Abstract: A device for processing a flow of particulate material by contact with a gas flow includes a housing defining a processing chamber. This chamber includes a gas distribution plate having openings. The gas distribution plate separates a lower gas plenum from a solid-gas contact zone. The contact zone has at least one cylindrical partition upstanding from the gas distribution plate dividing an inner section from an adjacent annular outer section. The at least one partition is provided with a transfer opening for the particulate material. The housing is also provided with an inlet for supplying particulate material to the inner section and an outlet for discharging processed particulate material from the annular outer section.

Abstract: A device for processing a flow of particulate material by contact with a gas flow includes a housing defining a processing chamber. This chamber includes a gas distribution plate having openings. The gas distribution plate separates a lower gas plenum from a solid-gas contact zone. The contact zone has at least one cylindrical partition upstanding from the gas distribution plate dividing an inner section from an adjacent annular outer section. The at least one partition is provided with a transfer opening for the particulate material. The housing is also provided with an inlet for supplying particulate material to the inner section and an outlet for discharging processed particulate material from the annular outer section.

Abstract: The present invention relates to a process for cooling hot torrefied biomass, which process comprises the steps of a) applying water onto the hot torrefied biomass, resulting in steam with entrained dust and organic volatiles, and cooled torrefied biomass comprising water; b) condensing the steam with entrained dust and organic volatiles to form a condensate comprising dust and organic volatiles; and c) recycling the condensate comprising dust and organic volatiles to step a). The invention also relates to a cooling device for cooling hot torrefied biomass enabling the cooling process according to the invention, and a system for producing torrefied biomass comprising such a cooling device.

Abstract: The present invention relates to a process for cooling hot torrefied biomass, which process comprises the steps of a) applying water onto the hot torrefied biomass, resulting in steam with entrained dust and organic volatiles, and cooled torrefied biomass comprising water; b) condensing the steam with entrained dust and organic volatiles to form a condensate comprising dust and organic volatiles; and c) recycling the condensate comprising dust and organic volatiles to step a). The invention also relates to a cooling device for cooling hot torrefied biomass enabling the cooling process according to the invention, and a system for producing torrefied biomass comprising such a cooling device.

Abstract: A treatment of biomass comprises supplying biomass which contains an amount of moisture to a first treatment device of a torrefaction system where the biomass is heated to a torrefaction temperature and substantially completely dried by evaporating the moisture to form a torrefied biomass. The at least partially torrefied biomass is removed from the first treatment device after a first time period and transferred to a second treatment device where it is kept for a longer second time period.

Abstract: A treatment of biomass comprises supplying biomass which contains an amount of moisture to a torrefaction system. The biomass containing moisture is heated to a torrefaction temperature in the torrefaction system. The biomass containing moisture is substantially completely dried by evaporating the moisture and the dried biomass torrefies at least partially to form torrefied biomass. The torrefaction system comprises a first treatment device and a second treatment device. The biomass is heated to the torrefaction temperature in the first treatment device within a first time period. The at least partially torrefied biomass is removed from the first treatment device after the first time period and the biomass which has been removed from the first treatment device is transferred to the second treatment device.

Abstract: A process for treating biomass comprises providing a material that contains an amount of residual moisture. The material is heated to a torrefying temperature in a low-oxygen atmosphere in a torrefaction reactor to convert it into a torrefied material. The material with the contained residual moisture is essentially fully dried in a drying chamber by evaporation of residual moisture. The torrefaction reactor comprises a torrefying chamber, in which the torrefaction of this dried material is essentially carried out. The material is conveyed through the torrefaction reactor. The drying of the material in the drying chamber is carried out by introducing into it a hot drying gas that flows therethrough cocurrently with the material. The torrefaction of the material in the torrefying chamber of the torrefaction reactor is carried out by introducing into it a hot torrefying gas that flows through the torrefying chamber countercurrently with the material.

Abstract: Method and device for cleaning synthesis gas obtained during gasification of biomass are disclosed. The synthesis gas is passed through a saturation device and an absorption device, both of which are fed with oil. In this way, the synthesis gas is scrubbed with oil and tar is substantially removed therefrom. The tar-containing oil which is released in this process is subjected to a cleaning step, as a result of which oil with a high percentage of tar and oil with a relatively low percentage of tar are formed. The first oil can be retuned to the gasification, and the remaining oil can be reused.

Abstract: A process for treating biomass comprises providing a material that contains an amount of residual moisture. The material is heated to a torrefying temperature in a low-oxygen atmosphere in a torrefaction reactor to convert it into a torrefied material. The material with the contained residual moisture is essentially fully dried in a drying chamber by evaporation of residual moisture. The torrefaction reactor comprises a torrefying chamber, in which the torrefaction of this dried material is essentially carried out. The material is conveyed through the torrefaction reactor. The drying of the material in the drying chamber is carried out by introducing into it a hot drying gas that flows therethrough cocurrently with the material. The torrefaction of the material in the torrefying chamber of the torrefaction reactor is carried out by introducing into it a hot torrefying gas that flows through the torrefying chamber countercurrently with the material.