METHOD OF RECEIVING OF HYDROCARBON FUEL, TECHNOLOGICAL HYDROGEN AND CARBON-BASE MATERIALS FROM BIOMASS Russian patent published in 2009 - IPC C10B49/10 C10G1/02 C09C1/60 C01B3/24 C10B53/02 

FIELD: metallurgy.

SUBSTANCE: received according to suggested invention carbon-base materials can be used in treatment processes of gas and liwuids in the capacity of sorbate. Method of receiving of hydrocarbon fuel, technological hydrogen and carbon-base materials from granulated biomass, in which initial biomass is fed into drying apparatus, and from it dewatered biomass is fed into the pre-saturator, where hard material is heated up to 250-400°C, from it-into the saturator, where hard material is heated up to 600-700°C, from saturator into activator, coal residue from the latter with the temperature 850-900°C is directed into carbonisation reactor of carbon residue with external heating for receiving of pyrocarbon and hydrogen, and gases from the saturator is fed successively into the dust collecting system and condenser of high molecular hydrocarbon, from the latter gases containing noncondensing combustive componentry are fed into fire chambers of pre-saturator and/or activating agent and outer consumers, and part or all liquid high molecular carbohydrates from the condenser are fed into evaporator, differs by that part of hard metal from the saturator and/or activating agent is possibly taken away from the system and delivered to outer consumers, and into reactor of carbonisation it is fed part or all porous material from activating agent and froming in evaporator vapor of liquid high molecular hydrocarbon, herewith heating of carbonisation reactor is implemented ensured by burning of nondensables part in heating system fire chamber, from which combustion materials are fed into dryer mixer, herewith vapor of liquid high molecular hydrocarbons are fed into carbonisation reactor with excessive pressure, and withdrawing from the carbonisation reactor technological hydrogen is taken out from the system by autonomous route with regulated aerodynamic resistance, herewith part of gases from the dryer or activator are fed into recycle, and from the pre-saturator all or part of gases are fed into fire chamber of heating system of carbonisation reactor and/or to recycle, herewith thermal processing in dryer, pre-saturator, saturator and activator are implemented in instruments of local fluidised layer with inclined without disastrous grating, and carbonisation process is implemented into gravitational moving compact or fluidised layer.

EFFECT: diversification of receiving of final desired products at failure or reduction in use of non-renewable sources of hydrocarbon raw materials.

2 ex, 1 dwg