A process for making recycle content ammonia by reacting hydrogen with nitrogen. At least a portion of the hydrogen is obtained directly or indirectly by molecular reforming a mixed plastic waste or pyrolysis product feedstock. The molecular reforming can be a steam reforming process or a partial oxidation process, such as a partial oxidation gasifier, to generate the syngas used as a source of hydrogen. The recycle content associated with the ammonia can be obtained from the mixed plastic waste, the recycle content in the pyrolysis product, such as pyoil or pygas, or the recycle content in the syngas or the purified hydrogen stream from the syngas.

A process and/or system for producing biomethane, hydrogen, or fuel, fuel intermediate, and/or chemical product from the biomethane or hydrogen. The biomethane and/or hydrogen is produced in a process that converts biomass to biomethane. In certain embodiments, the biomethane production process includes anaerobic digestion, which produces biogas and digestate. Carbon-containing material (e.g., derived from the biomass) is stored and/or used as part of at least one carbon capture and storage process, where the carbon-containing material includes (i) carbon dioxide produced from the biomethane production process (e.g., produced from anaerobic digestion), and (ii) carbon-containing material obtained or derived from residue of the biomethane production process, and optionally includes (iii) carbon dioxide produced from the hydrogen production process.

An improved hydrogen generation system and method for using the same are provided. The system includes an HDS unit configured to desulfurize hydrocarbons, a pre-reformer configured to convert heavy hydrocarbons within the process gas stream to methane, a reformer configured to produce a syngas stream and a flue gas, a PSA unit configured to produce a product hydrogen stream and a PSA off-gas stream, and means for cooling the flue gas against a combustion air and the PSA off-gas stream to a temperature below the dew point of sulfuric acid.

A fuel supply system includes a fuel reformer in contact with at least one of a combustion chamber or a wall of the combustion chamber. The fuel reformer includes a reformer chamber wall enclosing a fuel reformer chamber, and a reforming catalyst support sheet in the fuel reformer chamber.

A reforming unit for a fuel cell system is provided. The reforming unit may comprise a reforming section, a heat exchanging section and a bypass plenum. The reforming section reforms a hydrocarbon containing fuel. The heat exchanging section effects a heat transfer between a fluid flowing therethrough and the fluid flowing through the reforming section, the bypass plenum, or both. The bypass plenum provides a flowpath for the hydrocarbon-containing fuel to bypass the reforming section. The bypass plenum may comprise a flow restrictor in the outlet of the bypass plenum to control the amount of fluid communication between the outlet of the bypass plenum and the outlet of the reforming section.

A method of processing stranded remote gas comprising (a) introducing stranded remote gas and steam to a reforming unit to produce synthesis gas (syngas), wherein the stranded remote gas comprises methane, carbon dioxide, and sulfur-containing compounds, and wherein the syngas is characterized by a molar ratio of hydrogen to carbon monoxide of from about 1.7:1 to about 2.5:1; (b) introducing at least a portion of the syngas to a Fischer-Tropsch (FT) unit to produce an FT syncrude product, FT water, and FT tail gas, wherein the FT syncrude product comprises FT hydrocarbon liquids, wherein the FT syncrude product comprises FT wax in an amount of less than about 5 wt. %, and wherein the FT unit is characterized by an FT reaction temperature of from about 300 C. to about 350 C.; and (c) blending the FT syncrude product with crude oil for storage and/or transport.

A solar thermochemical processing system is disclosed. The system includes a first unit operation for receiving concentrated solar energy. Heat from the solar energy is used to drive the first unit operation. The first unit operation also receives a first set of reactants and produces a first set of products. A second unit operation receives the first set of products from the first unit operation and produces a second set of products. A third unit operation receives heat from the second unit operation to produce a portion of the first set of reactants.

The reactor has a heat exchanging body which includes therein a heat medium flow channel in which heat medium fluid is caused to flow, a reaction flow channel in which a reaction fluid containing a first reactant (and a second reactant) is caused to flow, and a supplement channel for supplying a second reactant at an intermediate portion of the reaction flow channel. A catalyst is provided in the reaction flow channel and promotes the reaction in the reaction fluid. The heat exchanging body has a plurality of holes through which the supplement channel communicates with the reaction flow channel. Steam reforming can be performed using water vapor and hydrocarbon as the first and second reactants.

A method of producing synthesis gas includes directing a first flow of hot synthesis gas through a first conduit, and directing a second flow of feed gas through at least one second conduit. The second conduit contains a reforming catalyst. The feed gas includes a mixture of steam and a hydrocarbon gas. The second conduit has an outer surface in contact with the hot synthesis gas. Heat from the hot synthesis gas is transferred across the second conduit to the feed gas thereby heating the feed gas and cooling the hot synthesis gas. The heated feed gas contacts the reforming catalyst and undergoes a reforming reaction that produces a third flow of synthesis gas.

Hydrogen production systems and methods of producing the same are provided. In an exemplary embodiment, a hydrogen production system comprises a reformer reactor that comprises a reformer reactor wall. A plurality of reformer tubes are interconnected to define a reformer lattice that has a reformer inner flow path and a reformer outer flow path. The plurality of reformer tubes are within the reformer reactor and connected to the reformer reactor wall at a plurality of discrete locations. The reformer lattice defines a combustor side that is one of the reformer inner or outer flow paths, and a reformer side that is the other of the reformer inner or outer flow paths. A reformer catalyst is positioned within the reformer side.