Abstract: A cryostorage system that includes: a cryocontainer operable to store hydrogen, the cryocontainer having an inner tank and an outer container; at least one cryopump, arranged in the inner tank, to deliver liquid hydrogen and/or gaseous hydrogen in one or more stages via an extraction line to a consumer at a pressure greater than a pressure in the inner tank; and a filling interface to facilitate filling of the inner tank at least in part via the extraction line and a spring-loaded non-return valve into the inner tank.

Abstract: A cryostorage system that includes: a cryocontainer operable to store hydrogen, the cryocontainer having an inner tank and an outer container; at least one cryopump, arranged in the inner tank, to deliver liquid hydrogen and/or gaseous hydrogen in one or more stages via an extraction line to a consumer at a pressure greater than a pressure in the inner tank; and a filling interface to facilitate filling of the inner tank at least in part via the extraction line and a spring-loaded non-return valve into the inner tank.

Abstract: A multi-cryostorage system that includes at least two cryocontainers for storing hydrogen. The at least two cryocontainers are connected in hydraulic communication via a cryogenic connecting line, and include a primary storage system having a primary inner tank and a primary outer container, and at least one secondary storage system having a secondary inner tank and a secondary outer container. A heat exchanger is operable to heat the hydrogen, and at least one cryopump is arranged in the primary inner tank to supply unpressurised liquid hydrogen and/or unpressurised gaseous hydrogen in one or more stages at low temperature, to the heat exchanger for delivery to a consumer at a pressure higher than the pressure in the primary inner tank.

Abstract: A cryostorage system that includes a cryocontainer operable to store liquid hydrogen and/or gaseous hydrogen, the cryocontainer having an inner tank and an outer container, and at least one cryopump, operable to operate at low temperatures, arranged in the inner tank to be fully surrounded, during normal operation, by cryogenic fluid, the cryopump delivering liquid hydrogen and/or gaseous hydrogen in one or more stages to a consumer at a pressure greater than a pressure in the inner tank.

Abstract: A liquid hydrogen reservoir and a method for operating a liquid hydrogen reservoir. The liquid hydrogen reservoir includes a cryostatic container operable to hold liquid hydrogen; a discharge line operable to discharge gaseous hydrogen in the cryostatic container; a boil-off management system (BMS), a return line, and a boil-off valve (BOV). The BMS that includes a mixing chamber operable to mix the gaseous hydrogen with ambient air, a catalyst arranged downstream of the mixing chamber and operable for a catalytic conversion of the gaseous hydrogen with the ambient air, and an exhaust gas line arranged downstream of the catalyst and operable to discharge the gas stream to the environment. The return line is operable to connect the exhaust gas line to the mixing chamber to facilitate a return flow of at least a partial stream of the exhaust gas line into the mixing chamber.

Abstract: Fuel cell device for propulsion of a motor vehicle, and a method for operating the same. The fuel cell and a cryogenic tank storing liquid hydrogen, a boil-off management system keeping the pressure in the cryogenic tank below a threshold, the boil-off management system includes a boil-off conduit fluidically connected to the cryogenic tank via a boil-off valve. A mixing chamber is configured to mix a first medium flowing through the boil-off conduit with a second medium flowing in through the air feed conduit. A catalytic converter is connected downstream of the mixing chamber, and an outlet is connected downstream of the catalytic converter. A fuel cell off-gas tract, such that after anode purge operation of the fuel cell, off-gas is discharged through the fuel cell off-gas tract, which is configured such that medium flowing through the fuel cell off-gas tract can be conducted selectively and/or partially into the air feed conduit of the boil-off management system.

Abstract: A boil-off management system for a cryotank includes a boil-off conduit which is fluidically connectable to a cryotank via a boil-off valve. The boil-off management system further includes an air feed conduit and a mixing chamber for mixing a first medium (e.g., hydrogen) flowing in through the boil-off conduit with a second medium (e.g., air and/or oxygen) flowing in through the air feed conduit. A catalytic converter is arranged downstream of the mixing chamber and an outlet downstream of the catalytic converter. At least one enrichment apparatus is provided and configured to temporarily increase the proportion of the first medium flowing in through the boil-off conduit in relation to the second medium flowing in through the air feed conduit at the catalytic converter.

