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WO1981002003A1 - Materiau et procede de dissociation de l'eau - Google Patents

Materiau et procede de dissociation de l'eau Download PDF

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Publication number
WO1981002003A1
WO1981002003A1 PCT/US1981/000037 US8100037W WO8102003A1 WO 1981002003 A1 WO1981002003 A1 WO 1981002003A1 US 8100037 W US8100037 W US 8100037W WO 8102003 A1 WO8102003 A1 WO 8102003A1
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WIPO (PCT)
Prior art keywords
alloy
weight
amalgam
further characterized
bismuth
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.)
Ceased
Application number
PCT/US1981/000037
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English (en)
Inventor
E Anderson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Horizon Manufacturing Corp
Original Assignee
Horizon Manufacturing Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Horizon Manufacturing Corp filed Critical Horizon Manufacturing Corp
Priority to AU67734/81A priority Critical patent/AU6773481A/en
Publication of WO1981002003A1 publication Critical patent/WO1981002003A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02—Preparation of oxygen
    • C01B13/0203—Preparation of oxygen from inorganic compounds
    • C01B13/0207—Water
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/08—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents with metals
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22C—ALLOYS
    • C22C7/00—Alloys based on mercury
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22C—ALLOYS
    • C22C9/00—Alloys based on copper
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Definitions

