The invention relates to a material and/or solid fuel which is produced from biomass. The material and/or fuel can be produced according to an apparatus and system for producing a fuel from a solid-liquid mixture of water and feed material with a carbon containing component, wherein the biomass forming the solid-liquid mixture is treated at a temperature of 160-300° C. at a pressure of at least 5 bar for a treatment duration of at least 2 hours and water formed by the chemical reaction is withdrawn from the reactor by a solid-liquid separation filtration device to increase a carbon fraction of the fuel.

The invention relates to a material and/or solid fuel which is produced from biomass. The material and/or fuel can be produced according to an apparatus and system for producing a fuel from a solid-liquid mixture of water and feed material with a carbon containing component, wherein the biomass forming the solid-liquid mixture is treated at a temperature of 160-300° C. at a pressure of at least 5 bar for a treatment duration of at least 2 hours and water formed by the chemical reaction is withdrawn from the reactor by a solid-liquid separation filtration device to increase a carbon fraction of the fuel.

A reactor for drying and torrefaction, configured for torrefying biomass, including a chamber in which two separate areas are delimited, a mechanism for mixing and transferring biomass from one end of the chamber to the other, a drying device in an upstream area of the chamber configured to dry the biomass introduced into the reactor, a torrefaction device in a downstream area of the chamber configured to torrefy biomass dried in the upstream area, and a transfer and sealing system configured to allow dried biomass to be transferred from the upstream area to the downstream area at time intervals, and to make the two areas mutually sealed during each interval. Such a reactor may, for example, find application to torrefaction of lignocellulosic biomass.

The method is for separation of lignin from original black liquor (BL.sub.IN) that has a first precipitation phase (PR1/PR2) for precipitation of lignin by a first acidification using acidifier, CO.sub.2, at alkaline conditions, then separating a lignin cake with subsequent suspension of the lignin cake in a strong acid in order to leach out metals from the lignin followed by dewatering and obtaining a clean lignin product LP. Lignin germ particles (LG) are added to the original black liquor in the first precipitation stage, preferably between two phases in said precipitation stage, in order to increase lignin particle growth on such lignin germ particles instead of spontaneous nucleation of lignin particles in said original black liquor. This results in improved filterability in subsequent dewatering and lignin cake formation and hence an increased lignin yield.

A modular system and method for producing urea from bio-mass includes means and steps for “homogenizing” a biomass feedstock stream having components with different bulk density BTU content into a stream having a consistent bulk density BTU content. The steps include cleaning the incoming bio-mass feedstock stream to remove non-organic matter, blending the cleaned bio-mass feedstock stream to obtain a homogeneous blend having a consistent bulk density BTU content, and milling the homogeneous blend bio-mass feedstock stream to a predetermined size no greater than 12 mm.

A modular system and method for producing urea from bio-mass includes means and steps for “homogenizing” a biomass feedstock stream having components with different bulk density BTU content into a stream having a consistent bulk density BTU content. The steps include cleaning the incoming bio-mass feedstock stream to remove non-organic matter, blending the cleaned bio-mass feedstock stream to obtain a homogeneous blend having a consistent bulk density BTU content, and milling the homogeneous blend bio-mass feedstock stream to a predetermined size no greater than 12 mm.

A biomass upgrading process comprises a steam-cracking step for producing a granulated combustible product, and, prior to the granulation step, a step of mixing an intermediate pulverulent product resulting from the steam-cracking of the biomass and a pulverulent material having a high lignin content.

A biomass upgrading process comprises a steam-cracking step for producing a granulated combustible product, and, prior to the granulation step, a step of mixing an intermediate pulverulent product resulting from the steam-cracking of the biomass and a pulverulent material having a high lignin content.

The present invention relates to a process for producing a solid biomass fuel, as well as a solid biomass fuel produced by said process. Additionally, the present invention relates to a combustion process comprising combusting said solid biomass fuel so as to produce energy.

The present invention relates to a process for producing a solid biomass fuel, as well as a solid biomass fuel produced by said process. Additionally, the present invention relates to a combustion process comprising combusting said solid biomass fuel so as to produce energy.