System and method for treating pulverized coal and biomass
A technology of biomass and biomass coke, which is applied to the gasification of biofuels, carbides, and granular/powdered fuels. Solve problems such as gas biomass coke, achieve the effect of improving heat utilization rate, reducing energy consumption and improving quality
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Embodiment 1
[0063] Utilizing the system of the present invention, the biomass whose length is less than 10 mm is sent into the non-heat carrier regenerative preheating furnace. Biomass is pyrolyzed in the preheating furnace to produce biomass coke and oil and gas products. The pyrolysis temperature is 600°C and the pyrolysis time is 50 minutes; the pyrolysis oil and gas are separated from oil and gas to obtain light tar and pyrolysis gas 1; light tar It is directly collected, purified and stored; the pyrolysis gas 1 is transported to the PSA absorber through a pipeline, and passes through a block of quicklime bed at 0.6Mpa to remove water and CO 2 , and pass through the solid filter bed for dust removal and purification to obtain pyrolysis gas 2; the pyrolysis gas 2 enters the hydrogenation gasifier through the nozzle, and is fully mixed with the coal powder sprayed into the coal powder nozzle, and is heated at 850°C and 2.0MPa The hydrogenation gasification reaction is carried out to obt...
Embodiment 2
[0065] This embodiment is the same as the system used in the above-mentioned embodiment 1, but the process conditions are different, as described below. The biomass with a length of less than 10mm is sent into the non-heat carrier regenerative preheating furnace. Biomass is pyrolyzed in the preheating furnace to produce biomass coke and oil and gas products. The pyrolysis temperature is 500°C and the pyrolysis time is 40 minutes; the pyrolysis oil and gas are separated from oil and gas to obtain light tar and pyrolysis gas 1; light tar It is directly collected, purified and stored; the pyrolysis gas 1 is transported to the PSA absorber through a pipeline, and passes through a block of quicklime bed at 1Mpa to remove water and CO 2 , and go through the solid filter bed for dust removal and purification to obtain pyrolysis gas 2; the pyrolysis gas 2 enters the hydrogenation gasifier through the nozzle, and is fully mixed with the coal powder injected by the coal powder nozzle, a...
Embodiment 3
[0067] This embodiment is the same as the system used in the above-mentioned embodiment 1, but the process conditions are different, as described below. The biomass with a length of less than 10mm is sent into the non-heat carrier regenerative preheating furnace. Biomass is pyrolyzed in the preheating furnace to produce biomass coke and oil and gas products. The pyrolysis temperature is 650°C and the pyrolysis time is 60 minutes; the pyrolysis oil and gas are separated from oil and gas to obtain light tar and pyrolysis gas 1; light tar It is directly collected, purified and stored; the pyrolysis gas 1 is transported to the PSA absorber through a pipeline, and passes through a block of quicklime bed at 0.4Mpa to remove water and CO 2 , and pass through the solid filter bed for dust removal and purification to obtain pyrolysis gas 2; the pyrolysis gas 2 enters the hydrogenation gasifier through the nozzle, and is fully mixed with the coal powder sprayed into the coal powder nozz...
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