of obtaining carbon-containing material from recyclable tires and / or rubber products, including: mechanical crushing of recycled tires and / or rubber products in a grinder and receiving the charge; feeding the charge to a reactor followed by pyrolysis with the formation of gaseous products and a solid residue; continuous removal of the gaseous products from the reactor with the subsequent condensation of liquid products in a condensation column of liquid fractions, discharge of solid residue from the reactor and its cooling; rough crushing of the solid residue in a crusher and removal of the metal in the magnetic separator, characterized in that before mechanical crushing, the metal bead rings are removed from recycled tires; before feeding the charge into the reactor, an inhibitor of coke formation is introduced into it, in an amount of 3-20% by weight of the charge, consisting of a solid component representing any combination of thermoplastic linear polymers from the group: polyethylene, polypropylene, polyethylene terephthalate, polystyrene, and a liquid component - polymethylsiloxane in an amount of 0.5 - 1.0% by weight of the inhibitor, the pyrolysis of the charge in the reactor is carried out at a temperature of 350 ° C in the main working area and to 600 ° C at the exit of the reactor; removal of metal from the crushed solid residue is performed until the metal content is not more than 0.1% of the total mass of the solid residue, then a treatment and an activation of the solid residue with superheated steam at a temperature of 250-350 ° C in the steam chamber are performed and the activated solid residue is crushed in a vortex mill; a two-stage classification of the solid residue is made at an air-through separator, from which the fine fraction is sent to further fine classification into an electro-mass classifier, and the large fraction is screened, sent to a bunker and then to a thermal furnace, where residual carbon is removed and an additional target product is obtained - a mineral component or re-grinding into a vortex mill, and the separation of the fine fraction of the solid residue is carried out in an electric mass classifier for fraction F1, less than 45 μm (F1 <45 μm) and fraction F2, more than 45 μm (F2> 45 μm); returning the solid residue powder of the F2 fraction to more than 45 μm (F2> 45 μm from the electrical mass classifier for repeated fine grinding in a vortex mill; the powder fraction F1 less than 45 μm (F1 <45 μm) from the electric mass classifier is sent to the storage bin. mechanical crushing of recycled tires and / or rubber products in a grinder and receiving the charge; feeding the charge to a reactor followed by pyrolysis with the formation of gaseous products and a solid residue; continuous removal of the gaseous products from the reactor with the subsequent condensation of liquid products in a condensation column of liquid fractions, discharge of solid residue from the reactor and its cooling; rough crushing of the solid residue in a crusher and removal of the metal in the magnetic separator, characterized in that before mechanical crushing, the metal bead rings are removed from recycled tires; before feeding the charge into the reactor, an inhibitor of coke formation is introduced into it, in an amount of 3-20% by weight of the charge, consisting of a solid component representing any combination of thermoplastic linear polymers from the group: polyethylene, polypropylene, polyethylene terephthalate, polystyrene, and a liquid component - polymethylsiloxane in an amount of 0.5 - 1.0% by weight of the inhibitor, the pyrolysis of the charge in the reactor is carried out at a temperature of 350 ° C in the main working area and to 600 ° C at the exit of the reactor; removal of metal from the crushed solid residue is performed until the metal content is not more than 0.1% of the total mass of the solid residue, then a treatment and an activation of the solid residue with superheated steam at a temperature of 250-350 ° C in the steam chamber are performed and the activated solid residue is crushed in a vortex mill; a two-stage classification of the solid residue is made at an air-through separator, from which the fine fraction is sent to further fine classification into an electro-mass classifier, and the large fraction is screened, sent to a bunker and then to a thermal furnace, where residual carbon is removed and an additional target product is obtained - a mineral component or re-grinding into a vortex mill, and the separation of the fine fraction of the solid residue is carried out in an electric mass classifier for fraction F1, less than 45 μm (F1 <45 μm) and fraction F2, more than 45 μm (F2> 45 μm); returning the solid residue powder of the F2 fraction to more than 45 μm (F2> 45 μm from the electrical mass classifier for repeated fine grinding in a vortex mill; the powder fraction F1 less than 45 μm (F1 <45 μm) from the electric mass classifier is sent to the storage bin.