A method for generating a gas-product includes: a) providing a first part of a feed stream; b) providing a second part of a feed stream; c) combining the first part of the feed stream with the second part of the feed stream into the feed stream; d) heating at least one of: the first part of the feed stream, the second part of the feed stream before step c, the feed stream after step c; e) conducting the feed stream into a reactor; f) reacting the feed stream into the gas-product. To reduce investment and in particular the footprint of the machine step d) is at least partly performed by compressing the respective stream by a supersonic compressor such that the respective stream is heated.

A method of producing hydrogen gas is provided. The method can include the steps of providing a reaction vessel containing aluminum, delivering a stream of natural gas to the reaction vessel, in which the natural gas includes methane, and heating the reaction vessel at a temperature in a range of 300 to 800° C., in which the heating causes a chemical reaction between the methane and the aluminum to provide hydrogen gas and aluminum carbide. The method can include delivering steam to the reaction vessel and heating the reaction vessel at a temperature in a range of 300 to 800° C., in which the heating causes a chemical reaction between the methane, steam, and the aluminum to provide hydrogen gas, aluminum carbide, and aluminum oxycarbide.

A power generation system that includes a membrane reformer assembly, wherein syngas is formed from a steam reforming reaction of natural gas and steam, and wherein hydrogen is separated from the syngas via a hydrogen-permeable membrane, a combustor for an oxy-combustion of a fuel, an expander to generate power, and an ion transport membrane assembly, wherein oxygen is separated from an oxygen-containing stream to be combusted in the combustor. Various embodiments of the power generation system and a process for generating power using the same are provided.

A hydrogen system includes: a compressor that applies a voltage between an anode and a cathode to move hydrogen in hydrogen-containing gas supplied to the anode to the cathode via an electrolyte membrane and compress the hydrogen; a first flow path through which hydrogen-containing gas discharged from the anode of the compressor flows; a second flow path to supply cathode off-gas to the anode of the compressor, the cathode off-gas being discharged from the cathode of the compressor; an on-off valve provided on the second flow path; and a controller that opens the on-off valve in a normal stop.

A system for controlling hydrogen production from water-reactive aluminum includes a regulator. For example, the regulator may include a plurality of discrete objects and a retainer. Each one of the discrete objects includes aluminum in an activated form reactable with water to produce hydrogen. The retainer may encase the plurality of discrete objects collectively in an elongate shape having an axial dimension greater than a radial dimension. Within the elongate shape, the plurality of discrete objects may define voids therebetween. The retainer may be permeable across its thickness such that water may enter the retainer to react with the activated form of aluminum of the discrete objects in a local concentration that promotes heat generation for rapid reaction while water about the retainer may globally cool the material in the retainer, with the combination promoting rapid and efficient reaction of aluminum to produce hydrogen.

The method for recycling carbon dioxide according to the present invention includes: injecting a reaction gas containing carbon dioxide and a carbon raw material into a rotary heating furnace; reacting the reaction gas and the carbon raw material with each other in the rotary heating furnace to generate a hydrocarbon precursor containing carbon monoxide; and converting the hydrocarbon precursor into a hydrocarbon compound, thereby exhibiting excellent conversion rate of carbon dioxide.

Systems and methods for the synthesis of ammonia includes a reformer; a carbon monoxide converter; a carbon dioxide scrubber unit with recovery; a methanation unit; and an ammonia synthesis unit; wherein the carbon dioxide scrubber unit with recovery is connected to at least one fired auxiliary steam boiler.

A method uses a chemical system to generate hydrogen gas. The chemistry involves a two-step reaction. In the first step, an alkaline hydride reacts with water to produce a hydroxide and hydrogen. In the second step, the hydroxide reacts with aluminum to produce even more hydrogen. The fuel is composed out of a mixture of powders of the alkaline hydride and aluminum. The fuel is encapsulated in a water soluble capsule for easy dispensing and protection against short time exposure to moisture. For large scale systems, the fuel is mixed with a low hydrophilicity ionic liquid to make it into a slurry that can be dispensed into a reaction chamber. The generation system comprises a tank, a pump, a first tube, a second tube, one or more capsules, a tank sensor assembly, and a processing system. The method comprises the steps of dispensing the capsules or the slurry in the tank; supplying water to the tank; and collecting hydrogen gas from the tank. After supplying water to the tank, the two reaction steps, being safe and controllable, facilitating hydrolysis reaction of metal and metal salts, are carried out. The produced hydrogen may be used in a fuel cell or a biomedical application.

A method for achieving a gas with a variable hydrogen to carbon monoxide ratio in a system including splitting a warm raw syngas stream into a first portion and a second portion, the second portioning having a portion flowrate. Sending the first portion of the warm raw syngas stream a carbon monoxide separator, thereby producing a first hydrogen enriched stream and a carbon monoxide rich stream. Sending the second portion of the warm raw syngas stream to a water/gas shift reactor, thereby producing a shifted syngas stream. Combining the first hydrogen enriched stream and the second hydrogen enriched stream and sending the combined stream to a hydrogen separator, thereby producing a product hydrogen stream having a hydrogen flowrate, and varying the hydrogen flowrate by increasing the portion flowrate.

A method for achieving a gas with a variable hydrogen to carbon monoxide ratio in a system including splitting a warm raw syngas stream into a first portion and a second portion, the second portioning having a portion flowrate. Sending the first portion of the warm raw syngas stream a carbon monoxide separator, thereby producing a first hydrogen enriched stream and a carbon monoxide rich stream. Sending the second portion of the warm raw syngas stream to a water/gas shift reactor, thereby producing a shifted syngas stream. Combining the first hydrogen enriched stream and the second hydrogen enriched stream and sending the combined stream to a hydrogen separator, thereby producing a product hydrogen stream having a hydrogen flowrate, and varying the hydrogen flowrate by increasing the portion flowrate.