Process for processing coal with low degree of metamorphism
A processing technology and low-metamorphic technology, applied in the petroleum industry, solid fuels, fuels, etc., can solve the problems of large residual water content in low-metamorphic coal, difficult to store, complicated methods, etc., to reduce pollution, reduce emissions, The effect of calorific value increase
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Embodiment 1
[0030] The raw coal particles are sent to the dryer, and the drying conditions are controlled at 50 cubic meters of hot gas per 1 kg of coal, and the oxygen content in the oxygen-deficient hot gas is 6.0% of the volume to ensure that the temperature of the raw coal particles is controlled at about 210°C. The raw coal particles treated by the above drying process conditions are sent into the pyrolyzer, and the high-temperature oxygen-poor hot gas is passed into the pyrolyzer at a flow rate of 50 cubic meters per kilogram of coal to control the flow rate of the oxygen-poor hot gas entering the pyrolyzer. The temperature was 400°C and the oxygen content was 2.5% by volume. The process by-product gas precipitated from the pyrolyzer is dedusted by the cyclone dust collector, enters the condenser, and is cooled to 110°C. The calorific value of the obtained coal solid was 5100 kcal / kg.
Embodiment 2
[0032] The raw coal particles are sent to the dryer, and the drying conditions are controlled at 40 cubic meters of hot gas per 1 kg of coal, and the oxygen content in the oxygen-deficient hot gas is 4.5% of the volume to ensure that the temperature of the raw coal particles is controlled at about 230°C. The raw coal particles treated by the above drying process conditions are sent into the pyrolyzer, and the high-temperature oxygen-poor hot gas is passed into the pyrolyzer at a flow rate of 40 cubic meters per kilogram of coal to control the flow rate of the oxygen-poor hot gas entering the pyrolyzer. The temperature was 450°C and the oxygen content was 2.0% by volume. The process by-product gas precipitated from the pyrolyzer is dedusted by the cyclone dust collector, enters the condenser, and is cooled to 100°C. The calorific value of the obtained coal solid was 5550 kcal / kg.
Embodiment 3
[0034] The raw coal particles are sent to the dryer, and the drying conditions are controlled at 30 cubic meters of hot gas per 1 kg of coal, and the oxygen content in the oxygen-deficient hot gas is 4.0% of the volume to ensure that the temperature of the raw coal particles is controlled at about 230°C. The raw coal particles treated by the above drying process conditions are sent into the pyrolyzer, and the high-temperature oxygen-poor hot gas is passed into the pyrolyzer at a flow ratio of 1 kg of coal to 10 cubic meters, and the flow rate of the oxygen-poor hot gas entering the pyrolyzer is controlled. The temperature was 550°C and the oxygen content was 1.5% by volume. The process by-product gas precipitated from the pyrolyzer is dedusted by the cyclone dust collector, enters the condenser, and is cooled to 130°C. The calorific value of the obtained coal solid was 6550 kcal / kg.
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