A process for isolating .sup.17O from water and a process for concentrating .sup.17O by using the same are provided. The process for isolating .sup.17O from water includes: mixing .sup.17O-containing water with formaldehyde to prepare an aqueous formaldehyde solution; heating the aqueous formaldehyde solution to generate a vapor mixture containing water vapor and formaldehyde vapor; and obtaining .sup.17O-depleted water, residual formaldehyde, and a gas mixture containing hydrogen and .sup.17O-enriched carbon monoxide, through photodissociating the vapor mixture. An .sup.17O-enriched water production process includes: an operation of adding hydrogen to the gas mixture to induce a catalytic methanation reaction to synthesize methane (CH.sub.4) and .sup.17O-enriched water (H.sub.2.sup.17O) through methanation, the operation being carried out following the process for isolating .sup.17O from water.

A thermal inverter for generating from a parent compound a first fluid of first molecules (H.sub.2) with a first molecular weight and a second fluid of second molecules (O.sub.2) with a second molecular weight. The molecular weight of the first molecules is less than the molecular weight of the second molecules. In a reaction device the parent compound is decomposed into a mixture compound of the first and second molecules. The thermal inverter has a gas separator device having a mixture inlet at a bottom section for the mixture compound of the first and second molecules and first and second outlets at a top section. The first outlet providing substantially the first molecules and the second outlet providing substantially the second molecules. The gas separator device has guiding elements which guides the molecules from the mixture inlet towards the first and second outlets in a coiled path which is confined by a sidewall.

Systems, apparatuses, and methods for generating electric power via conversion of water to hydrogen and oxygen. According to an aspect, a method includes applying super-heated steam across a catalyst surface within a catalyst chamber to generate ionized steam plasma. The method further includes forming an anode and a cathode between molecules of the ionized steam plasma. The method also includes using the anode and the cathode to generate electricity.

Contemplated systems and methods for hydrogen production use a solar heliostat system as an energy source to produce hydrogen during daytime, and employ molten salt as an energy source to produce hydrogen during nighttime.

A method of carbon dioxide hydrogenation comprises introducing gaseous water to a positive electrode of an electrolysis cell comprising the positive electrode, a negative electrode, and a proton-conducting membrane between the positive electrode and the negative electrode. The proton-conducting membrane comprises an electrolyte material having an ionic conductivity greater than or equal to about 102 S/cm at one or more temperatures within a range of from about 150 C. to about 650 C. Carbon dioxide is introduced to the negative electrode of the electrolysis cell. A potential difference is applied between the positive electrode and the negative electrode of the electrolysis cell to generate hydrogen ions from the gaseous water that diffuse through the proton-conducting membrane and hydrogenate the carbon dioxide at the negative electrode. A carbon dioxide hydrogenation system is also described.

The present invention relates to a process for conducting endothermic gas phase or gas-solid reactions, wherein the endothermic reaction is conducted in a production phase in a first reactor zone, the production zone, which is at least partly filled with solid particles, where the solid particles are in the form of a fixed bed, of a moving bed and in sections/or in the form of a fluidized bed, and the product-containing gas stream is drawn off from the production zone in the region of the highest temperature level plus/minus 200 K and the product-containing gas stream is guided through a second reactor zone, the heat recycling zone, which at least partly comprises a fixed bed, where the heat from the product-containing gas stream is stored in the fixed bed, and, in the subsequent purge step, a purge gas is guided through the production zone and the heat recycling zone in the same flow direction, and, in a heating zone disposed between the production zone and the heat recycling zone, the heat required for the endothermic reaction is introduced into the product-containing gas stream and into the purge stream or into the purge stream, and then, in a regeneration phase, a gas is passed through the two reactor zones in the reverse flow direction and the production zone is heated up; the present invention further relates to a structured reactor comprising three zones, a production zone containing solid particles, a heating zone and a heat recycling zone containing a fixed bed, wherein the solid particles and the fixed bed consist of different materials.

A device and system for energy generation using plasma incineration and further, for producing electricity by hydrogen gas generation and combustion.

The invention relates to a device for splitting water into hydrogen and oxygen by thermolysis, that is, by decomposition at elevated temperature. This device comprises: a reactor (1) having a heating system (2), a first reactor outlet (3), a second reactor outlet (4), at least one water inlet (5) and at least one oxygen filter (6); at least one hydrogen filter (7); an oxygen extraction pump (8), a hydrogen extraction pump (9), at least one water injection pump (10); a hydrogen separation chamber (11) located outside the reactor (1) and containing the hydrogen filter(s) (7); a heat exchanger (15) comprising an inlet (31) and an outlet (13) for a first circuit and an inlet (17) and an outlet (19) for a second circuit. The particularity of such a device is that it comprises two further heat exchangers (16, 28) each comprising an inlet (14, 27) and an outlet (20, 29) for a first circuit and an inlet (22, 36) and an outlet (23, 34) for a second circuit and in that: the inlet (31) of the first circuit of a first heat exchanger (15) is connected to an external water inlet (12) via the water injection pump (10), the outlet (13) of the first circuit of the first heat exchanger (15) is connected to the inlet (14) of a first circuit of a second heat exchanger (16); the inlet (17) of the second circuit of the first heat exchanger (15) is connected to an outlet (18) of the hydrogen separation chamber (11), which is connected to the filter(s) (7) and the outlet (19) of the second circuit of the first heat exchanger (15) is a hydrogen outlet of the device. The invention also pertains to a process for splitting water into hydrogen using the above device.

A method for producing hydrogen by thermochemical splitting of water includes injecting one or more feed streams of water into a reaction chamber. The method further includes using heat from a subterranean heat source to carry out the thermochemical splitting of water to form hydrogen and oxygen in the reaction chamber. The formed products are subsequently removed from the reaction chamber.

A method for producing hydrogen by thermochemical splitting of water includes injecting one or more feed streams of water into a reaction chamber. The method further includes using a molten salt heated by a subterranean heat source to carry out the thermochemical splitting of water to form hydrogen and oxygen in the reaction chamber. The formed products are subsequently removed from the reaction chamber. Hydrogen formed in the reaction chamber may be used in a downstream process to generate hydrocarbons.