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US3427153A - Method of preparing alloy blacks - Google Patents

Method of preparing alloy blacks Download PDF

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Publication number
US3427153A
US3427153A US374274A US3427153DA US3427153A US 3427153 A US3427153 A US 3427153A US 374274 A US374274 A US 374274A US 3427153D A US3427153D A US 3427153DA US 3427153 A US3427153 A US 3427153A
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Prior art keywords
alloy
blacks
metals
metal
gold
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US374274A
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Peruvemba Swaminath Venkatesan
Melvin Yarish
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Leesona Corp
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Leesona Corp
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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
    • H01M4/928Unsupported catalytic particles; loose particulate catalytic materials, e.g. in fluidised state
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M2004/8678Inert electrodes with catalytic activity, e.g. for fuel cells characterised by the polarity
    • H01M2004/8684Negative electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M2004/8678Inert electrodes with catalytic activity, e.g. for fuel cells characterised by the polarity
    • H01M2004/8689Positive electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0002Aqueous electrolytes
    • H01M2300/0014Alkaline electrolytes
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the method comprises admixing salts of the desired metals of the alloy in the proper ratios, forming a co-precipitate of the metals by addition of ammonium hydroxide to the salt solutions, and reducing the co-precipitated hydroxide.
  • This invention relates to the preparation of alloy blacks in finely divided form. More particularly, the invention relates to a simplified method for the preparation of improved alloy blacks. Basically, the improved method comprises admixing salts of the desired metals of the alloy in the proper ratios, forming a precepitate of the metal alloy by addition of ammonium hydroxide and reducing the co-precipitated hydroxide.
  • the alloy is formed into wires or narrow strips by usual methods known in the art such as drawing, etc.
  • the alloy wires or strips are mounted in ice water as electrodes, i.e., as an anode and cathode.
  • a direct current potential of between 150 and 200 volts is applied to the system and the wires brought into close proximity to establish an arc.
  • the arcing disrupts the metals and forms a fine suspension of alloy particles in the water.
  • the metal particles are filtered out, dried, and employed in known procedures. As apparent, the above-described process is complex and time consuming.
  • alloy blacks can be prepared by forming admixtures of the desired metal salts in their proper ratio, adding ammonium hydroxide to the admixture to form the co-precipitated metal hydroxides and thereafter reducing the metal hydroxide with a reducing agent, such as hydrazine or bubbling hydrogen, to form the alloy blacks.
  • a reducing agent such as hydrazine or bubbling hydrogen
  • the alloy blacks of any of the noble metals such as the so-called platinum and palladium metals and gold and silver can be prepared according to the method of the present invention. Thus, it is merely necessary to admix salts of the desired metals in the proper ratio and thereafter form the hydroxides and reduce.
  • metal alloy blacks of ruthenium, rhodium, palladium, osmium, iridium, platinum, gold, and silver can be prepared, gold-palladium alloy blacks are preferred in view of their exceptional activity and stability, particularly when employed as a catalyst on a fuel cell electrode.
  • the admixtures of metal hydroxides can be prepared from aqueous salt solutions of the metals, such as solutions of the chlorides, nitrates, and sulfates. However, it is necessary that the precipitate be prepared from a solution of the two or more metals of the alloy. Thus, quite surprisingly, it was found that when gold and palladium were precipitated separately, and thereafter the precipitates admixed and reduced, an alloy was not obtained but merely an admixture of the two metals.
  • the temperatures at which the precipitated hydroxides are formed or reduced are not critical and can be varied over a substantially wide range.
  • the alloy blacks can be used in any of the areas where conventional blacks have been employed.
  • EXAMPLE An alloy black was prepared by dissolving gold chloride salt in a concentrated aqueous palladium chloride solution, the concentration in terms of metal being 100 mg./ml., to obtain a gold to palladium ratio of :25 on an atomic percent basis. The mixture was introduced slowly into a 3% ammonical solution at room temperature with constant stirring. Upon contact of the two solutions, a finely divided yellow precipitate was formed immediately. Thereafter, an excess of dilute hydrazine was added to reduce the precipitated material to the finely divided metallic state. After washing in distilled water and drying, tests showed the finely divided metallic particles to be the gold-palladium alloy.
  • a reducing electrode was prepared by coating a nickel support screen having a mesh size of on the Tyler scale with a paste prepared from the above-described alloy black and Teflon suspended in water.
  • the Teflon, having an average particle size of 0.3 micron in diameter, and the alloy black were present in a ratio of 3:10. After coating the screen with the paste, the system was stabilized by heating at 300 C. for 30 minutes. After cooling,
  • the structure described as above was employed as the cathode in a fuel cell in conjunction with a similarly constructed anode employing platinum black as the activator.
  • the electrolyte of the cell is a normal aqueous potassium hydroxide solution.
  • the operating temperature is 75 C.
  • the anode is fed with hydrogen at a pressure of 0.15 p.s.i.g. Oxygen is fed to the cathode at a pressure of 0.25
  • the palladium and gold can be replaced by combinations of other metals such as platinum, ruthenium, osmium, iridium, silver, and rhodium. Such combinations must be capable of forming mixed oxide and/or hydroxide phases and solid metal solutions or an intermetallic phase. Moreover, the percentages of the different metals in the alloy can be varied to obtain substantially different compositions. Other metal salts can be employed in the preparation of the metal hydroxides. It should be appreciated that the invention is not to be limited by the example as it is possible to produce still other embodiments without departing from the inventive concept herein disclosed and covered by the appended claims.
  • the method of preparing a palladium-gold alloy black comprising the steps of (1) adding gold chloride to an aqueous solution of palladium chloride to obtain the desired gold to palladium ratio, (2) forming a precipitate by adding ammonium hydroxide to the solution of (l), and (3) reducing said gold and palladium hydroxide precipitate with hydrazine to form a metal alloy black.
  • the method of preparing a metal alloy black comprising the steps of (1) forming a solution of at least two metal salts; (2) forming a co-precipitate of the metals by adding ammonium hydroxide to the salt solution; and (3) reducing said co-precipitated metal hydroxide with a member of the group consisting of hydrazine and bubbling hydrogen to form a metal alloy black.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)
  • Catalysts (AREA)
  • Powder Metallurgy (AREA)

