WO2008015844A1 - Appareil générateur de courant - Google Patents
Appareil générateur de courant Download PDFInfo
- Publication number
- WO2008015844A1 WO2008015844A1 PCT/JP2007/061844 JP2007061844W WO2008015844A1 WO 2008015844 A1 WO2008015844 A1 WO 2008015844A1 JP 2007061844 W JP2007061844 W JP 2007061844W WO 2008015844 A1 WO2008015844 A1 WO 2008015844A1
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- WIPO (PCT)
- Prior art keywords
- hydrogen
- container
- functional
- electrolyte
- battery
- Prior art date
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M16/00—Structural combinations of different types of electrochemical generators
- H01M16/003—Structural combinations of different types of electrochemical generators of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
-
- 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
- C01B3/065—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 from a hydride
-
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/066—Integration with other chemical processes with fuel cells
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- 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
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- 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
- Y02E60/50—Fuel cells
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Definitions
- the present invention relates to a power generation apparatus having two systems: a system in which hydrogen gas is generated by hydrolysis and a hydrogen consumer generates power, and a system in which power is generated from a chemical reaction by oxidation and reduction of a plurality of ions and electricity.
- Patent Document 1 Patent Publication 2004—149394
- Patent Document 2 Patent Publication 2002— 069558
- Patent Document 3 International Patent Publication W02003 / 020635
- the equipment In this method of generating hydrogen by high-temperature heating of metal materials, the equipment is also subject to heat damage, and in the method of generating hydrogen by reacting water vapor with hydride containing acid / alkaline materials, solids due to acid and alkali are high. There are dangerous problems such as degradation of devices such as molecular fuel cells and hydrogen generation at low humidity even when operation is stopped.
- the method for generating hydrogen by heating metal materials at a high temperature is in a reaction environment of 600 ° C or higher, and the water itself supplied for hydrolysis is highly evaporated, resulting in poor efficiency.
- the hydrogen generation method in which water vapor is reacted with a hydride containing an alkali material, it takes time to regenerate the hydride, and harmful products are also generated.
- the conventional method has a problem that it is difficult to control the generated hydrogen gas and there is no means for storing surplus hydrogen gas, so that it bursts due to the pressure of the generated surplus gas. It is dangerous and unsuitable as a hydrogen supply source for hydrogen consumers such as polymer electrolyte fuel cells, hydrogen engines, hydrogen fusing systems, and semiconductor manufacturing equipment that are used in industry and consumer.
- the issue of controlling hydrogen generation is that water or an aqueous solution is injected into the device, especially when devices such as small mobile phones and automobiles are used upside down, or when random hydrogen supply is required. Therefore, by always accumulating on the side where the gravity acts, it is difficult to release the generated hydrogen gas, to secure the flow path, and to control the fluctuation of the hydrogen consumption.
- Ni-hydrogen secondary batteries that are charged and discharged from a chemical reaction caused by oxidation / reduction of ions with a negative nickel compound by mounting a hydrogen storage alloy on the negative electrode.
- Patent Document 4 Patent Publication 2 0 0 2—1 0 5 5 6 4
- the present invention has a function that does not affect the function even if it is used upside down or when a random hydrogen supply is required when the device, which is a prior art charge, is used as a power source for a small mobile phone or automobile. It is to be able to supply. In addition, even if the amount of hydrogen gas generated improves the battery function, the apparatus can be reduced in size and cost. Another purpose is to use safe materials that do not drain resources and are good for environmental conservation, and convert electrical energy from natural or renewable energy into physical (functional materials) for safe and large-scale storage. I will provide a. Disclosure of the invention
- a hydrogen generation means including a liquid container for generating hydrogen gas from both by hydrolysis of reacting with an aqueous solution (electrolyte) and alteration of a functional substance by hydrolysis, and by bonding of hydrogen atoms fixed between crystals;
- control means for controlling the amount.
- the functional material is a hydrogen storage alloy
- oxygen, carbon dioxide, nitrogen, moisture, etc. can be prevented from directly touching the surface of the hydrogen storage alloy in the atmosphere. Interfacial reactions can be prevented.
- heat and electricity conductivity can be increased by combining powders of functional substances into solid bodies or coarse particles.
- the coating material is a water-soluble polymer resin and a low-temperature thermoplastic polymer resin that fluidizes molecules at 70 ° C or lower, such as an aliphatic polyester resin, a functional material Even if the film cracks due to the expansion and contraction of the film, it can be self-repaired by the low-temperature heat of the self-heating to prevent the powder from falling off and to maintain the tight fixation.
