Systems and methods for producing green hydrogen from a source material (e.g., biowaste) are contemplated. The source material is at least partially dehydrated to produce a dried intermediate and recovered water. The dried intermediate is pyrolyzed to produce syngas and a char. The recovered water is electrolyzed to produce oxygen and green hydrogen.

It is provided a method of converting a carbonaceous material into syngas at a carbon conversion rate of at least 78% comprising gasifying the carbonaceous material in a fluidized bed reactor producing a crude syngas, classifying the crude syngas by particle size and density into a cut sizing device, introducing the classified particle crude syngas into a thermal reformer and reforming the classified crude syngas at a temperature above mineral melting point, producing the syngas.

What is provided is a liquid fuel manufacturing method in which efficiency can be achieved throughout the entire system. A liquid fuel manufacturing method has a hydrogen stock quantity checking step of checking a hydrogen stock quantity, a gasifying step of producing synthesis gas from a biomass raw material, an electrolyzing step of producing hydrogen from water by means of electricity of renewable energy, and a liquid fuel manufacturing step of manufacturing liquid fuel with synthesis gas produced in the gasifying step and hydrogen produced in the electrolyzing step as raw materials. In the liquid fuel manufacturing step, the amount of supplied water vapor is decreased stepwise when an H.sub.2/CO ratio is not smaller than a target lower limit value, and then the hydrogen stock quantity checking step is carried out when the H.sub.2/CO ratio becomes equal to or smaller than the target lower limit value. The amount of supplied water vapor is reverted to an immediately preceding amount when there is no hydrogen stock. The amount of supplied water vapor is decreased stepwise until the amount of produced carbon monoxide stops increasing when there is hydrogen stock, and the amount of supplied water vapor is reverted to the immediately preceding amount, hydrogen is supplied such that the H.sub.2/CO ratio becomes equivalent to the lower limit for the target value, and the hydrogen stock quantity checking step is carried out when carbon monoxide stops increasing.

The invention relates to the unique operation of a partial oxidation (POx) system by enabling simultaneous injection of feeds with widely varying properties, including simultaneous injection of gas, liquid and solid feedstocks to the hot oxygen burner.

Systems and methods for producing green hydrogen from a source material (e.g., biowaste) are contemplated. The source material is at least partially dehydrated to produce a dried intermediate and recovered water. The dried intermediate is pyrolyzed to produce syngas and a char. The recovered water is electrolyzed to produce oxygen and green hydrogen.

The invention relates to a method for hydrothermal carbonisation of biomass containing organic matter, the method comprising: injecting the biomass, a heat transfer fluid and a reagent into a reactor (1), circulating a mixture consisting of the biomass, the heat transfer fluid and the reagent under specific pressure and temperature conditions for transforming the organic matter by hydrothermal carbonisation. The invention consists in: 1) determining the production rate of the emitted gas T.sub.e during the hydrothermal carbonisation reaction; 2) comparing the determined production rate of the emitted gas T.sub.e with a predefined value for the set gas production rate T.sub.c, and 3) adjusting at least one of the reaction control parameters chosen from among the temperature within the reactor (1), the quantity of injected reactant, and the residence time in the reactor in order to adjust the production rate of the emitted gas T.sub.e, such that the value of said production rate of the emitted gas Te tends to be equal to the value of the set gas production rate T.sub.c. The invention is applicable to treatment of biomass containing organic matter.

In a method for physical and thermochemical treatment of biomass, the biomass moisture content is reduced in a dryer and ammonia (NH.sub.3) is also released from the biomass during drying. The dried biomass is then either pyrolyzed in a pyrolysis reactor and the pyrolysis gas is forwarded to and combusted in a combustion device to form flue gas, or is combusted in a combustion facility unit to form flue gas. In either case the flue gas is fed to a mixer. Oxygen (O.sub.2) is metered to the flue gas in the mixer and is fed directly to the dryer as drying gas. As the drying gas passes through the dryer, the sulfur dioxide (SO.sub.2) contained in the drying gas and/or the sulfur trioxide (SO.sub.3) chemically reacts with the ammonia (NH.sub.3) to form ammonium sulfite ((NH.sub.4).sub.2SO.sub.3) and/or ammonium sulfate ((NH.sub.4).sub.2SO.sub.4). Also a treatment facility physically and thermochemically treats the biomass.

A system for using carbonaceous material includes a steam reformer, a hydrocarbon reformer, and at least one gas-cleanup system. Also described are methods of producing liquid fuel and/or chemicals from carbonaceous material.

Apparatus and associated methods relate to drying a wet coated seed material stream comprising an incoming wet granular biosolids stream mixed with a controlled size dried seed material recycling stream to produce a moist air and pellet stream, separating an uncontrolled size dried pellet stream from the moist air and pellet stream, diverting a recycle portion of the uncontrolled size dried pellet stream to be recycled, diverting the remainder of the uncontrolled size dried pellet stream to an outlet, resizing oversized pellets from the recycle portion of the uncontrolled size dried pellet stream to produce the controlled size dried seed material recycling stream, and mixing the controlled size dried seed material recycling stream with the incoming wet granular biosolids stream to produce the wet coated seed material stream. Oversized pellets may be selected using a screen. The oversized pellets may be resized using a crusher inline with the recycle stream.

The present invention relates to the processing of carbonaceous materials for, inter alia, hydrogen production. In particular, the invention relates to the production of hydrogen, for example, as input for industrial manufacturing applications or as a fuel source for the associated generation of electric power. In one form, the invention provides a method of producing hydrogen comprising the step of reacting a combination of solid carbonaceous material and a catalyst comprising alpha phase iron-based material adapted to produce an exothermic reaction with the solid carbonaceous material.