Description

United States Patent METHOD OF PREI ARING ALLOY BLACKS Peruvemba Swarninatha Venkatesan, Bronx, and Melvin Yarish, Brooklyn, N.Y., assignors to Leesona Corporation, Warwick, R.I., a corporation of Massachusetts No Drawing. Filed June 11, 1964, Ser. No. 374,27? US. Cl. 75-108 2 Claims Int. Cl. C22c 1/06, 5/00 ABSTRACT OF THE DISCLOSURE An improved method of preparing all-0y blacks is described. The method comprises admixing salts of the desired metals of the alloy in the proper ratios, forming a co-precipitate of the metals by addition of ammonium hydroxide to the salt solutions, and reducing the co-precipitated hydroxide.
This invention relates to the preparation of alloy blacks in finely divided form. More particularly, the invention relates to a simplified method for the preparation of improved alloy blacks. Basically, the improved method comprises admixing salts of the desired metals of the alloy in the proper ratios, forming a precepitate of the metal alloy by addition of ammonium hydroxide and reducing the co-precipitated hydroxide.
It is recognized in the art that many metals, particularly the transition metals of the fifth and sixth series of Group VIII of the Mendelejeifs Periodic Table and the noble metals of Sub-Group I have excellent properties as catalysts particularly in gas-solid reactions. Quite surprisingly, when certain alloys of two or more metals are prepared, the alloys have enhanced catalytic properties in comparison with any of the metals of the alloy taken singly. Therefore, the use of alloys as catalysts has become more prevalent in recent years, particularly as activators in fuel cell electrodes, i.e., cells wherein the energy of reaction between a fuel and an oxidant is converted directly into electrical energy.
Further, it is known that the value of a catalyst, apart from the intrinsic activity of the material, is directly related to the surface area of the catalyst exposed to reactants. For his reason, metals and alloys are used as catalysts in finely divided or spongy form having a high surface :area. Although there are several methods of preparing finely divided metals such as electrolytic precipitation of the metal from a suitable salt solution, the prepa' ration of alloy blacks presents more of a problem. Thus, one method of preparing blacks of an alloy is first to form an alloy by known metallurgical means such as melting powders of the different metals together in the proper proportions, preferably above the melting point of the metals and thereafter cooling. The alloy is formed into wires or narrow strips by usual methods known in the art such as drawing, etc. The alloy wires or strips are mounted in ice water as electrodes, i.e., as an anode and cathode. A direct current potential of between 150 and 200 volts is applied to the system and the wires brought into close proximity to establish an arc. The arcing disrupts the metals and forms a fine suspension of alloy particles in the water. The metal particles are filtered out, dried, and employed in known procedures. As apparent, the above-described process is complex and time consuming.
It has now been found that alloy blacks can be prepared by forming admixtures of the desired metal salts in their proper ratio, adding ammonium hydroxide to the admixture to form the co-precipitated metal hydroxides and thereafter reducing the metal hydroxide with a reducing agent, such as hydrazine or bubbling hydrogen, to form the alloy blacks. In addition to the aforesaid process 3,427,153 Patented Feb. 11, 1969 being extremely simple, the blacks formed have enhanced activity particularly when used on fuel cell electrodes, possibly due to an increase in the surface area.
Accordingly, it is an object of the present invention to provide an improved method of preparing metal alloy blacks.
It is still a further object of the present invention to provide metal alloy blacks having a large surface area by forming admixtures of the metal salts in the desired ratio, co-precipitating the metal hydroxides by adding ammonium hydroxide and reducing the co-precipitate.
It is a still further object of the present invention to provide gold-palladium alloy blacks by adding a solution of ammonium hydroxide to an aqueous solution of palladium and gold salts to form the co-precipitated hydroxides and thereafter reducing with an aqueous hydrazine solution to form the finely divided metal alloy black.
These and other objects of the invention will become more fully apparent from the following detailed description and illustrative examples.
The alloy blacks of any of the noble metals such as the so-called platinum and palladium metals and gold and silver can be prepared according to the method of the present invention. Thus, it is merely necessary to admix salts of the desired metals in the proper ratio and thereafter form the hydroxides and reduce. However, although metal alloy blacks of ruthenium, rhodium, palladium, osmium, iridium, platinum, gold, and silver can be prepared, gold-palladium alloy blacks are preferred in view of their exceptional activity and stability, particularly when employed as a catalyst on a fuel cell electrode.