- a water-soluble or organic solvent-soluble polymer resin can be easily formed into a thin film with water or an organic solvent.
- an emulsion type in which an aliphatic polyester resin or a polyolefin resin, which is a water-soluble organic polymer resin obtained by polymerizing lactic acid by a chemical synthesis method, is dispersed in water.
- Other common organic polymer resins can also be used.
- a functional substance is attached to the equipment and cracks occur on the surface of the coating as the operation time elapses, the polymer function changes from low temperature thermoplasticity to heat generation during operation, etc. Can self-repair cracks.
- the functional substance is a hydrogen storage alloy
- various functional substances in the form of coated particles When the solid material mixed with the binder is packed inside or outside of the pipe in the equipment and installed, the coated granular functional substance is activated in advance and then mixed with the binder. Pasted with organic solvent If the material is solidified and packed inside or outside of the pipe in the device, or if the pasted material is solid-bonded in the groove of the corrugated plate, the large device will be under pressure because activation is not required later. On the other hand, it does not have to be a sturdy container.
- This application is for the purpose of hydrogen purification, hydrogen purification equipment for reformed gas and low-purity hydrogen gas including pipe or sheet shape, or for the purpose of heat pump, for heat exchange equipment, or for the purpose of hydrogen pressurization.
- the same effect can be obtained in the hydrogen compression apparatus.
- the active material becomes a fine powder due to expansion and contraction due to insertion and extraction of hydrogen and lithium.
- a power generation element consisting of a negative electrode, a positive electrode, and a separation membrane is joined and covered with an insulating film, the functionality of the power generation element is increased and the life of the battery is extended. realizable.
- the process of hydrogenation of functional substances put high-pressure hydrogen into a pressure-resistant container with coarse particles of metal or alloy in the functional substance, and install a heating wire, electric plug, laser-radiating plug, etc.
- one end of the functional substance is heated at high temperature and ignited, so that synthesis using self-heating due to hydrogenation reaction can be performed, so the hydride fine powder containing nanometer-scale metal crystals is low. It can be easily obtained with Kos ⁇ .
- the metal can be reduced by a method in which a material such as a metal compound is heated at a high temperature, gasified and separated, and then cooled.
- magnesium oxide is used as a functional substance
- a laser beam made from renewable energy such as natural energy is irradiated from the laser radiation plug of the temperature control unit, and the magnesium oxide is heated to a high temperature.
- the gas can be gasified, oxygen can be dissipated, and the magnesium gas can be cooled to reduce and produce fine metal.
- functional substances produced by reduction and hydrogenation using natural or renewable energy can be sealed and stored in waterproof containers or bags.
- electrical energy generated by natural or renewable energy electrical energy can be converted and stored and transported as a high-density safe substance.
- This hydrogenated functional substance is, for example, magnesium hydride, filled in a hydrogen generation container, and injected with water or an aqueous solution into the hydrogen generation container, so that hydrogen and hydrogen gas generated by hydrolysis are generated.
- magnesium reacts and transforms into magnesium hydroxide, hydrogen atoms fixed between the magnesium crystals are released.
- a large amount of hydrogen gas can be obtained from both of the hydrogen gas generated when two atoms combine to form hydrogen molecules.
- the generated hydrogen gas is supplied to a hydrogen consumer, and if the hydrogen consumer is a fuel cell or a hydrogen organization, water is produced by the combination of oxygen and hydrogen. Since this generated water does not contain acid or alkali, it can be directly circulated again inside the hydrogen generation vessel, and raw water for hydrolysis can be obtained without supplying water from the outside.
- this hydrolysis reaction can be carried out with water by using an aqueous solution of acid or alkaline materials, or by heating at 140 ° C or higher in a high pressure environment.
- aqueous solution of acid or alkaline materials
- electrolysis reaction cannot be sustained, it is natural and useful for the human body.
- nigari magnesium chloride ZM g CI
- electrolysis reaction it will hydrolyze at normal temperature and pressure.
- a self-propelled reaction can be performed.
