A method and system for collecting xenon (Xe) is described. A microchannel heat exchanger is used in combination with a mechanical cooler and an absorbent. A combination of components makes up a Xe Collection Subsystem that is adapted for use in an efficient process for collecting, purifying, and measuring Xe isotopes collected from air as part of the International Monitoring System.

A neon recovering/purifying system including: a recovery vessel that is arranged on an exhaust gas route and stores exhaust gas, the exhaust gas route being branched and extending from a discharge line; a compressor that increases a pressure of the exhaust gas sent out from the recovery vessel, to a third pressure; an exhaust gas flow rate regulating unit that regulates a flow rate of the exhaust gas whose pressure has been increased by the compressor; a first impurity removing unit that removes a first impurity from the exhaust gas; a second impurity removing unit that removes a second impurity from the exhaust gas from which the first impurity has been removed; a pressure increasing vessel that stores purified gas that has been processed by the first impurity removing unit and the second impurity removing unit; a pressure reducing valve that reduces a pressure of the purified gas sent out from the pressure increasing vessel, to the first pressure; and a purified gas flow rate regulating unit that regulates a flow rate of the purified gas supplied to a supply line of a manufacturing system.

A method and system for collecting xenon (Xe) is described. A microchannel heat exchanger is used in combination with a mechanical cooler and an absorbent. A combination of components makes up a Xe Collection Subsystem that is adapted for use in an efficient process for collecting, purifying, and measuring Xe isotopes collected from air as part of the International Monitoring System.

A method and system for collecting xenon (Xe) is described. A microchannel heat exchanger is used in combination with a mechanical cooler and an absorbent. A combination of components makes up a Xe Collection Subsystem that is adapted for use in an efficient process for collecting, purifying, and measuring Xe isotopes collected from air as part of the International Monitoring System.

A method and system for collecting xenon (Xe) is described. A microchannel heat exchanger is used in combination with a mechanical cooler and an absorbent. A combination of components makes up a Xe Collection Subsystem that is adapted for use in an efficient process for collecting, purifying, and measuring Xe isotopes collected from air as part of the International Monitoring System.

Disclosed are methods and systems for desulfurization of CO-rich streams. A method can include contacting a CO-rich gas stream with activated carbon and/or contacting the CO-rich gas stream with a zinc-oxide sorbent material at a temperature of ( ) to 50 C. to remove at least a portion of the sulfur-containing compounds present in the stream.

The present disclosure provides a methane reforming reaction system comprising: a reaction chamber (1), a hydrogen gas separation chamber (2) and a carbon dioxide separation chamber (3). The reaction chamber (1) is used for a methane reforming reaction between methane and steam; a hydrogen permeable membrane (4) is provided between the hydrogen gas separation chamber (2) and the reaction chamber (1) and a first outlet (6) is provided on the hydrogen gas separation chamber (2) for separating hydrogen gas produced in the reaction chamber (1); a carbon dioxide permeable membrane (5) is provided between the carbon dioxide separation chamber (3) and the reaction chamber (1) and a second outlet (7) is provided on the carbon dioxide separation chamber (3) for separating carbon dioxide produced in the reaction chamber (1); wherein the hydrogen gas in the hydrogen gas separation chamber (2) has a chemical potential less than that of the hydrogen gas in the reaction chamber (1) under a chemical equilibrium state of the methane reforming reaction; and the carbon dioxide in the carbon dioxide separation chamber (3) has a chemical potential less than that of the carbon dioxide in the reaction chamber (1) under the chemical equilibrium state of the methane reforming reaction.

Apparatus, system, and method for geothermally driven ammonia production. Hydrogen is generated using energy obtained from the underground magma reservoir and nitrogen is captured from air using the energy obtained from the underground magma reservoir. At least a portion of the generated hydrogen is combined with at least a portion of the generated nitrogen and heated at least to a reaction temperature using the energy obtained from the underground magma reservoir. The heated hydrogen contacts the heated nitrogen for a residence time to form the ammonia.

The present invention provides systems and methods for simultaneously producing a high-purity helium gas product, a methanol-water liquid mixture, and a methane-rich fuel product from a hydrogen-rich feedstock gas containing helium by treating the hydrogen-rich feedstock gas containing helium and carbon dioxide in a reverse water gas shift unit (1500) to produce carbon monoxide, which is then treated in a methanol production unit (300) and a methanol absorption unit (400) to produce a methanol-aqueous solution and a methanol-free gas. The methanol-free gas is then treated in a methane production unit (500) to produce methane, which is then treated in a carbon dioxide recovery membrane unit (1100) and a cryogenic nitrogen rejection unit (600) to produce the methanol-water liquid mixture, the methane-rich fuel product, and a helium-rich gas. The helium-rich gas is then treated to produce the high-purity helium gas product.

An apparatus for nitrogen generation for methanol powered maritime vehicles can include a compression system for compressing air and feeding compressed air to a separation unit for separation of nitrogen and oxygen from the compressed air. The nitrogen can be output from the separation unit for storage at an elevated pre-selected pressure suitable for feeding to a methanol engine of a maritime vehicle (e.g. a ship) for use in purging, leak testing, inerting, or other uses. Embodiments can be configured so there is no heat exchanger or booster compressor positioned between the separation unit and the nitrogen storage unit.