FIELD: oil and gas production.
SUBSTANCE: initial biomass with humidity of 15÷25% is supplied to first device 2 where it is heated up to temperature of 350÷450°C. Then coal residue is supplied from first device 2 to second device 3, where it is heated up to temperature of 850÷1000°C and then it is supplied from it to third device 4. Steam-gas is supplied from first device 2 to third device 4, where they are filtered through coal residue, and after that, they are supplied to cooler-condenser 7. Steam-gases are supplied from second device 3 to cooler 6, where they are cooled to 350÷400°C, after that they are supplied to cooler-condenser 7.
EFFECT: decreasing power consumption of the process and reducing hydrocarbon fuel being used, possibility of supplying high-caloric gaseous fuel to distant consumers.
1 dwg
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