- This reaction can be triggered by a self-discharge phenomenon caused by a short circuit of the local battery, and by using this to form a battery element in the container. If the battery element is configured to fall, the negative active material is loaded with functional magnesium (Mg) or magnesium hydride (MgH2), and the electrolyte is magnesium chloride (MgCI) aqueous solution (electrolyte) )
- MgCI magnesium chloride
- the high molecular solid electrolyte and anode diffusion layer are made of Ni, Ti and other metals, alloys, powders of metal compounds, powdered activated carbon, graphite and catalysts mixed with fluororesin.
- a battery having a plurality of active materials such as oxygen and nickel hydroxide
- a diffusion layer that expands the unit area and promotes the interfacial reaction. It can function as a magnesium battery that also serves as hydrolysis with reduced polarization resistance.
- the electrolyte must contain a function of shielding the outflow of hydrogen gas, so that it contains a polymer solid electrolyte and a non-woven fabric with capillary action and a gel body together with an electrolyte.
- the hydrogen gas generated in the hydrogen generation container can be sent to the hydrogen consumer without flowing out of the open surface of the anode surface, and the container can be prevented from bursting.
- This can be applied to the small battery field of portable devices such as plate batteries and button batteries.
- the active material such as a metal, alloy, metal compound powder, and catalyst such as N, ⁇ ⁇ or the like that can accept hydrogen and magnesium ions is mixed in the anode.
- the unit area can be expanded to promote the interfacial reaction, and by receiving multiple ions including polyvalent ions, it can function as a battery that also serves as a hydrolysis with reduced separation resistance.
- magnesium (Mg) in the negative electrode is increased or decreased by energizing the load device with the electric power generated by the battery element of the container and changing the amount of current flowing through the load
- the magnesium (Mg) The amount by which the metal crystal is denatured into magnesium hydroxide from the surface side of M g ) is also proportional.
- hydrogen atoms that have lost their anchorage between Mg metal crystals generate hydrogen gas because two of the atoms combine to form hydrogen molecules.
- the amount of generated hydrogen can be controlled by the electric current from the reaction of the load current.
- stacking containers and cells of battery elements makes it easy to control hydrogen generation even in the field of using high-voltage hydrogen demand devices that have large fluctuations in hydrogen consumption, such as fuel cell vehicles.
- a negative electrode magnesium (Mg) is hydrogenated by manufacturing a container by attaching magnesium (Mg) particles or powder to the negative electrode and charging it first. And can be used as a large capacity primary battery.
- the container When the container is configured as a secondary battery (charge / discharge) using oxygen (O) as the active material, it is coated with magnesium (Mg) powder with a plastic polymer or metal and solidly attached to the negative electrode.
- Mg magnesium
- the anode uses oxygen in the atmosphere as an active material, the amount of electricity that can be discharged is not limited on the positive electrode side, and the electric capacity can be dramatically increased. Charging can be performed by supplying both.
- the active material of the anode is metal oxide or lithium cobaltate (LiCo02), lithium nickelate (LiNi02), manganese
- LiCo02 lithium cobaltate
- LiNi02 lithium nickelate
- manganese When a battery element is configured in a container using a functional material of a transition metal oxide such as lithium oxide (LiMn204), and various materials are used for the electrolyte and the functional material of the negative electrode, multiple ions (hydrogen ions, metal ions) A composite battery that avoids polarization resistance due to ions, lithium ions, etc.) can be obtained.
- a reaction chamber is provided in the lower part, and various forms of magnesium (Mg, for example, plate-like lumps or fragments, powders or solidified powders, etc.) ) Or magnesium hydride (Mg H2) functional substance is installed inside, a liquid chamber is provided in the upper part, and an aqueous solution (electrolyte) is put into the structure.
- the aqueous solution (electrolyte) is pushed up (flowed out) by the pressure of hydrogen gas, or the generated hydrogen gas is consumed by the hydrogen consumer, causing the pressure to drop and fall down (inflow).
- the hydrolysis reaction can be controlled automatically.
- FIG. 1 is an overall view of an embodiment of the present invention and shows an overall outline.
- FIG. 2 shows a cross section of the whole and a part where a small hydrogen generating container according to the present invention is mounted.
- FIG. 3 shows a cross section of the whole and a part of a medium-sized and large-sized hydrogen generating container according to one embodiment of the present invention.
- FIG. 4 shows an overall cross section of a hydrogen generation container that does not use battery elements in one embodiment of the present invention.
- the functional substance is a hydrogen storage alloy
- the materials are generally known as Ca, La, Mg, Ni, Ti, etc., as well as the third element V, etc.
