An integrated process for the production of a useful liquid hydrocarbon product comprises: feeding a gasification zone with an oxygen-containing feed and a first carbonaceous feedstock comprising waste materials and/or biomass, gasifying the first carbonaceous feedstock in the gasification zone to produce first synthesis gas, partially oxidising the first synthesis gas in a partial oxidation zone to generate partially oxidised synthesis gas, combining at least a portion of the first synthesis gas and/or the partially oxidised synthesis gas and at least a portion of electrolysis hydrogen obtained from an electrolyser in an amount to achieve the desired hydrogen to carbon monoxide molar ratio of from about 1.5:1 to about 2.5:1, and to generate a blended synthesis gas, wherein the electrolyser operates using green electricity; and subjecting at least a portion of the blended synthesis gas to a conversion process effective to produce the liquid hydrocarbon product.

An integrated process for the production of a useful liquid hydrocarbon product comprises: feeding a gasification zone with an oxygen-containing feed and a first carbonaceous feedstock comprising waste materials and/or biomass, gasifying the first carbonaceous feedstock in the gasification zone to produce first synthesis gas, partially oxidising the first synthesis gas in a partial oxidation zone to generate partially oxidised synthesis gas, combining at least a portion of the first synthesis gas and/or the partially oxidised synthesis gas and at least a portion of electrolysis hydrogen obtained from an electrolyser in an amount to achieve the desired hydrogen to carbon monoxide molar ratio of from about 1.5:1 to about 2.5:1, and to generate a blended synthesis gas, wherein the electrolyser operates using green electricity; and subjecting at least a portion of the blended synthesis gas to a conversion process effective to produce the liquid hydrocarbon product.

A method of continuously performing one or more heat-consuming processes, where at least one heat-consuming process is electrically heated. The maximum temperature in the reaction zone of the heat-consuming process is higher than 500° C., at least 70% of products of the heat-consuming process are continuously processed further downstream and/or fed to a local energy carrier network, and the electrical energy required for the heat-consuming process is drawn from an external power grid and from at least one local power source. The local power source is fed by at least one local energy carrier network and by products from the heat-consuming process. The local energy carrier network stores natural gas, naphtha, hydrogen, synthesis gas, and/or steam as energy carrier, and has a total capacity of at least 5 GWh. The local energy carrier network is fed with at least one further product and/or by-product from at least one further chemical process.

A method of continuously performing one or more heat-consuming processes, where at least one heat-consuming process is electrically heated. The maximum temperature in the reaction zone of the heat-consuming process is higher than 500° C., at least 70% of products of the heat-consuming process are continuously processed further downstream and/or fed to a local energy carrier network, and the electrical energy required for the heat-consuming process is drawn from an external power grid and from at least one local power source. The local power source is fed by at least one local energy carrier network and by products from the heat-consuming process. The local energy carrier network stores natural gas, naphtha, hydrogen, synthesis gas, and/or steam as energy carrier, and has a total capacity of at least 5 GWh. The local energy carrier network is fed with at least one further product and/or by-product from at least one further chemical process.

A method of using a feedstock gas reactor is described. A hydrocarbon, such as methane, is chemical decomposed in the feedstock gas reactor using heat of combustion generated from the combustion of a combustible gas. A mixed product stream is extracted from the feedstock gas reactor. The mixed product stream comprises hydrogen, carbon, and water. At least a portion of the one or more combustion product gases are vented from the combustion chamber. At least some of the carbon is activated using the vented one or more combustion product gases. At least some of the activated carbon is recycled to the feedstock gas reactor.

A method of using a feedstock gas reactor is described. A hydrocarbon, such as methane, is chemical decomposed in the feedstock gas reactor using heat of combustion generated from the combustion of a combustible gas. A mixed product stream is extracted from the feedstock gas reactor. The mixed product stream comprises hydrogen, carbon, and water. At least a portion of the one or more combustion product gases are vented from the combustion chamber. At least some of the carbon is activated using the vented one or more combustion product gases. At least some of the activated carbon is recycled to the feedstock gas reactor.

This invention provides for a self-sustaining fluidized bed reactor after the wave rotor reactor in which the reactor may be a fluidized bed reactor, a self-catalytic system, and may include an arrangement for the continuous removal and/or replenishment of particles in the fluidized bed, as well as possibly including a heater for heating the walls and/or a way for managing buildup of solids on the walls of the reactor.

Fixed point applications of producing hydrogen from hydrocarbons and using such are described. A feedstock including natural gas is introduced to a plasma reformer, and H2 is generated from the feedstock. The plasma reformer can be integrated into a number of locations for various purposes. For example, reformers can be integrated into buildings for onsite generation of H2 , either for storage, distribution as fuel, or for generating electricity for onsite needs to alleviate strain on the energy grid. Likewise, legacy natural gas distribution points or fuel stations can be converted to H2 distribution points, or further used as electricity distribution points by way of an H2 fuel cell. Likewise, reformers can be integrated into natural gas distribution networks to self-energize nodes or stations in the network via H2 fuel cells.

Producing hydrogen and carbon from hydrocarbons in a single-step process is described. A feedstock including natural gas or other light (e.g., <C5) hydrocarbons is introduced to a plasma reformer. The plasma reformer typically includes a non-thermal plasma. The plasma separates hydrogen from the carbon of the feedstock, yielding H2 and carbon black. The carbon is separated from the H2, and the H2 is further used as fuel (e.g., generating electricity via fuel cell) either contemporaneously or at a later time, stored, pressurized, or dispensed to a vehicle. Excess electricity generated form the H2 is stored in a battery, and excess is either stored or pressurized. Carbon black is further condensed to reduce volume for storage or transport.

Producing hydrogen and carbon from hydrocarbons in a single-step process is described. A feedstock including natural gas or other light (e.g., <C5) hydrocarbons is introduced to a plasma reformer. The plasma reformer typically includes a non-thermal plasma. The plasma separates hydrogen from the carbon of the feedstock, yielding H2 and carbon black. The carbon is separated from the H2, and the H2 is further used as fuel (e.g., generating electricity via fuel cell) either contemporaneously or at a later time, stored, pressurized, or dispensed to a vehicle. Excess electricity generated form the H2 is stored in a battery, and excess is either stored or pressurized. Carbon black is further condensed to reduce volume for storage or transport.