A process for the production of charcoal comprising the steps of: a) feeding biomass, in particular wood chips, into a pyrolysis unit, in which the wood chips are pyrolyzed into a full stream comprising solid, liquid and gaseous material, b) feeding the full stream and a gasifying agent into an oxidation unit, wherein the full stream is oxidized at least partially and transported pneumatically, c) feeding the partially oxidized full stream from the oxidation unit into a reduction unit arranged essentially vertically, the material outlet of the oxidation unit being connected to the reduction unit, with the cross-section of the reduction unit increasing as the distance from the material outlet of the oxidation unit increases, the flow rate of the full stream in the reduction unit being adapted to the material of the full stream and to the shape of the flow cross-section of the reduction unit in such a way that a stable fixed bed kept in suspension is formed in the reduction unit, d) removing the raw charcoal from the reduction unit via an overflow, e) separating gaseous components in a hot gas filter and collecting the charcoal, and f) quenching the collected charcoal with water.

A process for the production of charcoal comprising the steps of: a) feeding biomass, in particular wood chips, into a pyrolysis unit, in which the wood chips are pyrolyzed into a full stream comprising solid, liquid and gaseous material, b) feeding the full stream and a gasifying agent into an oxidation unit, wherein the full stream is oxidized at least partially and transported pneumatically, c) feeding the partially oxidized full stream from the oxidation unit into a reduction unit arranged essentially vertically, the material outlet of the oxidation unit being connected to the reduction unit, with the cross-section of the reduction unit increasing as the distance from the material outlet of the oxidation unit increases, the flow rate of the full stream in the reduction unit being adapted to the material of the full stream and to the shape of the flow cross-section of the reduction unit in such a way that a stable fixed bed kept in suspension is formed in the reduction unit, d) removing the raw charcoal from the reduction unit via an overflow, e) separating gaseous components in a hot gas filter and collecting the charcoal, and f) quenching the collected charcoal with water.

In some variations, the invention provides a biocarbon pellet comprising: 35 wt % to 99 wt % of a biogenic reagent, wherein the biogenic reagent comprises, on a dry basis, at least 60 wt % carbon; 0 wt % to 35 wt % water moisture; and 1 wt % to 30 wt % of a binder, wherein the biocarbon pellet is characterized by an adjustable Hardgrove Grindability Index (HGI) from about 30 to about 120, as shown in the Examples. The pellet HGI is adjustable by controlling process conditions and the pellet binder. The binder can be an organic binder or an inorganic binder. The carbon is renewable as determined from a measurement of the .sup.14C/.sup.12C isotopic ratio. Many processes of making and using the biocarbon pellets are described. Applications of the biocarbon pellets include pulverized coal boilers, furnaces for making metals such as iron or silicon, and gasifiers for producing reducing gas.

The presently disclosed subject matter relates to torrefied biomass briquettes and methods for producing the same that make use of a mixture of lightly torrefied material (LTM) and highly torrefied material (HTM) and/or make use of torrefied materials that are subjected to a hydrolysis pretreatment prior to being torrefied.

A flavor or aroma charcoal material, such as charcoal briquets, which is formulated to include a flavor or aroma component. The charcoal material may include a smoldering agent (e.g., limestone), wood particles (e.g., sawdust), a binder, and the flavor or aroma component (herbs and/or spices). The flavor or aroma charcoal material may not be configured as a fuel charcoal material, for example, it may be substantially void of char and/or coal. In an embodiment, the flavor or aroma charcoal material may be provided as part of a blend of different charcoal materials that includes both flavor or aroma briquets in combination with fuel briquets (e.g., which fuel briquets include char and/or coal, while the flavor briquets do not). The flavor briquets provide enhanced aroma and/or flavor to the grilling experience.

A flavor or aroma charcoal material, such as charcoal briquets, which is formulated to include a flavor or aroma component. The charcoal material may include a smoldering agent (e.g., limestone), wood particles (e.g., sawdust), a binder, and the flavor or aroma component (herbs and/or spices). The flavor or aroma charcoal material may not be configured as a fuel charcoal material, for example, it may be substantially void of char and/or coal. In an embodiment, the flavor or aroma charcoal material may be provided as part of a blend of different charcoal materials that includes both flavor or aroma briquets in combination with fuel briquets (e.g., which fuel briquets include char and/or coal, while the flavor briquets do not). The flavor briquets provide enhanced aroma and/or flavor to the grilling experience.

A method for manufacturing a coal additive that is added to coal as a solid fuel to microgranulate and uniformize the coal, thereby increasing the combustion area of the coal, leading to a decrease in combustion time and a reduction in unburned carbon generation. A raw material for the coal additive is prepared as a liquid phase by placing, in a container, a fermented liquid, which is an extract obtained from the incubation of fermenting bacteria (enzyme) in fruit residues, and an emulsion of metal ions and bentonite or gelrite, followed by mixing. Coal may be subjected to microgranulation and uniformization as a solid fuel by addition of the liquefied additive to the coal. The degree of coal powder is improved to increase combustion area, thereby shortening combustion time and reducing generation of unburned carbon, leading to increasing energy efficiency, which is environmentally friendly and safe and has remarkable effects.

A process of aggregating coal fines in a coal flotation concentrate includes dewatering the coal flotation concentrate to reduce moisture content and provide a dewatered flotation concentrate, mixing the dewatered flotation concentrate with a binder to provide a mixture, compacting the mixture under pressure to provide a green body of aggregated coal fines, having a sufficient strength for handling utilizing typical commercial methods of conveying and shipping.

A process of aggregating coal fines in a coal flotation concentrate includes dewatering the coal flotation concentrate to reduce moisture content and provide a dewatered flotation concentrate, mixing the dewatered flotation concentrate with a binder to provide a mixture, compacting the mixture under pressure to provide a green body of aggregated coal fines, having a sufficient strength for handling utilizing typical commercial methods of conveying and shipping.

The presently disclosed subject matter relates to torrefied biomass briquettes and methods for producing the same that make use of a mixture of lightly torrefied material (LTM) and highly torrefied material (HTM) and/or make use of torrefied materials that are subjected to a hydrolysis pretreatment prior to being torrefied.