TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Process: The process takes place without or with incomplete separation, preferably with complete separation of the pyrolysis coke of the pyrolysis condensate before the first condensation step and interference of smoldering tar and/or organic components into the pyrolysis coke during the first condensation step, where the smoldering tar and/or the organic components absorbed in the porous pyrolysis coke are not separated. The smoldering tar and/or the organic components in the porous pyrolysis coke are separated before the removal of the pyrolysis coke from the pyrolysis plant. The process further comprises: transferring separately the condensate containing the pyrolysis coke and a liquid ingredients as mixer current intermediate product to a mixture; mixing a mixer current intermediate product to a continuous homogeneous mixer current and gasification of the mixer current in air current-pressure carburetor. The transformation process takes place in a closed container or silo to the intermediate or carrier. The transformation process takes place without filling of the components in container or silo. The intermixing a pre-inter mixture by introducing of smoldering water in a container or silo to transformation of the pyrolysis coke upstream. The air current high-pressure gasification of the mixture in a central mixing apparatus takes place temporally or directly. Heating of the mixture current intermediate product takes place at pre- or during- the premixing process. EXAMPLE - The condensed pyrolysis coke was removed by the continuous supply of the pyrolysis current, and the liquid condensate (containing 15-40% of organic smoldering tar and 60-85% of water condensate) was extracted in two-stage, where the viscosity of the smoldering tar was adjusted to the temperature of the first condensation step. Further organic tar was subsequently mixed with the dried pyrolysis coke to obtain a biomass (1000 kg) containing 260-530 kg of organic pyrolysis coke with a 28-57% of solid material and 370-640 kg of smoldering water, where the wet pyrolysis coke is in loosened condition up to 300 kg/m3 and compressed up to 500-900 kg/m3. Further gasification takes place by the interference of pyrolysis condensate to a mixture current. The pyrolysis coke with smoldering water was mixed with the organic smoldering tar, such that the movement of the slurry during gasification was avoided.