  • 06/068,749 entitled MATERIAL AND METHOD FOR OBTAINING HYDROGEN BY DISSOCIATION OF WATER, filed on August 23, 1979; and of an application having attorney's indicia AE-109,entitled MATERIAL AND METHOD TO DISSOCIATE WATER AT CONTROLLED RATES, filed on October 16, 1979; and is related to to an application having at ⁇ torney's indicia AE-106, entitled HYDROGEN GENERATING APPARATUS AND METHOD, filed on October 16, 1979; and to Application Serial No. 06/056,994, entitled FUEL SYSTEM AND METHOD, filed on July 12, 1979.
  • This invention relates to a material for and method of effecting the decomposition/dissociation of water into hydrogen and oxygen.
  • Thermochemical cycles comprising metal-metaloid com ⁇ binations for the generating of both hydrogen and oxygen are disclosed in U. S. Patent 3,969,495. Closed cycle processes for dissociation of water into hydrogen and oxygen are disclosed in U. S. Patents 3,821,358, 3,928,549 and 4,011,305. Combinations of var ⁇ ious metals in multistep processes for dissociation of water are, therefore, well known; however, the simple and facile manner of producing hydrogen and oxygen utilizing an amalgam of alkali metal, aluminum and mercury combined with a catalytic alloy comprising nickel and at least one element selected from the group consisting of germanium, antimony, gallium, thallium, indium and bismuth has not been heretofore appreciated.
  • the material I have found to be suitable for the generation of hydrogen and oxygen from water without spon taneous combustion of the resultant evolved hydrogen and oxygen gases comprises an amalgam of (1) an alkali metal such as lithium, sodium, potassium, cesium, or combina ⁇ tions thereof, (2) aluminum and (3) mercury combined with a catalytic alloy comprising nickel and at least one element selected from the group consisting of germanium, antimony, gallium, thallium, indium and bismuth.
  • the particle size of the sodium and aluminum is such as to enable formation of an amalgam and may fall within the range of from about 10 to about 100 mesh. Most pre- ferably, the particle size of the aluminum should be about 10 mesh. Alkali metal of 1/4" diameter is suitable. The particle size of either the alkali metal or aluminum is not critical since the foregoing metals and mercury readily intermix. The smaller the particle size, of course, the more rapid the mixing.
  • the atomic weight ratio of alkali metal to mercury is from about 1:100 to about 100:1 and the atomic weight ratio of alkali metal to aluminum is from about 1:100 to about 100:1.
  • the atomic weight ratio of alkali metal to mercury is from about 3:1 to about 1:1.5 and the atomic weight ratio of alkali metal to aluminum is from about 1:1 to about 3:1.
  • the amalgam of alkali metal, aluminum and mercury is combined with a catalytically active alloy which is present in a catalytically effective amount and, at the conditions of hydrogen generation, functions to regenerate amalgam to the active metallic state.
  • the catalyst/alloy is nickel and at least one element selected from the group consisting of germanium, antimony, gallium, thallium, indium and bismuth.
  • the catalyst comprises nickel and at least one element selected from the group consisting of germanium, antimony, gallium, thallium, indium and bismuth. Catalytic activity is further enhanced by the addi- tion of minor amounts of zirconium and chromium.
  • TE SHEET Silver and/or gold may be incorporated in the catal as an alloying element to lower the melting point of the alloy.
  • the alloy and amalgam may be combined in weight rati of from about 1:1 to about 1:5 and preferably from about 1:2 to about 1:3.
  • the alloy and amalgam In combining the alloy and amalgam, they may be com ⁇ pounded with an extender.
  • the extender functions both to dilute the amalgam-catalytic alloy combination and to provide a heat sump for heat generated during the dissoci tion of water by contact with the combined amalgam and catalytic alloy.
  • the extender is preferably bismuth; however, admixtures of tin and bismuth or gallium may also function as extenders.
  • the combination of amalgam and alloy or amalgam, alloy and extender is most suitably used in solid block form, hereinafter referred to as a reactor block. Where an extender is employed it may be present as a major con ⁇ stituent of the reactor block.
  • the water reacts with the alkali metal, e.g., sodium, and the aluminum liberat ⁇ ing hydrogen and forming Na3AL(OH)5-
  • the a3AL(OH)g is unstable, and in the presence of the alloy at the condi ⁇ tions of a3AL(OH)g formation, the foregoing composition decomposes to form H2, O2 and regenerated amalgam.
  • the alloy apparently functions to catalyze the decomposition, and thereby extends the useful life of the amalgam.
  • the process may be depicted as follows:
  • chromium is generally present in the alloy in an amount measured on a weight percent basis of said alloy of from about 0.7% to about 1.1% and preferably for about 0.8% to about 0.9%.
  • Each of the components of the alloy may be present in amounts of from about 0.4% by weight to about 28 " .5% by weight based on the weight of the combined catalytic alloy and amalgam.
  • the preferred alloy comprises (1) nickel present in an amount of from about 3.5 to about 6.5% by weight, (2) bismuth present in an amount of from about 40.1 to about 68.7% by weight, (3) antimony present in an amount of from about 25.-5 to about 42.5% by weight, (4) chromium present in an amount of from about 0.7 to about 1.1% by weight, (5) zirconium present in an amount of from about 4.1 to about 6.8% by weight and gold present in an amount of from about 1.1 0.6 to about 1.9% by weight.
