C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
C25B 9/21 - Cells comprising dimensionally-stable non-movable electrodesAssemblies of constructional parts thereof with diaphragms two or more diaphragms
2.
CERAMIC CATALYST, METHOD OF PRODUCTION AND USES THEREOF
233 associated with cobalt oxide including at least Co2+and Co3+233 with an aqueous solution comprising Co2+2323233 associated with cobalt oxide including at least Co2+and Co3+ oxidation states with a solution comprising borohydride compound and proton donor solvent.
inter aliainter alia, an electrolytic cell comprising an anode region comprising an anode, a cathode region comprising a cathode and configured for operating within an electrolyte organic solvent and a barrier partitioning the anode region from the cathode, the barrier being selective for alkali metal cation conduction.
A system for releasing Hydrogen gas from a Hydrogen liquid carrier is described. The system may be used to provide hydrogen gas for a respective fuel cell. The system comprises a water recycling module placed in fluid communication with the fuel cell and with a hydrogen liquid carrier assembly and being configured and operable to capture water released from the fuel cell and convey the captured water to the hydrogen liquid carrier assembly for use in producing the Hydrogen liquid carrier. The captures water may be in liquid or gas phase.
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
5.
A CATALYST FOR GENERATING HYDROGEN AND METHOD OF ITS PRODUCTION
B01J 27/185 - PhosphorusCompounds thereof with iron group metals or platinum group metals
B01J 27/18 - PhosphorusCompounds thereof containing oxygen with metals
B01J 37/02 - Impregnation, coating or precipitation
C25D 5/00 - Electroplating characterised by the processPretreatment or after-treatment of workpieces
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
A system and respective method for releasing hydrogen gas from hydrogen carrier are described. The system comprises a first reaction chamber carrying one or more catalysts and configured to release hydrogen gas from hydrogen liquid carrier, and a second reaction chamber. The second reaction chamber comprises a liquid inlet port connectable to said first reaction chamber enabling flow of spent hydrogen carrier liquid from said first reaction chamber, a gas outlet port for removing hydrogen gas released within said second reaction chamber, and a mounting mechanism configured for carrying one or more reactants. The one or more reactants are selected to react with the spent hydrogen carrier liquid for release of an additional portion of hydrogen gas from said spent hydrogen carrier liquid.
C01B 3/00 - HydrogenGaseous mixtures containing hydrogenSeparation of hydrogen from mixtures containing itPurification of hydrogen
B01J 19/18 - Stationary reactors having moving elements inside
B25J 9/02 - Programme-controlled manipulators characterised by movement of the arms, e.g. cartesian co-ordinate type
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
C01B 6/15 - Metal borohydridesAddition complexes thereof
B01J 19/00 - Chemical, physical or physico-chemical processes in generalTheir relevant apparatus
A system for releasing Hydrogen gas from a Hydrogen liquid carrier is described. The system may be used to provide hydrogen gas for a respective fuel cell. The system comprises a water recycling module placed in fluid communication with the fuel cell and with a hydrogen liquid carrier assembly and being configured and operable to capture water released from the fuel cell and convey the captured water to the hydrogen liquid carrier assembly for use in producing the Hydrogen liquid carrier. The captures water may be in liquid or gas phase.
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
an inlet for receiving the hydrogen liquid carrier; and at least one cartridge arranged within the housing. The cartridge may include at least one catalyst configured to cause a release of hydrogen gas when exposed to the hydrogen liquid carrier. The modular device may include a gas outlet for expelling the hydrogen gas released in the modular device and a liquid outlet for expelling spent hydrogen liquid carrier.
H01M 8/04082 - Arrangements for control of reactant parameters, e.g. pressure or concentration
B01J 16/00 - Chemical processes in general for reacting liquids with non-particulate solids, e.g. sheet materialApparatus specially adapted therefor
B01J 19/00 - Chemical, physical or physico-chemical processes in generalTheir relevant apparatus
B01J 19/18 - Stationary reactors having moving elements inside
B01J 27/185 - PhosphorusCompounds thereof with iron group metals or platinum group metals
C01B 3/04 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of inorganic compounds, e.g. ammonia
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
C01B 3/32 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
F17C 11/00 - Use of gas-solvents or gas-sorbents in vessels
H01M 8/065 - Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dissolution of metals or alloysCombination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dehydriding metallic substances
9.
BATCH SYSTEMS AND METHODS FOR HYDROGEN GAS EXTRACTION FROM A LIQUID HYDROGEN CARRIER
A system for extracting hydrogen gas from a liquid hydrogen carrier may include a hydrogen gas reactor, a catalyst for facilitating extraction of the hydrogen gas from the liquid hydrogen carrier, and a reservoir for containing the liquid hydrogen carrier and a spend liquid hydrogen carrier. The system may be configured to regulate a flow of liquid hydrogen carrier in and out of the hydrogen gas reactor, to move a catalyst relative to a volume of the liquid hydrogen carrier, and to provide a continuous flow of the hydrogen gas, in response to a demand for the hydrogen gas.
A modular device for generating hydrogen gas from a hydrogen liquid carrier may include a housing; an inlet for receiving the hydrogen liquid carrier; and at least one cartridge arranged within the housing. The cartridge may include at least one catalyst configured to cause a release of hydrogen gas when exposed to the hydrogen liquid carrier. The modular device may include a gas outlet for expelling the hydrogen gas released in the modular device and a liquid outlet for expelling spent hydrogen liquid carrier.
