A tyre recycling method, in which tyres are placed in a container and heated, whilst the generated gas is discharged to a gas tank, characterised in that the recycling process is taking place in an installation containing three identical units: the first unit , the second unit , the third unit , wherein each of the units is located inside a separate container structure and includes a hearth , in which a rotary reactor with recycled tyres, a horizontal rectification column provided with at least three fraction tank sections and with a gas tank with filters are placed; once the recycled tyres and possibly rubber waste with a total mass of at least 1,000 kg are placed in tyre containers of rotary reactors and these are placed in hearts of each of the units , gas is fed from a cylinder to burners of the hearth located inside the first unit and the gas is ignited, wherein temperature inside the rotary reactor located inside the hearth of the first unit should increase over the course of 3 h with a constant temperature increase rate not higher than 90°C/h and reach a value in the range between 250°C and 270°C, for the next 1,5 h this temperature should increase at a constant rate not exceeding 90°C/h and reach a value in the range between 350°C and 380°C, the rotary reactor located in the hearth of the first unit is subsequently heated and maintained at a temperature between 350°C and 380°C until the flow sensor located inside the horizontal rectification column of the first unit no longer indicates that liquid fraction is flowing, next the gas valve , feeding gas from the cylinder is closed, the rotary reactor of the first unit , in which tyres have been rectified, is removed from hearth , and another rotary reactor loaded with tyres is then placed inside this hearth of the first unit ; 3 h after the process was initiated in the hearth of the first unit , gas received from the first unit leaving burners of the hearth located in the second unit is ignited; 3 h after combustion is started in the hearth of the second unit gas received from the second unit leaving burners of the hearth located in the third unit is ignited, wherein temperature inside the rotary reactor located in the hearth of the respective unit (1 or 2) should increase over the course of 3 h after gas was ignited in this unit, with a constant temperature increase rate not exceeding 90°C/h and reach a value in the range of 250°C to 270°C, for the next 1,5 h this temperature should increase at a constant rate not exceeding 90°C/h and reach a value in the range of 350°C to 380°C, the rotary reactor located in the hearth of the corresponding unit (1 or 2) is then heated and maintained at a temperature between 350°C and 380°C until the flow sensor located in the horizontal rectification column of the corresponding unit (1 or 2) no longer indicates that liquid fraction is flowing, next the rotary reactor , in which tyres have been rectified, is removed and another rotary reactor loaded with tyres is placed into this hearth of the corresponding unit (1 lub 2), and tyre recycling is repeated in the corresponding units , wherein gas leaving burners of the hearth located in the corresponding unit (1, 2 or 3) is ignited using flame of previously delivered gas; wherein in the case of recycled tyres and possibly rubber waste with a mass of 1,000 kg placed in tyre containers of rotary reactors placed in hearths of each of the units , the rotary reactor in which tyres have been rectified is removed 7,5 h after combustion started in the hearth of the corresponding unit (1, 2 or 3) and another rotary reactor loaded with tyres is placed in the hearth of the corresponding unit (1, 2 or 3), wherein time intended for rotary reactor replacement is 0.5 h, which means that recycling of tyres placed in a rotary reactor of the corresponding unit (1, 2 or 3) begins every 8 h. <EOS>