  • a specific example of said preferred alloy comprises about 4.5 weight percent nickel, about 53.7 weight percent bismuth, about 34.0 weight percent antimony, about 0.9 weight percent chromium, about 5.4 weight percent zirconium and about 1.5 weight percent gold.
  • the amalgam of sodium, aluminum and mercury is pre ⁇ pared utilizing any of the well known procedures with the added proviso that an inert atmosphere be employed.
  • Amal ⁇ gamation may be facilitated by utilization of an elevated temperature, preferably around 200° C ⁇ 10° C.
  • the amalgam is preferably maintained at this elevated temperature for about 10 minutes where 100 grams.are being processed, and the time is extended about 1 minute for each additional 100 gram aliquot.
  • the preparation of the alloy selected may be in any well known manner having in mind the proviso that an ine atmosphere be maintained.
  • the alloy, upon solidification, and as a practical matter, upon cooling is ground into a powder, preferably a fine powder of about 10 mesh or less. Cooling may be effected in a dessicator to insure the absence of oxygen and moisture, whose presence is detrimental during prepa ation. Grinding/pulverizing may be effected in any well known manner including use of a ball, hammer and/or stam mill.
  • the objective in combining the alloy and amalgam is to intimately admix the two respective components.
  • the specific manner of catalysis is not known, but generally catalysis is a surface phenomenon and consistent there ⁇ with in the instant invention it appears that the cata ⁇ lysis is related to both particle size and nature as wel as uniformity of mixture of the amalgam and catalytic alloy.
  • the amalgam and catalytic alloy may be used (1) in particulate form such as a floating bed, or other inti ⁇ mate dispersion, (2) in the form of porous mass which ma be formed by compression or sintering or (3) as a solid mass by alloying of the amalgam and catalytic alloy.
  • SUBSTITUTE SHEET alloying it is meant that the amalgam and catalytic alloy are combined to form an admixture and alloyed under inert conditions at a temperature above the melting point of said admixture.
  • an extender such as gallium, tin, bismuth, and preferably bismuth may be utilized.
  • the extender functions to vary activity and as a heat sink to retain at least a portion of the heat of reaction of- sodium aluminum hydroxide formation, whereby catalysis of the unstable hydroxide to the metal and oxygen and hydrogen is enhanced.
  • Admixture of extender with the amalgam and catalytic alloy is effected utilizing the extender in a particulate form of comparable size to the other components, which size is generally from about 10 to about 100 mesh.
  • the resulting amalgam is cooled to room temperature in a dessicator in an inert argon atmosphere. There ⁇ after, the amalgam is formed into a fine powder of about 10 mesh utilizing a ball mill. Grinding is effected in an inert atmosphere of argon.
  • Catalytic Alloy 53.7 parts by weight bismuth, 34.0 parts by weight antimony, 4.5 parts by weight nickel, 1.5parts by -weight gold, 5.4 parts by weight zirconium and 0.9 parts by weight chromium are introduced into a graphite crucible which is
  • the resulting alloy is cooled in a dessicator to about room temperature in an inert helium atmosphere. Thereafter the amalgam is formed into a fine powder of about 10 mesh or less utilizing a ball mill. Grinding i effected in an inert atmosphere of helium.
  • the inert atmosphere is used to prevent oxidation o the alloy.
  • Three parts by weight of powdered amalgam is admixe with one part by weight powdered alloy in an inert atmos phere to obtain a uniform mixture of the amalgam and cat lytic alloy.
  • the admixture may be utilized by passing steam up ⁇ wardly therethrough whereby steam is dissociated into hydrogen and oxygen.
  • the resulting block is heated to an elevated temper ature of about 10° C above the melting point of the mass and maintained at said temperature for about lO ⁇ l minutes.
  • amalgam and alloy prepared above and an extender of gallium are admixed in the following proportions:
  • gallium 69.0 parts by weight gallium.
  • the resultant mixture is compressed to form a solid mass by application of pressure of about 40,000 pounds per square inch in a graphite mold conforming to the desired shape of the finished product.
  • the compressed mass in a cru ⁇ proficient conforming to the shape thereof is heated to an elevated temperature of about 10° C. above the melting point of the mass and this temperature is maintained for about 10JI1 minutes. In the oven utilized for heating, an inert atmosphere is maintained. Thereafter the crucible
  • SUBSTITUTE SHEET and its contents are transferred to a desiccator wherein an inert atmosphere is maintained. Upon cooling the re- suiting block is ready for use.
  • the reactor blocks are contacted with a fine spray of water at about room temperature in an atmospheric en ⁇ vironment.
  • the gaseous effluent from said contact com- prises hydrogen and oxygen and burns when subjected to electrical sparking.
  • the volume of gas evolved is depen ⁇ dent on reactor block surface area and the volume of wate impinging thereon. Generally a 2.5 square cm surface will react with 0.10 gallons of water per minute.
