Method for production and preparation of rapid pyrolysis products from biomass, comprising a granulate-type long-term stable pyrolysis condensate-pyrolysis coke mixture, not generating dust and not self-igniting, in a pyrolysis plant, and subsequent gasification in an entrained-phase pressure gasification method, comprising the following steps: a) heating the biomass in the absence of oxygen in a pyrolysis reactor of a pyrolysis plant, wherein for up to 50 seconds a temperature of between 400 and 600 °C is imposed, and the biomass reacts to form porous pyrolysis coke, pyrolysis condensate, and pyrolysis gas, b) removal of the pyrolysis gas, and c) condensing of vaporous constituent parts of the pyrolysis condensate in several condensation stages, wherein d) in the first condensation stage, at temperatures above the dew point of water a bituminous tar is condensed out of the pyrolysis vapours, e) in at least one following condensation stage, an aqueous solution designated as bituminous water, consisting of organic compounds containing oxygen, is condensed and separated out at temperatures between 0 and the dew point of water, characterised in that f) a separation of pyrolysis coke from the vaporous constituents of the pyrolysis condensate takes place before the condensation stage, g) a mixing of bituminous tar and/or organic constituents into the pyrolysis coke takes place with the formation of the granulate-type long-term stable pyrolysis condensate-pyrolysis coke mixture, not generating dust and not self-igniting, takes place before the pyrolysis coke is screened out of the pyrolysis plant, h) a separated onward conveying of the granulate-type long-term stable pyrolysis condensate-pyrolysis coke mixture, not generating dust and not self-igniting, on the one hand, and of fluid condensate constituents on the other, takes place, as mixed-flow raw products, to a mixing Method, i) a mixing of mixed-flow raw products takes place to form a continuous homogeneous mixed flow, and j) gasification of the mixed flow in an entrained-phase pressure gasification system. a) heating the biomass in the absence of oxygen in a pyrolysis reactor of a pyrolysis plant, wherein for up to 50 seconds a temperature of between 400 and 600 °C is imposed, and the biomass reacts to form porous pyrolysis coke, pyrolysis condensate, and pyrolysis gas, b) removal of the pyrolysis gas, and c) condensing of vaporous constituent parts of the pyrolysis condensate in several condensation stages, wherein d) in the first condensation stage, at temperatures above the dew point of water a bituminous tar is condensed out of the pyrolysis vapours, e) in at least one following condensation stage, an aqueous solution designated as bituminous water, consisting of organic compounds containing oxygen, is condensed and separated out at temperatures between 0 and the dew point of water, characterised in that f) a separation of pyrolysis coke from the vaporous constituents of the pyrolysis condensate takes place before the condensation stage, g) a mixing of bituminous tar and/or organic constituents into the pyrolysis coke takes place with the formation of the granulate-type long-term stable pyrolysis condensate-pyrolysis coke mixture, not generating dust and not self-igniting, takes place before the pyrolysis coke is screened out of the pyrolysis plant, h) a separated onward conveying of the granulate-type long-term stable pyrolysis condensate-pyrolysis coke mixture, not generating dust and not self-igniting, on the one hand, and of fluid condensate constituents on the other, takes place, as mixed-flow raw products, to a mixing Method, i) a mixing of mixed-flow raw products takes place to form a continuous homogeneous mixed flow, and j) gasification of the mixed flow in an entrained-phase pressure gasification system.