- hydrogen is stored and the fine particles of hydrogen storage material are formed by initial pulverization or mechanical pulverization. It is manufactured.
- metal or alloy particles or Mg particles are placed in a pressure vessel and high-pressure hydrogen is introduced, and one end of the functional substance is heated at high temperature and ignited to cause hydrogenation.
- Fine powder in the nanometer range is manufactured.
- non-equilibrium (amorphous) fine powder is produced by cooling a gasified material heated at a high temperature by one laser irradiation.
- a functional substance using a hydrogen adsorbing material and a hydrogen storage alloy for example, a graphite material or a carbon-based material powder having an amorphous structure and one or more of hydrogen storage alloy, carbide or oxide are used.
- a fine powder in the nanometer range of a functional substance is produced by mixing powders of more than seeds and using an inert gas or the like by mechanical dusting.
- the specific surface area is about 45 m 2 Z g. If the particle size is 0.5 iU m, the specific surface area is about 1 m 2 Z g. Compared with the fine powder in the nanometer range, the surface area per unit mass is much higher. In addition to hydrogen storage, hydrogen and methane adsorption functions, as well as catalytic functions such as deodorization and decomposition, the reaction time per unit weight will be shortened by hydrolysis.
- the functional material is a halogen element such as iodine or a compound thereof.
- Oxygen group elements such as sulfur and selenium or alloys or compounds thereof.
- Nitrogen group elements such as arsenic, antimony and bismuth, or alloys or compounds thereof.
- Carbon group elements such as carbon, silicon and tin, their alloys or their compounds.
- Alkali metal elements such as lithium, sodium and force lithium, or alloys or compounds thereof.
- Al strength earth metal elements such as perillium, magnesium, calcium, alloys thereof or compounds thereof. Powder, cadmium, mercury zinc, cadmium, elemental mercury or its alloys or compounds.
- Boron group elements such as boron, aluminum, and gallium, or alloys or compounds thereof.
- Transition elements of the fourth period such as titanium, chromium, manganese, iron and nickel, transition elements of the fifth period such as zirconium, ruthenium and palladium, and transition elements of the sixth period such as lanthanum, tantalum and platinum
- transition elements of the 7th period such as thorium, and these transition elements or alloys or their compounds.
- One or more of these materials are selected and used as functional substances as required.
- the manufactured functional substance of fine powder in the nanometer range goes through a coating process.
- Low-temperature thermoplastic aliphatic polyester Teeramac / Unitica
- Polyolefin-based Arrowbase / Unitica, etc.
- tetrafluorinated ethylene etc.
- the coating material is dried at 110 ° C to 150 ° C and glass transitioned to crystallize.
- a film with a thickness of "! ⁇ 5jtim" has been formed.
- the plastic organic solvent polymer can be used as an organic solvent.
- the aqueous solution is dried and then pulverized into powder.
- a film with a thickness of 1-5 iWm after crystallization can be formed around the particles of the substance.
- the film material is glass-transduced by heat treatment at 1 10 ° C to 150 ° C using an electrothermal pressure bonding nozzle, etc. A coating is applied.
- the manufactured functional substance is dried or heated after being applied to the inside or outside of the target device or the pipe in the device, or into the groove of the corrugated plate, or to the electrode after the paste kneaded with the binder is applied. Solid bonded. If necessary, a film is formed by applying a water-soluble or organic solvent-soluble plastic polymer resin diluted with a solvent from the solidified surface.
- a fluoropolymer such as polytetrafluoroethylene (PTFE), polychlorofluoroethylene (PCTFE), polyvinylidene fluoride (PVDF), or a known polymer resin such as styrene butadiene rubber or carboxycellulose is used.
- PTFE polytetrafluoroethylene
- PCTFE polychlorofluoroethylene
- PVDF polyvinylidene fluoride
- a known polymer resin such as styrene butadiene rubber or carboxycellulose
- magnesium or magnesium hydride powder for example, magnesium or magnesium hydride powder, or a mixture of the powder and a powder obtained by drying an aliphatic polyester resin, etc., and glass transition is performed by heating. What is crushed to a particle size is sealed in a sealed container or bag filled with inert gas.
- Example 2 The verification of hydrolysis and electromotive force using magnesium (Mg) or magnesium hydride (Mg H2) as a functional substance is described.