  • the resulting amalgam is cooled to room temperature in a dessicator in an inert argon atmosphere. There ⁇ after, the amalgam is formed into a fine powder of about 10 mesh utilizing a ball mill. Grinding is effected in an inert atmosphere of argon.
  • the resulting alloy is cooled in a desiccator to about room temperature in an inert helium atmosphere. Thereafter the amalgam is formed into a fine powder of about 10 mesh or less utilizing a ball mill. Grinding is effected in an inert atmosphere of helium.
  • the inert atmosphere is used to prevent oxidation of the alloy.
  • Three parts by weight of powdered amalgam is admixed with one part by weight powdered alloy in an inert atmos ⁇ phere to obtain a uniform mixture of the amalgam and cata- lytic alloy.
  • the admixture may be utilized by passing steam up ⁇ wardly therethrough whereby steam is dissociated into hydrogen and oxygen.
  • SUBSTITUTE SHEET The resulting block is heated to an elevated temper ature of about 10° C above the melting point of the mass and maintained at said temperature for about 10 ⁇ 1 minutes. In the oven utilized for heating, an inert at- mosphere is maintained. Thereafter the mass comprised o amalgam and alloy is transferred to a dessicator wherein an inert atmosphere is maintained and the mass is allowe to cool. Upon cooling the resultant block is ready for use.
  • the entire foregoing procedure should be carried ou in an inert atmosphere such as helium or argon and in th absence of contaminants. Oxidation of the metallic com ⁇ ponents and/or hydroxide formation will "poison" the resulting reactor block and reduce the activity thereof. Moreover, during the steps of the process operated at elevated temperature, the presence of any oxygen will cause the mass to ignite.
  • the resultant mixture is compressed to form a solid mass by application of pressure of about 40,000 pounds per squar inch in a graphite mold conforming to the desired shape of the finished product.
  • the compressed mass in a crucible conforming to the shape thereof is heated to an elevated temperature of about 10°C above the melting point of the mass and this temperature is maintained for about 10+1 minutes.
  • the reactor blocks are contacted with a fine spray of water at about room temperature in an atmospheric en ⁇ vironment.
  • The. gaseous effluent from said contact com ⁇ prises hydrogen and oxygen and burns when subjected to electrical sparking.
  • the volume of gas evolved is depen ⁇ dent on the reactor block surface area and the volume of water impinging thereon. Generally a 2.5 square cm sur ⁇ face will react with 0.14 gallons of water per minute.
  • the resulting amalgam is cooled to room temperature in a dessicator in an inert argon atmosphere. There ⁇ after, the amalgam is formed into a fine powder of about 10 mesh utilizing a ball mill. Grinding is effected in an inert atmosphere of argon.
  • the resulting alloy is cooled in a desiccator to about room temperature in an inert helium atmosphere. Thereafter the amalgam is formed into a fine powder of . about 10 mesh or less utilizing a ball mill. Grinding i effected in an inert atmosphere of helium.
  • the inert atmosphere is used to prevent oxidation o the alloy.
  • Three parts by weight of powdered amalgam is admixe with one part by weight powdered alloy in an inert atmos phere to obtain a uniform mixture of the amalgam and cat lytic alloy.
  • the admixture may be utilized by immmersion in wate whereby water is dissociated into hydrogen and oxygen.
  • the resultant mixture is compressed to form a solid mass by application of pressure of about 40,000 pounds per square inch in a graphite mold conforming to the desired shape of the finished product.
  • the mold utilized pro ⁇ cutes a cubical block.
  • amalgam and alloy prepared above and a powdered extender comprising 50 weight percent tin and 50 weight percent bismuth of about 10 mesh are admixed in the following proportions: 5 21.775 parts by weight amalgam.
  • the weighing and blending of the foregoing metal ⁇ lic compounds should be done in an inert atmosphere.
  • the resultant mixture is compressed to form a solid mass by application of pressure of about 40,000 pounds per square inch in a graphite mold conforming to the desired shape of the finished product.
  • the compressed mass in a crucible conforming to the shape thereof is heated to an elevated temperature of about 10°C above the melting point of the mass and this temperature is maintained for about lO ⁇ l minutes.
  • an inert atmosphere is main ⁇ tained.
  • the crucible and its contents are transferred to a desiccator wherein an inert atmosphere is maintained. Upon cooling the resultant block is read for use.
  • the reactor blocks are contacted with a fine spray of water at about room temperature in an atmospheric en- viron ent.
  • the gaseous effluent from said contact com ⁇ prises hydrogen and oxygen and burns when subjected to electrical sparking.
  • the volume of gas evolved is depen dent on the reactor block surface area and the volume of water impinging thereon. Generally a 2.5 square cm sur- face-will react with 0.08 gallons of water per minute.
  • the resulting amalgam is cooled to room temperature in a desiccator in an inert argon atmosphere.
  • Catalytic Alloy 33.131 parts by weight bismuth, 12.145 parts by weight nickel, 42.847 parts by weight antimony , 2.429 parts by weight cadmium and 9.448 parts by weight zirconium are introduced into a graphite crucible which is thereafter placed in an oven and heated to melting in an inert atmos ⁇ phere of helium to form an alloy of said metals.
