn Sept 1957 Chemical Rubber Publishing Company, Cleveland, Ohio; 2,816,826 Brennan Dec. 17, 1957 Page 344 2,834,690 Marvin May 13, 1958 10 2,913,333 Eaton et al. Nov. 17, 1959
Claims (1)
1. A PROCESS FOR THE PRODUCTION OF CHROMIUM LAMELLA COMPRISING INTRODUCING A CHROMIUM METALLO-ORGANIC COMPOUND WHICH IS IN THE GASEOUS STATE INTO INTIMATE CONTACT WITH A MOLTEN SUPPORTING VEHICLE, AND SAID MOLTEN SUPPORTING VEHICLE BEING CHARACTERIZED AS POSSESSING A BOILING POINT HIGHER THAN THE DECOMPOSITION TEMPERATURE OF SAID CHROMIUM METALLO-ORGANIC COMPOUND AND CHAMICALLY INERT AND NON-WETTING TO CHROMIUM METAL; AND NAINTAINING SAID SUPPORTING VEHICLE AT A TEMPARATURE SUFFICIENT TO CAUSE THERMAL DECOMPOSITION OF SAID GASEOUS CHROMIUM METALLO-ORGANIC COMPOUND; AND MAINTAINING SAID INTIMATE CONTACT BETWEEN SAID MOLTEN SUPPOORTING VEHICLE AND SAID CHROMIUM METALLO-ORGANIC COMPOUND FOR A TIME SUFFICIENT TO CAUSE THERMAL DECOMPOSITION OF SAID CHROMIUM METALLOORGANIC COMPOUND, WHEREBY SAID THERMAL DECOMPOSITION OF SAID CHROMIUM METALLO-ORGANIC COMPOUND PRODUCES ELEMENTAL CHROMIUM METAL WHICH NUCLEATES TO FORM A LAMELLA ON SAID MOLTEN SUPPORTING VEHICLE; AND REMOVING SAID LAMELLA.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US253756A US3131049A (en) | 1963-01-24 | 1963-01-24 | Production of chromium lamella on a molten supporting vehicle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US253756A US3131049A (en) | 1963-01-24 | 1963-01-24 | Production of chromium lamella on a molten supporting vehicle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3131049A true US3131049A (en) | 1964-04-28 |
Family
ID=22961576
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US253756A Expired - Lifetime US3131049A (en) | 1963-01-24 | 1963-01-24 | Production of chromium lamella on a molten supporting vehicle |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3131049A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005064035A1 (en) * | 2003-12-23 | 2005-07-14 | Dipl.-Ing. Hilmar Weinert Vakuum-Verfahrenstechnik Gmbh | Production of small thin plates made of at least one dielectric material |
| GB2530337A (en) * | 2014-09-22 | 2016-03-23 | Bae Systems Plc | Graphene Manufacture |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1759661A (en) * | 1926-07-06 | 1930-05-20 | Ig Farbenindustrie Ag | Finely-divided metals from metal carbonyls |
| GB683459A (en) * | 1950-05-03 | 1952-11-26 | Gen Aniline & Film Corp | Production of metal carbonyl powders of small size |
| US2729190A (en) * | 1951-10-08 | 1956-01-03 | Pawlyk Peter | Apparatus for plating the interior of hollow objects |
| US2732292A (en) * | 1956-01-24 | Process of heating particulate metal | ||
| US2807532A (en) * | 1954-12-30 | 1957-09-24 | Monsanto Chemicals | Method of preparing nickel catalyst |
| US2816826A (en) * | 1952-11-04 | 1957-12-17 | Joseph B Brennan | Apparatus for and method of producing metal powders and metal strips |
| US2834690A (en) * | 1954-03-22 | 1958-05-13 | Ohio Commw Eng Co | Method of producing metal shapes by gas plating |
| US2913333A (en) * | 1956-05-31 | 1959-11-17 | Du Pont | Method of producing chromium |
| USRE24821E (en) * | 1960-05-03 | Method of producing metals by decomposition of halides |
-
1963
- 1963-01-24 US US253756A patent/US3131049A/en not_active Expired - Lifetime
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2732292A (en) * | 1956-01-24 | Process of heating particulate metal | ||
| USRE24821E (en) * | 1960-05-03 | Method of producing metals by decomposition of halides | ||
| US1759661A (en) * | 1926-07-06 | 1930-05-20 | Ig Farbenindustrie Ag | Finely-divided metals from metal carbonyls |