- the experimental method was started by pouring 5 cc of each of three types of normal temperature (20 ° C) aqueous solutions into the sample in the test tube. If the free-running reaction was slow, the solution was observed and measured while gradually heating the aqueous solution. did.
- aqueous solution 1 water (H20) did not react at all, and a slight bubble was confirmed on the particle surface at heating 90 ° C.
- Aqueous solution 2 Chenic acid (C6H807) The 8% aqueous solution reacted vigorously and the reaction was completed in less than 2 minutes as the temperature rose.
- aqueous solution 3 nigari (hexahydrate magnesium chloride MgC I2-6H20), the reaction was slow, and as the reaction proceeded quickly with heating, an increase in bubbles was confirmed at 90 ° C.
- aqueous solution 1 water (H20), and the rise of bubbles was confirmed by heating 90.
- Aqueous solution 2 Chenic acid (C6H807) The 8% aqueous solution reacted vigorously, and the reaction was completed in less than 1.5 minutes as the temperature rose.
- Aqueous solution 3 The reaction was fast, and as the temperature rose due to self-heating with time, the bubble was confirmed to rise violently at 90 ° C.
- the positive electrode current collector of the product is formed in a net-like shape by applying powdered activated carbon, graphite, catalyst, etc. mixed with fluororesin to copper foil and firing.
- reaction formula of the experiment and the measured value of the electromotive force are as follows: Positive reaction formula: 2Mg ⁇ 2Mg 2+ + 4 ⁇ "( ⁇ £ s AlluBnt ⁇ ⁇ » ⁇ , negative reaction formula: 0 2 + 2 ⁇ 2 0 + 4 ⁇ " -* 4 OH—, total reaction formula: 2Mg + 0 2 + 2H 2 0 ⁇ 2Mg (OH) 2 i, initial electromotive force is 2.7 V.
- Lithium battery with magnesium as negative battery The theoretical electromotive force of air and magnesium is 2.7 V, but at the same time the hydrolysis reaction (reaction formula: MgH2 + 2H 2 0 ⁇ Mg 2+ + It gradually decreases due to polarization resistance caused by multiple ions due to 20H— + 2H 2 T).
- the measured value of hydrogen gas generation was about 650 c c / g (magnesium weight ratio 6 wt%). Since the amount of electricity and magnesium decrease are in a relative relationship, Table 1 shows the relationship between the amount of electricity and magnesium (Mg) decrease, and the relationship between the negative electrode area and current using Faraday's law. Shows the draft of the numerical value that was issued. 1
- FIG. 1 shows that the anode 6 of the battery element, the separator 4 and the functional substance 2 are installed inside the hydrogen generation vessel 1.
- the lead electrode 3 and the load device 10 are connected by an electric wire and energized, and the other hydrogen consumer 30 and the hydrogen pipe 12 are connected and connected.
- the entire apparatus 100 of the present invention is constituted.
- the power generation device is a mobile device 40 in which the hydrogen generation container 1 is incorporated in the cellular phone 40.
- the hydrogen generation container 1 is laminated. This is an example 10 3 of a medium-sized and large-sized apparatus.
- the positive electrode 6 is a functional material of the diffusion layer 5 and is made of a metal or alloy such as Ni or Mg Ti.
- a metal oxide powder, powdered activated carbon or graphite mixed in a fluororesin is applied to the inner surface of the foil and fired to form a net, and the lead wire is connected to the electrode foil.
- the anode 6 in the case where the hydrogen generating container 1 is a secluded secondary battery and uses oxygen or the like as the active material, the metal is used as a functional material for the diffusion layer 5 in the precursor solution, such as N TiO or Mg Ti system. It is formed by applying metal oxide powder in addition to metals and alloys to the inner surface of the foil foil and firing it, and the lead wire is connected to the electrode foil.
- Separator 4 consists of a solid polymer electrolyte film, glass fiber non-woven fabric, etc. mixed with gel material such as acrylic acid-based resin or natto yarn component, natto resin synthesized by irradiating polyglutamic acid with radiation. It is provided to extend from the battery element component to the liquid container 20 so that it can be used to improve the power generation function and suck up water or an aqueous solution (electrolyte) 21 so that sufficient water can be replenished.
- gel material such as acrylic acid-based resin or natto yarn component, natto resin synthesized by irradiating polyglutamic acid with radiation.
- the separator 4 is not particularly required for a gel material. However, as in the case of the separator 4 in FIG. If the side is opened, it is provided with an electrolyte using non-woven cloth and gel material.