  • the resulting alloy is cooled in a desiccator to about room temperature in an inert helium atmosphere. Thereafter the amalgam is formed into a fine powder of about 10 mesh or less utilizing a ball mill. Grinding is effected in an inert atmosphere of helium.
  • the inert atmosphere is used to prevent oxidation of the alloy.
  • Three parts by weight of powdered amalgam is admixed with one part by weight powdered alloy in an inert atmos ⁇ phere to obtain a uniform mixture of the amalgam and cata ⁇ lytic alloy.
  • the admixture may be utilized by spraying water on the admixture whereby water is dissociated into hydrogen and oxygen.
  • the resultant mixture is compressed to form a solid mass by application of pressure of about 40,000 pounds per square inch in a graphite mold conforming to the desired shape of the finished product.
  • the mold utilized pro ⁇ cutes a cubical block.
  • the resulting block is heated to an elevated tem ⁇ perature of about 10°C above the melting point of the mass and- maintained at said temperature for about lO ⁇ l minutes.
  • an inert atmosphere is maintained in the oven utilized for heating.
  • the mass com ⁇ prised of amalgam and alloy is transferred to a desic ⁇ cator wherein an inert atmosphere is maintained and the mass is allowed to cool.
  • the resul- tant block is ready for use.
  • gallium 69.0 parts by weight gallium.
  • the resultant mixture is compressed to form a solid mass by application of pressure of about 40,000 pounds per square inch in a graphite mold conforming to the desired shape of the finished product.
  • the compressed mass in a crucible conforming to the shape thereof is heated to an elevated temperature of about 10°C above the melting point of the mass and this temperature is maintained for about lO ⁇ l minutes.
  • an inert atmosphere is main- tained.
  • the crucible and its contents are transferred to a desiccator wherein an inert atmosphere is maintained. Upon cooling the resultant block is ready for use.
  • the reactor blocks are contacted with a fine spray of water at about room temperature in an atmospheric en ⁇ vironment.
  • the gaseous effluent from said contact co - prises hydrogen and oxygen and burns when subjected to electrical sparking.
  • the volume of gas evolved is depen ⁇ dent on the reactor block surface area and the volume of water impinging thereon. Generally a 2.5 square cm sur ⁇ face will react with 0.10 gallons of water per minute.
  • S UBSTITUTE SHEET mercury is formed in a graphite crucible in an inert atm phere of argon at an elevated temperature of 200°C
  • the resulting amalgam is cooled to room temperature in a desiccator in an inert argon atmosphere. There- after, the amalgam is formed into a fine powder of about 10 mesh utilizing a ball mill. Grinding is effected in an inert atmosphere of argon.
  • the resulting alloy is cooled in a desiccator to about room temperature in an inert helium atmosphere. Thereafter the amalgam is formed into a fine powder of about 10 mesh or less utilizing a ball mill. Grinding i effected in an inert atmosphere of helium.
  • the inert atmosphere is used to prevent oxidation o the alloy.
  • Three parts by weight of powdered amalgam is admixe with one part by weight powdered alloy in an inert atmos phere to obtain a uniform mixture of the amalgam and cat lytic alloy. .
  • the admixture may be utilized by steam upwardly the through whereby steam is dissociated into hydrogen and oxygen.
  • the resultant mixture is compressed to. form a solid mass by application of pressure of about 40,000 pounds per square inch in a graphite mold conforming to the desired shape of the finished product.
  • the mold utilized pro ⁇ symbolizes a cubical block.
  • the resulting block is heated to an elevated temper ⁇ ature of about 10°C above the melting point of the mass and maintained at said temperature for about lO ⁇ l minutes. In the oven utilized for heating, an inert atmosphere is maintained. Thereafter ' , the mass com- prised of amalgam and alloy is transferred to a desic ⁇ cator wherein an inert atmosphere is maintained and the mass is allowed to cool. Upon cooling, the resul ⁇ tant block is ready for use.
  • amalgam and alloy prepared above and an ex ⁇ tender of powdered tin of about 10 mesh are admixed in the following proportions:
  • the resultant mixture is compressed to form a solid mass by application of pressure of about 40,000 pounds per squar inch in a graphite mold conforming to the desired shape of the finished product.
  • the compressed mass in a crucible conforming to the shape thereof is heated to an elevated temperature of about 10°C above the melting point of the mass and this temperature is maintained for about lO ⁇ l minutes.
  • an inert atmosphere is main ⁇ tained.
  • the crucible and its contents are trandferred to a desiccator wherein an inert atmosphere is maintained.
  • the resultant block is read for use.
  • the reactor blocks are contacted with a fine spray of water at about room temperature in an atmospheric en ⁇ vironment.
  • the gaseous effluent from said contact com ⁇ prises hydrogen and oxygen and burns when subjected to electrical sparking.
  • the volume of gas evolved is depen dent on the reactor block surface area and the volume of water impinging thereon. Generally a 2.5 square cm sur ⁇ face will react with 0.14 gallons of water per minute.

