Type of processed material | municipal solid waste |
Income material hymidity | Less than 50% |
Productivity on material processing | 278 (100 000) t/day (t/year) |
Number of pyrolysis units (reactors) | 9 (18) |
Operating mode | Cyclic-continuous |
Amount of produced liquid fuel fractions* | Up to 19 (7 000) t/day (t/year) |
Amount of produced pyrolysis gas* | Up to 76 000 (27 000 000) t/day (t/year) |
Amount of produced carbonaceous residue* | Up to 12 (4 000) t/day (t/year) |
Amount of waste waster* | Up to 75 (27 000) t/day (t/year) |
Sorting and preparation of waste of pyrolysis utilization.
Received waste is being unloaded at waste receiving area. Bulky objectsd are being selected from waste, than waste is being moved to the pit of loading conveyor. Waste sorting line is designed for selection of inorganic materials (earth, sand, stones, glass, metal), chlorine-containing components and useful fractions. “Tailings” of sorting are being crushed to a fraction not more than 150 mm and enter the accumulation hoppers, from which they are loads in reactors by conveyor lines.
Process of thermal waste processing is sequential-parallel operating of pyrolysis reactors (no less than 6). This process allows receiving fuel products in continuous mode. Due to sequential launch of reactors with intervals of 2-3 hours (single reactor loading time) and approximately the same duration of technological cycles, waste utilization facility produces combustible gas in continuous mode. Most of gas is being used for operating of reactor burners. Received liquid hydro-carbon fractions and carbonaceous recidue are being used as fuel for producing of steam in steam generators (steam boilers), mini CHP plants and generation of electrical power in a steam turbine power plant. The heat energy of the exhaust steam after the turbine is directed to the heat supply system of the facility.