- the negative electrode 3 is provided with the functional substance 2 attached on the inner surface side, and on the outer surface side, a spring 25 is sandwiched between the battery element so that the battery element adheres and the reaction and conductivity are enhanced.
- the lead wire is connected to the electrode foil.
- the functional substance 2 attached to the inner surface of the negative electrode 3 is a plate-like lump of magnesium (Mg), debris, or magnesium hydride (Mg) when the hydrogen generation vessel 1 is hydrolyzed and functions as a primary battery. coarse particles of H 2) is solidified, or if the secondary battery function, flour powder of magnesium coated with plastic polymer or metal (M g) is molded by hardening a binding material, lead wire It is joined to the electric foil provided.
- the material and form of the battery element are not specified, and generally known ones can be used.
- a functional polymer powder is coated or adhered using a plastic polymer agent, the coating damage is self-repaired and scattering is prevented, thereby improving durability.
- Durability can be improved by adopting alkaline button batteries, nickel-cadmium batteries, nickel metal hydride batteries, lithium-ion batteries, lead-acid batteries, etc. in the same way.
- aqueous solution In the liquid container 20, water or bittern (magnesium hexahydrate Mg CI 2-6H20) aqueous solution is used as the aqueous solution (electrolyte) 21, but depending on the functional substance of the battery element, potassium hydroxide Known electrolytes such as (KOH), sodium hydroxide (NaOH), and non-aqueous solutions are selected and injected according to the battery configuration and purpose.
- KOH potassium hydroxide
- NaOH sodium hydroxide
- non-aqueous solutions are selected and injected according to the battery configuration and purpose.
- a hydrogen gas pipe socket with the hydrogen demand body 30 and a separator from the liquid vessel 20 4 is provided with a sealed connection port for sending water or an aqueous solution (electrolyte) to 4 so that the hydrogen generating container 1 can be detached and attached.
- the hydrogen consumer 30 is a fuel cell for a battery, a hydrogen engine for a hydrogen engine, a hydrogen jet engine for fusing or welding, a hydrogen burner for fusing or welding, and a hydrogen gas such as a hydrogen pump for hydrogen stage. It is an apparatus that uses the gas and is integrated with the target apparatus and connected through a hydrogen pipe, so that hydrogen gas is supplied without accumulating in the hydrogen generation container 1.
- a single cell or a hydrogen generation container 1 made of battery elements may be stacked to facilitate use in a field where hydrogen consumption is random due to high-voltage power, such as a fuel cell vehicle.
- air leaks from the inside can be prevented by pumping air 22 with a blower pump to enhance the reaction of the anode and increase the external pressure.
- the series of operations of the hydrogen generating container 1 configured in this way is the case of a primary battery.
- the load device 10 When the load device 10 is turned on, the active material inside the hydrogen generating container 1 is turned on. Electrons from the lead wire reach the anode 6 through the load device 10 as a current from the lead wire, and at the same time, the active material of the negative electrode 3 is oxidized and ionized to elute into the electrolyte, and the ions pass through the separator 4.
- the active material for example, hydrated nickel gel, reacts with the reached electrons.
- the negative contact 3 is a functional substance for hydrogenation
- the functional substance is altered and scraped by oxidation and ionization from the surface side, and the hydrogen atoms fixed between the crystals are fixed. Since two atoms are bonded to form hydrogen molecules, hydrogen gas is generated.
- One of the hydrogen gas is dissolved in the electrolyte and ionized, and the separator (4) reacts with the oxygen (O) etc. of the active material air (22) in the diffusion layer (5) of the anode (6), On the other hand, the remaining hydrogen gas flows to the hydrogen consumer 30 and flows through the hydrogen pipe 12.
- the load device 10 when the load resistance is lowered, the amount of current increases and hydrogen gas is generated more. When the switch is set to OFF, the generation of hydrogen gas is minimized.
- the discharge is applied to the load device 1
- the switch of 0 When the switch of 0 is turned on, if it falls from the functional material of the negative electrode 3 of the hydrogen generation vessel 1, the stored hydrogen atoms elute into the electrolyte and ionize and pass through the separator 4 to the diffusion layer 5 of the anode 6.
- the electrons reach the anode 6 through the load device 10 as a current through the conductive wire, so that the hydrogen ions and the electrons that have reached the oxide (O), nitric oxide, etc. react.
