FIELD: power engineering; shale-processing industry. SUBSTANCE: plant has shale pyrolysis unit with process furnace, exhaust-heat boiler connected to process furnace, steam-gas mixture cleaning and condensing system, storage tanks for semicoke gas and liquid fuel fractions, steam-turbine power unit connected to tank holding fractions with boiling temperature Tb= 350-450, gas-turbine unit connected to tank holding fractions with boiling temperatures Tb= 200-350 C and Tb< 200 C, additional gas-turbine unit connected to semicoke gas tank. Waste- gas outlets of gas-turbine units are connected to steam-turbine unit boiler. Shale is subjected to pyrolysis to produce steam-gas mixture and semicoke; the latter is burned and heat of stack gases is used to produce steam; steam-gas mixture is cleaned and condensed to form semicoke gas and liquid-fuel fractions. The latter are accumulated in respective tanks; fractions with Tb= 350-450°C C are burned in steam-turbine unit, those with Tb = 200-350 C and <200 C are burned in gas-turbine unit, and fraction with Tb higher than 450 C is returned to pyrolysis stage; semicoke gas is burned in additional gas-turbine unit. EFFECT: improved effectiveness of power generation and efficiency of power plant. 6 cl, 1 dwg
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Authors
Dates
2000-07-10—Published
1999-01-25—Filed