The present invention concerns a device and a process for the storage and restitution of heat which comprises at least two concentric heat storage volumes (TES1, TES2, TES3). The walls (2) delimiting these storage volumes are configured in a manner such that the thickness of the wall delimiting the central storage volume is greater than the thickness of the wall delimiting the peripheral storage volume.

The present invention concerns a device and a process for the storage and restitution of heat which comprises at least two concentric heat storage volumes (TES1, TES2, TES3). The walls (2) delimiting these storage volumes are configured in a manner such that the thickness of the wall delimiting the central storage volume is greater than the thickness of the wall delimiting the peripheral storage volume.

An apparatus for performing energy transformation between thermal energy and acoustic energy is in a thermoacoustic transducer apparatus is disclosed. The acoustic energy is associated with a periodic flow of a working fluid within an acoustic power loop of the thermoacoustic transducer. The apparatus includes a common central plenum having a first fluid port for providing fluid communication with the acoustic power loop, and a plurality of discrete cylindrical thermal converters radially arranged about the plenum, each thermal converter including a regenerator. The apparatus also includes a second fluid port for providing fluid communication between the thermal converter and the acoustic power loop, and fluid flow passages in fluid communication with the plenum and extending through the regenerator to the second fluid port.

The invention is directed to a process to increase pressure and temperature of a feed gas by means of indirect heat exchange against a fluid having a higher temperature to obtain a gas high in pressure and temperature in a system. The system comprises a fluidly interconnected inlet zone, a heat exchange zone, a product gas zone and a low pressure outlet zone.

The invention is directed to a process to increase pressure and temperature of a feed gas by means of indirect heat exchange against a fluid having a higher temperature to obtain a gas high in pressure and temperature in a system. The system comprises a fluidly interconnected inlet zone, a heat exchange zone, a product gas zone and a low pressure outlet zone.

A solid hydrogen storage device is provided and has a shape in which a polygonal cross section extends in a longitudinal direction. The device includes a plurality of heat exchange tubes having heat transfer fluid flowing therein and are disposed inside the storage device in a polygonal shape corresponding to the cross section of the storage device while extending in the same direction as an extending direction of the storage device. A hydrogen storage body is disposed inside the storage device to absorb or release heat through a reaction that releases or bonds with hydrogen and to exchange heat with the heat exchange tubes.

A solid hydrogen storage device is provided and has a shape in which a polygonal cross section extends in a longitudinal direction. The device includes a plurality of heat exchange tubes having heat transfer fluid flowing therein and are disposed inside the storage device in a polygonal shape corresponding to the cross section of the storage device while extending in the same direction as an extending direction of the storage device. A hydrogen storage body is disposed inside the storage device to absorb or release heat through a reaction that releases or bonds with hydrogen and to exchange heat with the heat exchange tubes.

A hydrocarbon burner for an enclosed environment includes a heat exchanger having a first heat exchanger inlet connected to an inlet of the hydrocarbon burner and a first heat exchanger outlet connected to a heater, and a second heat exchanger inlet connected to a reactor outlet and a second heat exchanger outlet connected to an outlet of the hydrocarbon burner. A reactor includes a reactor inlet, the reactor outlet, and a catalyst mixture disposed in a reactor bed between the reactor inlet and the reactor outlet. The heater connects the first heat exchanger outlet to the reactor inlet. The reactor is a low temperature reactor configured to convert at least one hydrocarbon to at least one of H2O and CO2.

A hydrocarbon burner for an enclosed environment includes a heat exchanger having a first heat exchanger inlet connected to an inlet of the hydrocarbon burner and a first heat exchanger outlet connected to a heater, and a second heat exchanger inlet connected to a reactor outlet and a second heat exchanger outlet connected to an outlet of the hydrocarbon burner. A reactor includes a reactor inlet, the reactor outlet, and a catalyst mixture disposed in a reactor bed between the reactor inlet and the reactor outlet. The heater connects the first heat exchanger outlet to the reactor inlet. The reactor is a low temperature reactor configured to convert at least one hydrocarbon to at least one of H2O and CO2.

An energy accumulator for storing electrical energy in the form of heat energy comprising an electric heater for converting electrical energy into heat energy, a heat accumulator for storing the heat energy of the electric heater, and a heat exchanger for emitting heat energy from the heat accumulator. The heat accumulator comprises, at least, a plurality of metal rods arranged upright and serving to store heat energy from the electric heater; a base; and multiple supporting units, wherein each supporting unit supports one of the metal rods and is connected with the base. Furthermore described is a corresponding method for operating an energy accumulator of this type.