- hydrogen gas is dissolved in the electrolyte using a hydrogen permeable membrane and stored in a negative active material.
- the other method is to electrolyze water by connecting to both batteries using an external power source, and to store the generated hydrogen in the negative active material.
- the structure of the hydrogen generation container having such a battery element is advantageous because the polarization resistance is lowered.
- substances can be generated and reduced using various electrolytes and ion reactions.
- Example 1 04 will be described with reference to FIG. 4.
- the hydrogen generation vessel 1 is provided with a reaction chamber 29 in the lower part, and is a plate-like lump or piece, or a solidified powder or powder.
- a functional substance 2 of various forms or a hydrogenated functional substance 2 is mounted, a liquid chamber 28 is provided in the upper part, and an aqueous solution (electrolyte) 21 is placed.
- a check valve 3 7 is provided in the hydrogen generation vessel 1 in the communication pipe between the liquid chamber 2 8 and the reaction chamber 29, and the communication pipe between the bottom of the reaction chamber 29 and the upper part of the liquid chamber 28.
- a check valve 3 8 is provided, and a hydrogen pipe 12 connected to the hydrogen demand body 30 is connected to the upper part of the reaction chamber 29, and a plurality of similar hydrogen generation vessels 1 are joined in parallel. Has been.
- the aqueous solution (electrolyte) 2 1 can react with harmful substances when magnesium chloride (Mg C,) is used. There is no generation and a known aqueous solution (electrolytic solution) can be selected and used.
- hydrogenated functional substances generate a large amount of hydrogen gas from both hydrolysis and hydride, the amount of water produced, condensed and recovered by the hydrogen consumer is considered to be reduced to the atmosphere. However, since the amount of water necessary for hydrolysis can be ensured, it is not necessary to replenish water from the outside when the produced water is circulated into the liquid container again.
- a hydrogen generation vessel When a hydrogen generation vessel is configured in this way, the series of operations is stopped by pushing up (outflowing) the aqueous solution (electrolyte) 2 1 with the pressure of hydrogen gas generated using the siphon phenomenon.
- the hydrogen consumer 30 consumes the generated hydrogen gas, and the pressure drops, causing the aqueous solution (electrolyte) 2 1 to fall (inflow) and the aqueous solution (electrolyte) 2 1 and the functional substance.
- the hydrolysis reaction with 2 is started, and control is automatically performed without using an electronic control unit.
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- Chemical & Material Sciences (AREA)
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- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Sustainable Energy (AREA)
- Health & Medical Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Combustion & Propulsion (AREA)
- General Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Hybrid Cells (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Fuel Cell (AREA)
Description
Claims
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2007279876A AU2007279876A1 (en) | 2006-07-31 | 2007-06-05 | Power generating apparatus |
JP2008527682A JPWO2008015844A1 (ja) | 2006-07-31 | 2007-06-05 | 発電装置 |
EP07745131A EP2048110A1 (en) | 2006-07-31 | 2007-06-05 | Power generating apparatus |
CA002659513A CA2659513A1 (en) | 2006-07-31 | 2007-06-05 | Power generating apparatus |
MX2009001132A MX2009001132A (es) | 2006-07-31 | 2007-06-05 | Aparato de generador de potencia. |
BRPI0715461-5A BRPI0715461A2 (pt) | 2006-07-31 | 2007-06-05 | aparelho de geraÇço de energia, recipiente de geraÇço de hidrogÊnio, material funcional, e, mÉtodos para hidrogenar um material funcional, e para reduzir um material funcional |