| GB683459A (en) * | 1950-05-03 | 1952-11-26 | Gen Aniline & Film Corp | Production of metal carbonyl powders of small size |
| US2729190A (en) * | 1951-10-08 | 1956-01-03 | Pawlyk Peter | Apparatus for plating the interior of hollow objects |
| US2816826A (en) * | 1952-11-04 | 1957-12-17 | Joseph B Brennan | Apparatus for and method of producing metal powders and metal strips |
| US2834690A (en) * | 1954-03-22 | 1958-05-13 | Ohio Commw Eng Co | Method of producing metal shapes by gas plating |
| US2807532A (en) * | 1954-12-30 | 1957-09-24 | Monsanto Chemicals | Method of preparing nickel catalyst |
| US2913333A (en) * | 1956-05-31 | 1959-11-17 | Du Pont | Method of producing chromium |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005064035A1 (en) * | 2003-12-23 | 2005-07-14 | Dipl.-Ing. Hilmar Weinert Vakuum-Verfahrenstechnik Gmbh | Production of small thin plates made of at least one dielectric material |
| GB2530337A (en) * | 2014-09-22 | 2016-03-23 | Bae Systems Plc | Graphene Manufacture |
| GB2530337B (en) * | 2014-09-22 | 2018-10-17 | Bae Systems Plc | Graphene Manufacture |
| US11015037B2 (en) | 2014-09-22 | 2021-05-25 | Bae Systems Plc | Graphene manufacture |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Westengen | Formation of intermetallic compounds during DC casting of a commercial purity Al-Fe-Si alloy | |
| DE2834425C2 (en) | Process for the production of a ductile, crystalline titanium-zirconium alloy | |
| EP0960675A1 (en) | Ultrafine particles and process for the production thereof | |
| US4585617A (en) | Amorphous metal alloy compositions and synthesis of same by solid state incorporation/reduction reactions | |
| US5017250A (en) | Copper alloys having improved softening resistance and a method of manufacture thereof | |
| DE2516747B2 (en) | ||
| US6746511B2 (en) | Decomposition method for producing submicron particles in a liquid bath | |
| JPS6196051A (en) | Quickly solidified aluminum-transition metal-silicon alloy | |
| US3671228A (en) | Method of making high-density sintered metal | |
| US3131049A (en) | Production of chromium lamella on a molten supporting vehicle | |
| US5074933A (en) | Copper-nickel-tin-silicon alloys having improved processability | |
| US4718475A (en) | Apparatus for casting high strength rapidly solidified magnesium base metal alloys | |
| US2766113A (en) | Method of making titanium alloys | |
| US4728507A (en) | Preparation of reactive metal hydrides | |
| US3357826A (en) | Powder metallurgical production of chromium-containing alloys | |
| US4787943A (en) | Dispersion strengthened aluminum-base alloy | |
| US3399050A (en) | Production of nickel powder | |
| JPH0762198B2 (en) | Aluminum alloy for hydrogen generation and method for producing the same | |
| Basu et al. | The controlled reduction of copper tungstate in H 2 O/H 2 mixtures | |
| US1969396A (en) | Production of metallic articles | |
| US4380479A (en) | Foils of brittle alloys | |
| US4069171A (en) | Metallic fibrous skeletal catalysts and process for producing them | |
| US5039478A (en) | Copper alloys having improved softening resistance and a method of manufacture thereof | |
| GB1207538A (en) | Graphitic alloys and processes for the production thereof | |
| US3565604A (en) | Production of spherical-particle powders of metals |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: ELKEM METALS COMPANY, 270 PARK AVENUE, NEW YORK, N Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:UNION CARBIDE CORPORATION, A NY CORP.;REEL/FRAME:003882/0761 Effective date: 19810626 Owner name: ELKEM METALS COMPANY, A NEW YORK GENERAL PARTNERSH Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:UNION CARBIDE CORPORATION, A NY CORP.;REEL/FRAME:003882/0761 Effective date: 19810626 |