A hydrogen mixed gas generation apparatus includes a superheated vapor heating part that heats a raw water to generate a superheated vapor and further heats the superheated vapor to produce a mixed gas that includes a hydrogen gas, and a communication part that is communicable with a predetermined terminal device and transmits information to the terminal device. The superheated vapor heating part houses a reduction acceleration member and includes a heating pipe where the raw water flows therein, and a coil heater that is wound around the heating pipe. The reduction acceleration member includes a first metal member that is formed of a stainless steel and includes a cylindrical part where rod bodies respectively extend from both ends thereof and a second metal member that is formed of an iron and steel material and is housed in the cylindrical part in a state where a plurality thereof are bundled.

A hydrogen supply system supplying hydrogen, the hydrogen supply system including: a dehydrogenation reaction unit acquiring a hydrogen-containing gas by performing a dehydrogenation reaction of a raw material containing a hydride; and a control unit controlling the hydrogen supply system, in which in a case in which generation of the hydrogen-containing gas in the dehydrogenation reaction unit stops, the control unit causes the hydrogen supply unit to supply hydrogen to the dehydrogenation reaction unit, and the hydrogen supply unit supplies at least one of the hydrogen-containing gas between the dehydrogenation reaction unit and a vapor-liquid separating unit separating a dehydrogenation product from the hydrogen-containing gas and the hydrogen-containing gas separated by the vapor-liquid separating unit separating a dehydrogenation product from the hydrogen-containing gas to the dehydrogenation reaction unit.

Disclosed is a method of: providing a hydrogenated sp.sup.2 carbon allotrope, and releasing hydrogen gas from the carbon allotrope. The method may be used an apparatus having: a vessel for containing the hydrogenated sp.sup.2 carbon allotrope, a fuel cell capable of using hydrogen gas a fuel, and a tube for transporting hydrogen gas from the vessel to the fuel cell. The carbon allotrope may be made by: providing a mixture of an sp.sup.2 carbon allotrope and liquid ammonia, adding an alkali metal to the mixture, and sonicating the mixture to form a hydrogenated form of the carbon allotrope. The hydrogenated carbon can be at least 3.5 wt % hydrogen covalently bound to the carbon.

Disclosed is an apparatus and method of preparing synthetic fuel using natural gas extracted from a standard gas field on land or at sea as a raw material through a compact GTL process or a GTL-FPSO process. A parallel-type gas purification unit for controlling a molar ratio of synthetic gas and a concentration of carbon dioxide in the synthetic gas, in which a CO.sub.2 separation device and a bypass unit are disposed in parallel, is provided and, thus, the gas purification unit may prepare the synthetic gas by a steam carbon dioxide reforming (SCR) reaction using natural gas having different CO.sub.2 contents of various standard gas fields and then supply the synthetic gas having an optimum composition suitable for a Fischer-Tropsch synthesis reaction to prepare the synthetic fuel.

A fuel cell system includes a reformer generating a reformed gas from a fuel gas supplied from a fuel supplier by a reforming reaction to discharge a mixed gas of the fuel gas unreacted and the reformed gas, and including a catalyst device including a catalyst used for the reforming reaction and a fuel cell stack including an anode receiving the reformed gas generated at the reformer, a cathode receiving oxygen, and a reforming device generating a reformed gas from the unreacted fuel gas of the mixed gas supplied from the reformer by a reforming reaction to be provided to the anode and being installed integrally with or adjacent to the anode, and the reformer controls the amount of the unreacted fuel gas discharged from the reformer to increase and decrease a reforming amount inside the fuel cell stack based on a temperature of the fuel cell stack.

A combined hydrogen and electricity supply system for producing hydrogen, electrical Power (P) and co-production, the system including a variable electrical load for varying the amount of impedance on the system, a pre-reformer connected to a stream of carbonaceous fuel, a stream of steam and connected to a heating source. The pre-reformer produces a first reformate gas having at least hydrogen, carbon monoxide and unconverted carbonaceous fuel. The pre-reformer is responsive to the amount of heat provided by the heating source, a solid oxide fuel cell stack coupled to the variable electrical load and coupled to the first reformate gas. The ratio between electrical power (P) and amount of hydrogen produced depends at least on the variable electrical load and the heat provided by the heating source.

An energy production device may include: a supply device for hydrocarbon gas; energy converter configured to convert the energy supplied by the H.sub.2 into electrical, thermal, and/or mechanical energy; H.sub.2 producer fluidically between the supply device and the energy converter; the H.sub.2 producer including a plasmalysis reactor configured to generate plasmalysis of the hydrocarbon gas so as to produce at least one dihydrogen directed towards the energy converter; a controller configured to generate a control instruction for the H.sub.2 producer with information on H.sub.2 present in a H.sub.2 distribution area arranged fluidically between the plasmalysis reactor and the energy converter, the H.sub.2 distribution area including a storage assembly at the plasmalysis reactor outlet and hydraulically connected to the plasmalysis reactor and energy converter, the storage assembly including a compression device, storage tank, and expander, the compression device being positioned to transfer H.sub.2 exiting the plasmalysis reactor into the storage tank.

Low carbon hydrogen will play a crucial role in decarbonization of chemical complexes and manufacturing facilities. Depending on the application, different grades of low carbon hydrogen might be requiredfuel grade (90-99% H2 purity) or chemical grade (>99% H2 purity). The current invention describes a hydrogen production process based on autothermal reforming and CO2 capture to produce low carbon hydrogen with hydrogen rich offgas as part of the feedstock.

A hydrogen-producing device is provided which can start up without receiving an energy supply from the outside. This hydrogen-producing device 1 is provided with an input unit 11 which is connected to a hydrogen source 41, a reformer 12 which produces a hydrogen-containing gas, a hydrogen storage container 13, a fuel battery 15 which generates power using the hydrogen-containing gas, and a control unit 18. The hydrogen storage container 13 is connected to a fuel hydrogen supply path 16 for supplying hydrogen to the fuel battery 15, and to an external supply path 17 which supplies hydrogen to an external load 42. The control unit 18 stores a threshold value of the hydrogen-containing gas necessary for start-up of the fuel battery 15, and controls the amount stored in the hydrogen storage container 13 to be greater than or equal to the amount necessary for start-up of the fuel battery 15. Further, when starting up the hydrogen-producing device, the fuel battery 15 generates power by receiving a supply of the hydrogen-containing gas stored in the hydrogen storage container 13 and supplies power to the reformer 12 from a power supply path 30. The reformer 12 starts up and hydrogen is produced.

Provided is a hydrogen gas aspirator which can be carried by a user and freely carried by the user, and which can be supplied with hydrogen gas by adjusting concentrations of the aspirator. The hydrogen gas aspirator for generating and aspirating hydrogen gas includes: a first hydrogen gas aspirator body having at least a hollow interior; a second hydrogen gas aspirator body having an aspirator hollow layer and an aspirator hollow layer connected to each other by a low pressure check valve; and a variable pressure control valve capable of adjusting and passing hydrogen gas concentrations between the first and second hydrogen gas aspirator bodies, wherein substances that hydrogen generate and react by contacting water and water for reaction can be placed on the aspirator hollow layer inside the second hydrogen gas aspirator body.