US12/375,261 US20090324997A1 (en) | 2006-07-31 | 2007-06-05 | Power generating apparatus |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006-209157 | 2006-07-31 | ||
JP2006209157 | 2006-07-31 | ||
JP2007-142528 | 2007-04-27 | ||
JP2007142528A JP2010042933A (ja) | 2007-04-27 | 2007-04-27 | 水素需要装置の水素発生容器 |
Publications (1)
Publication Number | Publication Date |
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WO2008015844A1 true WO2008015844A1 (fr) | 2008-02-07 |
Family
ID=38997028
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/JP2007/061844 WO2008015844A1 (fr) | 2006-07-31 | 2007-06-05 | Appareil générateur de courant |
Country Status (9)
Country | Link |
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US (1) | US20090324997A1 (ja) |
EP (1) | EP2048110A1 (ja) |
JP (1) | JPWO2008015844A1 (ja) |
KR (1) | KR20090060996A (ja) |
AU (1) | AU2007279876A1 (ja) |
BR (1) | BRPI0715461A2 (ja) |
CA (1) | CA2659513A1 (ja) |
MX (1) | MX2009001132A (ja) |
WO (1) | WO2008015844A1 (ja) |
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JP2009269811A (ja) * | 2008-04-30 | 2009-11-19 | Hyundai Motor Co Ltd | 水素発生装置 |
WO2010116530A1 (ja) * | 2009-04-10 | 2010-10-14 | 株式会社テクノバンク | 洋上自然エネルギー変換装置 |
JP4778111B1 (ja) * | 2010-06-29 | 2011-09-21 | 貴夫 舩田 | 水酸化マグネシウム及びその製造方法 |
WO2011125150A1 (ja) * | 2010-04-01 | 2011-10-13 | 株式会社アクモ | マグネシウム電池 |
JP2012038697A (ja) * | 2010-07-15 | 2012-02-23 | Toyota Motor Corp | 負極材料、金属二次電池、および負極材料の製造方法 |
WO2013098997A1 (ja) | 2011-12-28 | 2013-07-04 | 合同会社 矢部学術振興会 | 電池システム |
JP2014082059A (ja) * | 2012-10-15 | 2014-05-08 | Rohm Co Ltd | 発電装置 |
JP2014521583A (ja) * | 2011-07-25 | 2014-08-28 | エイチ2 カタリスト、エルエルシー | 水素を生成するための方法およびシステム |
JP2016033866A (ja) * | 2014-07-31 | 2016-03-10 | 日本碍子株式会社 | 亜鉛空気二次電池 |
JP2017188483A (ja) * | 2014-10-17 | 2017-10-12 | 株式会社東洋製作所 | マグネシウム電池 |
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TWI371427B (en) | 2009-03-13 | 2012-09-01 | Ind Tech Res Inst | Solid state hydrogen fuel with polymer matrix and fabrication methods thereof |
TWI371888B (en) | 2009-04-16 | 2012-09-01 | Ind Tech Res Inst | Hydrogen supply device |
FR2948654B1 (fr) * | 2009-07-30 | 2015-01-16 | Gerkaro | Cogeneration d'energie electrique et d'hydrogene |
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- 2007-06-05 MX MX2009001132A patent/MX2009001132A/es unknown
- 2007-06-05 CA CA002659513A patent/CA2659513A1/en not_active Abandoned
- 2007-06-05 AU AU2007279876A patent/AU2007279876A1/en not_active Abandoned
- 2007-06-05 WO PCT/JP2007/061844 patent/WO2008015844A1/ja active Application Filing
- 2007-06-05 BR BRPI0715461-5A patent/BRPI0715461A2/pt not_active Application Discontinuation
- 2007-06-05 EP EP07745131A patent/EP2048110A1/en not_active Withdrawn
- 2007-06-05 KR KR1020097004364A patent/KR20090060996A/ko not_active Application Discontinuation
- 2007-06-05 US US12/375,261 patent/US20090324997A1/en not_active Abandoned
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JP2009269811A (ja) * | 2008-04-30 | 2009-11-19 | Hyundai Motor Co Ltd | 水素発生装置 |
WO2010116530A1 (ja) * | 2009-04-10 | 2010-10-14 | 株式会社テクノバンク | 洋上自然エネルギー変換装置 |
WO2011125150A1 (ja) * | 2010-04-01 | 2011-10-13 | 株式会社アクモ | マグネシウム電池 |
JP4778111B1 (ja) * | 2010-06-29 | 2011-09-21 | 貴夫 舩田 | 水酸化マグネシウム及びその製造方法 |
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JP2017188483A (ja) * | 2014-10-17 | 2017-10-12 | 株式会社東洋製作所 | マグネシウム電池 |
Also Published As
Publication number | Publication date |
---|---|
AU2007279876A1 (en) | 2008-02-07 |
EP2048110A1 (en) | 2009-04-15 |
BRPI0715461A2 (pt) | 2013-01-22 |
JPWO2008015844A1 (ja) | 2009-12-17 |
MX2009001132A (es) | 2009-04-27 |
KR20090060996A (ko) | 2009-06-15 |
CA2659513A1 (en) | 2008-02-07 |
US20090324997A1 (en) | 2009-12-31 |
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