Abstract: A liquid hydrogen store including a cryostatic container for holding the liquid hydrogen, a discharge line for discharge of gaseous hydrogen, a boil-off management system, a boil-off valve in the discharge line for selective opening and closing of a fluidic connection of the discharge line to the boil-off management system, a heat transport line, and one or more thermal contact members to establish thermal contact of the heat transport line with the boil-off management system.

Abstract: A liquid hydrogen reservoir and a method for operating a liquid hydrogen reservoir. The liquid hydrogen reservoir includes a cryostatic container operable to hold liquid hydrogen; a discharge line operable to discharge gaseous hydrogen in the cryostatic container; a boil-off management system (BMS), a return line, and a boil-off valve (BOV). The BMS that includes a mixing chamber operable to mix the gaseous hydrogen with ambient air, a catalyst arranged downstream of the mixing chamber and operable for a catalytic conversion of the gaseous hydrogen with the ambient air, and an exhaust gas line arranged downstream of the catalyst and operable to discharge the gas stream to the environment. The return line is operable to connect the exhaust gas line to the mixing chamber to facilitate a return flow of at least a partial stream of the exhaust gas line into the mixing chamber. The BOV is arranged in the discharge line and operable to selectively open and close a flow connection of the discharge line to the BMS.

Abstract: A storage container includes an inner tank to store a cryogenic liquid gas and an extraction system to permit extraction of the cryogenic liquid gas by a cryogenic liquid gas consumer. The extraction system includes an extraction line, a consumer line to facilitate extraction of the cryogenic liquid gas by the cryogenic liquid gas consumer, a return line to facilitate return of the cryogenic liquid gas to the inner tank, a heat transmitter to heat the cryogenic liquid gas extracted from the inner tank and transfer the cryogenic liquid gas to a gaseous phase, and a compressor to compress the gaseous cryogenic liquid gas. A first flow of the compressed cryogenic liquid gas is conducted to the cryogenic liquid gas consumer via the consumer line and a second flow of the compressed cryogenic liquid gas is returned to the inner tank via the return line.

Abstract: A storage container includes an inner tank to store a cryogenic liquid gas and an extraction system to permit extraction of the cryogenic liquid gas by a cryogenic liquid gas consumer. The extraction system includes an extraction line, a consumer line to facilitate extraction of the cryogenic liquid gas by the cryogenic liquid gas consumer, a return line to facilitate return of the cryogenic liquid gas to the inner tank, a heat transmitter to heat the cryogenic liquid gas extracted from the inner tank and transfer the cryogenic liquid gas to a gaseous phase, and a compressor to compress the gaseous cryogenic liquid gas. A first flow of the compressed cryogenic liquid gas is conducted to the cryogenic liquid gas consumer via the consumer line and a second flow of the compressed cryogenic liquid gas is returned to the inner tank via the return line.

Abstract: A pressure accumulator system, and a method of operating a pressure accumulator system. The method includes operatively connecting a tank neck to at least two pressure accumulator vessels having different admissible operating pressures, in which at least one of the pressure accumulator vessels has an admissible operating pressure lower than a maximum applicable pressure at the tank neck, simultaneously filling via the tank neck the at least two pressure accumulator vessels with a fluid medium, and preventing an inadmissible pressure rise in the pressure accumulator vessels with the lower admissible operating pressure during the simultaneous filling.

Abstract: A pressure accumulator system, and a method of operating a pressure accumulator system. The method includes operatively connecting a tank neck to at least two pressure accumulator vessels having different admissible operating pressures, in which at least one of the pressure accumulator vessels has an admissible operating pressure lower than a maximum applicable pressure at the tank neck, simultaneously filling via the tank neck the at least two pressure accumulator vessels with a fluid medium, and preventing an inadmissible pressure rise in the pressure accumulator vessels with the lower admissible operating pressure during the simultaneous filling.

Abstract: The apparatus for the collection and distribution of liquid in a column having at least one lamella collector and a distributor outflow system which is arranged below it. A side passage is contained in the or in each lamella collector and liquid outflow openings are arranged in a combination, as a result of which a hydrodynamic equalization for a liquid to be distributed results.

Abstract: The apparatus for the collection and distribution of liquid in a column comprises at least one lamella collector (200) and a distributor outflow system (300) which is arranged below it. A side passage (210) is contained in the or in each lamella collector and liquid outflow openings (214, 216, 332) are arranged in a combination, as a result of which a hydrodynamic equalisation for a liquid to be distributed results.