B01J 19/24 - Stationary reactors without moving elements inside
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
A fuel tank for storing a hydrogen liquid carrier and a spent hydrogen liquid carrier includes a substantially rigid exterior tank wall including a first chamber and a second chamber. The first chamber is fluidly disconnected from the second chamber, and the second chamber includes a dynamically expandable and contractible enclosure, the enclosure being configured to define a dynamic boundary between the hydrogen liquid carrier and spent hydrogen liquid carrier. The fuel tank also includes a first channel in flow communication with one of the first chamber or the second chamber and a second channel in flow communication with another of the first chamber or the second chamber, wherein the first channel and the second channel are flow connected such that a flow through one of the first or second channels is returned to the another of the first or second channels, and that during the flow, the dynamic boundary changes position causing a change in a volume of the second chamber.
B01J 19/24 - Stationary reactors without moving elements inside
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
F17C 11/00 - Use of gas-solvents or gas-sorbents in vessels
A reaction chamber for generating hydrogen gas using a hydrogen liquid carrier line may include a channel including a catalyst for causing the hydrogen gas to be produced from a hydrogen liquid carrier, the channel including an inlet end for the hydrogen liquid carrier and an outlet end for a spent carrier. The reaction chamber may also include a valve for controlling a rate of flow of the hydrogen liquid carrier flowing through the channel; a gas outlet for evacuating the hydrogen gas generated in the channel; and at least one processor configured to receive at least one indicator of a demand for the hydrogen gas and to control the valve to adjust the rate of flow of the hydrogen liquid carrier to meet the demand for the hydrogen gas.
B01J 16/00 - Chemical processes in general for reacting liquids with non-particulate solids, e.g. sheet materialApparatus specially adapted therefor
B01J 19/24 - Stationary reactors without moving elements inside
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
13.
BATCH SYSTEMS AND METHODS FOR HYDROGEN GAS EXTRACTION FROM A LIQUID HYDROGEN CARRIER
A system for extracting hydrogen gas from a liquid hydrogen carrier may include a hydrogen gas reactor, a catalyst for facilitating extraction of the hydrogen gas from the liquid hydrogen carrier, and a reservoir for containing the liquid hydrogen carrier and a spend liquid hydrogen carrier. The system may be configured to regulate a flow of liquid hydrogen carrier in and out of the hydrogen gas reactor, to move a catalyst relative to a volume of the liquid hydrogen carrier, and to provide a continuous flow of the hydrogen gas, in response to a demand for the hydrogen gas.
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
B01J 19/24 - Stationary reactors without moving elements inside
A modular device for generating hydrogen gas from a hydrogen liquid carrier may include a housing;
an inlet for receiving the hydrogen liquid carrier; and at least one cartridge arranged within the housing. The cartridge may include at least one catalyst configured to cause a release of hydrogen gas when exposed to the hydrogen liquid carrier. The modular device may include a gas outlet for expelling the hydrogen gas released in the modular device and a liquid outlet for expelling spent hydrogen liquid carrier.
H01M 8/04082 - Arrangements for control of reactant parameters, e.g. pressure or concentration
F17C 11/00 - Use of gas-solvents or gas-sorbents in vessels
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
C01B 3/32 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
B01J 27/185 - PhosphorusCompounds thereof with iron group metals or platinum group metals
H01M 8/065 - Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dissolution of metals or alloysCombination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dehydriding metallic substances
B01J 16/00 - Chemical processes in general for reacting liquids with non-particulate solids, e.g. sheet materialApparatus specially adapted therefor
B01J 19/00 - Chemical, physical or physico-chemical processes in generalTheir relevant apparatus
B01J 19/18 - Stationary reactors having moving elements inside
C01B 3/04 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of inorganic compounds, e.g. ammonia
A fuel tank for storing a hydrogen liquid carrier and a spent hydrogen liquid carrier includes a substantially rigid exterior tank wall including a first chamber and a second chamber. The first chamber is fluidly disconnected from the second chamber, and the second chamber includes a dynamically expandable and contractible enclosure, the enclosure being configured to define a dynamic boundary between the hydrogen liquid carrier and spent hydrogen liquid carrier. The fuel tank also includes a first channel in flow communication with one of the first chamber or the second chamber and a second channel in flow communication with another of the first chamber or the second chamber, wherein the first channel and the second channel are flow connected such that a flow through one of the first or second channels is returned to the another of the first or second channels, and that during the flow, the dynamic boundary changes position causing a change in a volume of the second chamber.
H01M 8/04082 - Arrangements for control of reactant parameters, e.g. pressure or concentration
F17C 11/00 - Use of gas-solvents or gas-sorbents in vessels
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
C01B 3/32 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
B01J 27/185 - PhosphorusCompounds thereof with iron group metals or platinum group metals
H01M 8/065 - Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dissolution of metals or alloysCombination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dehydriding metallic substances
16.
Method for catalytically induced hydrolysis and recycling of metal borohydride solutions
C01B 6/21 - Preparation of borohydrides of alkali metals, alkaline earth metals, magnesium or berylliumAddition complexes thereof, e.g. LiBH4.2N2H4, NaB2H7
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
C01B 6/17 - Preparation from boron or inorganic compounds containing boron and oxygen
B01J 37/34 - Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves
B01J 27/185 - PhosphorusCompounds thereof with iron group metals or platinum group metals
C01B 3/34 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
17.
Method for catalytically induced hydrolysis and recycling of metal borohydride solutions
C01B 3/34 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
B01J 37/34 - Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves
B01J 27/185 - PhosphorusCompounds thereof with iron group metals or platinum group metals
C01B 3/06 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
C01B 6/21 - Preparation of borohydrides of alkali metals, alkaline earth metals, magnesium or berylliumAddition complexes thereof, e.g. LiBH4.2N2H4, NaB2H7
C01B 6/17 - Preparation from boron or inorganic compounds containing boron and oxygen
patents