The admixtures of metal hydroxides can be prepared from aqueous salt solutions of the metals, such as solutions of the chlorides, nitrates, and sulfates. However, it is necessary that the precipitate be prepared from a solution of the two or more metals of the alloy. Thus, quite surprisingly, it was found that when gold and palladium were precipitated separately, and thereafter the precipitates admixed and reduced, an alloy was not obtained but merely an admixture of the two metals. The temperatures at which the precipitated hydroxides are formed or reduced are not critical and can be varied over a substantially wide range.
The alloy blacks can be used in any of the areas where conventional blacks have been employed.
Having described the invention in general terms, the following example is set forth to illustrate a preferred embodiment of the invention.
EXAMPLE An alloy black was prepared by dissolving gold chloride salt in a concentrated aqueous palladium chloride solution, the concentration in terms of metal being 100 mg./ml., to obtain a gold to palladium ratio of :25 on an atomic percent basis. The mixture was introduced slowly into a 3% ammonical solution at room temperature with constant stirring. Upon contact of the two solutions, a finely divided yellow precipitate was formed immediately. Thereafter, an excess of dilute hydrazine was added to reduce the precipitated material to the finely divided metallic state. After washing in distilled water and drying, tests showed the finely divided metallic particles to be the gold-palladium alloy.
To demonstrate the utility of the novel alloy black, a reducing electrode was prepared by coating a nickel support screen having a mesh size of on the Tyler scale with a paste prepared from the above-described alloy black and Teflon suspended in water. The Teflon, having an average particle size of 0.3 micron in diameter, and the alloy black were present in a ratio of 3:10. After coating the screen with the paste, the system was stabilized by heating at 300 C. for 30 minutes. After cooling,
. 3 the Teflon gold-palladium alloy coating adhered very well to the support screen.
The structure described as above was employed as the cathode in a fuel cell in conjunction with a similarly constructed anode employing platinum black as the activator. The electrolyte of the cell is a normal aqueous potassium hydroxide solution. The operating temperature is 75 C. The anode is fed with hydrogen at a pressure of 0.15 p.s.i.g. Oxygen is fed to the cathode at a pressure of 0.25
In the aforesaid examples, the palladium and gold can be replaced by combinations of other metals such as platinum, ruthenium, osmium, iridium, silver, and rhodium. Such combinations must be capable of forming mixed oxide and/or hydroxide phases and solid metal solutions or an intermetallic phase. Moreover, the percentages of the different metals in the alloy can be varied to obtain substantially different compositions. Other metal salts can be employed in the preparation of the metal hydroxides. It should be appreciated that the invention is not to be limited by the example as it is possible to produce still other embodiments without departing from the inventive concept herein disclosed and covered by the appended claims.
What is claimed is:
1. The method of preparing a palladium-gold alloy black comprising the steps of (1) adding gold chloride to an aqueous solution of palladium chloride to obtain the desired gold to palladium ratio, (2) forming a precipitate by adding ammonium hydroxide to the solution of (l), and (3) reducing said gold and palladium hydroxide precipitate with hydrazine to form a metal alloy black.
2. The method of preparing a metal alloy black comprising the steps of (1) forming a solution of at least two metal salts; (2) forming a co-precipitate of the metals by adding ammonium hydroxide to the salt solution; and (3) reducing said co-precipitated metal hydroxide with a member of the group consisting of hydrazine and bubbling hydrogen to form a metal alloy black.
References Cited UNITED STATES PATENTS 2,254,976 9/1941 Powell -108 2,375,506 5/1945 Turck 75-108 2,726,151 12/1955 Kern 75108 2,787,540 4/1957 Appell 75l08 2,863,762 12/1958 Pullen 75108 2,970,051 1/1961 MackiW et al 75l08 RICHARD O. DEAN, Primary Examiner.
U.S. Cl. X.R. 75-118, 121
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3620713A (en) * 1970-02-26 1971-11-16 Du Pont Process of preparing noble metal powders
US3620714A (en) * 1970-02-26 1971-11-16 Du Pont Process of preparing noble metal alloy powders
US3771996A (en) * 1971-05-13 1973-11-13 Du Pont Process for manufacturing gold powder
US3776776A (en) * 1972-01-21 1973-12-04 Prototech Co Gold-coated platinum-metal black catalytic structure and method of preparation
US3816097A (en) * 1971-05-06 1974-06-11 Owens Illinois Inc Powders of metal, silver and gold
US4456473A (en) * 1983-05-05 1984-06-26 Chemet Corporation Method of making silver powder
US4456474A (en) * 1983-05-05 1984-06-26 Chemet Corporation Method of making fine silver powder
EP0117290A2 (en) * 1982-12-30 1984-09-05 International Business Machines Corporation Fuel cell catalysts
US4678505A (en) * 1984-08-29 1987-07-07 E. I. Du Pont De Nemours And Company Process for forming solid solutions
US20090291848A1 (en) * 2006-03-27 2009-11-26 Juergen Biener Method for forming gold-containing catalyst with porous structure
US20130178360A1 (en) * 2012-01-06 2013-07-11 California Institute Of Technology Nickel-based electrocatalytic photoelectrodes