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  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
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Abstract

Un materiau et un procede de decomposition/dissociation de l'eau en hydrogene et en oxygene sont decrits. Le materiau consiste en un amalgame d'un metal alcalin, de mercure et d'aluminium combine avec une quantite a effet catalytique d'un alliage consistant en du nickel et au moins un metal choisi parmi le groupe constitue par le germanium, l'antimoine, le gallium, le thallium, l'indium, et le bismuth.
PCT/US1981/000037 1980-01-07 1981-01-07 Materiau et procede de dissociation de l'eau Ceased WO1981002003A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU67734/81A AU6773481A (en) 1980-01-07 1981-01-07 Material and method to dissociate water

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US06/110,218 US4289744A (en) 1979-10-16 1980-01-07 Material and method to dissociate water
US110218 1998-07-06

Publications (1)

Publication Number Publication Date
WO1981002003A1 true WO1981002003A1 (fr) 1981-07-23

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PCT/US1981/000037 Ceased WO1981002003A1 (fr) 1980-01-07 1981-01-07 Materiau et procede de dissociation de l'eau

Country Status (3)

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US (1) US4289744A (fr)
EP (1) EP0042873A1 (fr)
WO (1) WO1981002003A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001059858A3 (fr) * 2000-02-09 2002-03-14 Millenium Energy Llc Compositions a alliages destinees a etre utilisees comme materiaux d'electrode et pour la production d'hydrogene
WO2002000950A3 (fr) * 2000-06-23 2002-06-27 Millenium Energy Llc Nouvelles compositions destinees a etre utilisees comme materiaux d'electrode et dans la production d'hydrogene
EP1473271A3 (fr) * 2000-05-31 2005-03-30 Heineken Technical Services B.V. Ensemble distributeur de boisson, récipient pour boisson et canalisation de distribution de boisson
CN101962171A (zh) * 2010-09-19 2011-02-02 清华大学 一种铝水连续制氢系统

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Publication number Priority date Publication date Assignee Title
US4358291A (en) * 1980-12-31 1982-11-09 International Business Machines Corporation Solid state renewable energy supply
US4588577A (en) * 1984-03-20 1986-05-13 Cardinal Earl V Method for generating hydrogen
WO2001097966A2 (fr) * 2000-06-19 2001-12-27 Hydrogen Energy America Llc Alliage catalytique pour la dissociation de l'eau dans l'hydrogene et l'oxygene et son procede de fabrication
WO2002006153A1 (fr) 2000-07-13 2002-01-24 Hydrogen Energy America Llc Procede et dispositif de production commandee d'hydrogene par dissociation de l'eau
US8080233B2 (en) * 2006-05-12 2011-12-20 Purdue Research Foundation Power generation from solid aluminum
US7938879B2 (en) * 2006-05-12 2011-05-10 Purdue Research Foundation Power generation from solid aluminum
US8323364B2 (en) * 2007-07-31 2012-12-04 Purdue Research Foundation Control system for an on-demand gas generator

Citations (12)

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GB190903188A (en) * 1909-02-09 1909-09-30 George William Johnson Improvements in Means for the Preparation of Pure Hydrogen.
US2083648A (en) * 1932-02-25 1937-06-15 Ig Farbenindustrie Ag Preparation of alkali metal hydroxide solutions
US2837408A (en) * 1954-06-29 1958-06-03 Olin Mathieson Process and apparatus for the catalytic decomposition of alkali metal amalgams
US3313598A (en) * 1965-06-07 1967-04-11 Ethyl Corp Method of controlled hydrogen generation
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