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2254976A (en) * 1937-12-20 1941-09-02 Johnson Matthey Co Ltd Manufacture and production of fine metal and alloy powders
US2375506A (en) * 1941-12-13 1945-05-08 Colgate Palmolive Peet Co Process for producing metal compositions of low apparent density
US2726151A (en) * 1949-07-12 1955-12-06 Schweiz Sprengstoff Fabrik A G Producing and reactivating a carrierless nickel catalyst
US2787540A (en) * 1949-12-22 1957-04-02 Universal Oil Prod Co Recovery of platinum
US2863762A (en) * 1956-12-28 1958-12-09 Universal Oil Prod Co Recovery of noble metals
US2970051A (en) * 1959-05-01 1961-01-31 Sherritt Gordon Mines Ltd Process for the separation of lead from solutions

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2254976A (en) * 1937-12-20 1941-09-02 Johnson Matthey Co Ltd Manufacture and production of fine metal and alloy powders
US2375506A (en) * 1941-12-13 1945-05-08 Colgate Palmolive Peet Co Process for producing metal compositions of low apparent density
US2726151A (en) * 1949-07-12 1955-12-06 Schweiz Sprengstoff Fabrik A G Producing and reactivating a carrierless nickel catalyst
US2787540A (en) * 1949-12-22 1957-04-02 Universal Oil Prod Co Recovery of platinum
US2863762A (en) * 1956-12-28 1958-12-09 Universal Oil Prod Co Recovery of noble metals
US2970051A (en) * 1959-05-01 1961-01-31 Sherritt Gordon Mines Ltd Process for the separation of lead from solutions

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3620714A (en) * 1970-02-26 1971-11-16 Du Pont Process of preparing noble metal alloy powders
US3620713A (en) * 1970-02-26 1971-11-16 Du Pont Process of preparing noble metal powders
US3816097A (en) * 1971-05-06 1974-06-11 Owens Illinois Inc Powders of metal, silver and gold
US3771996A (en) * 1971-05-13 1973-11-13 Du Pont Process for manufacturing gold powder
US3776776A (en) * 1972-01-21 1973-12-04 Prototech Co Gold-coated platinum-metal black catalytic structure and method of preparation
EP0117290A2 (en) * 1982-12-30 1984-09-05 International Business Machines Corporation Fuel cell catalysts
EP0117290A3 (en) * 1982-12-30 1986-01-22 International Business Machines Corporation Fuel cell catalysts
US4456474A (en) * 1983-05-05 1984-06-26 Chemet Corporation Method of making fine silver powder
US4456473A (en) * 1983-05-05 1984-06-26 Chemet Corporation Method of making silver powder
US4678505A (en) * 1984-08-29 1987-07-07 E. I. Du Pont De Nemours And Company Process for forming solid solutions
US20090291848A1 (en) * 2006-03-27 2009-11-26 Juergen Biener Method for forming gold-containing catalyst with porous structure
US8785346B2 (en) * 2006-03-27 2014-07-22 Lawrence Livermore National Security, Llc Method for forming gold-containing catalyst with porous structure
US20130178360A1 (en) * 2012-01-06 2013-07-11 California Institute Of Technology Nickel-based electrocatalytic photoelectrodes

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