A kind of lignite semi-coke reducing agent for industrial silicon production and preparation method thereof
A technology of lignite semi-coke and reducing agent, applied in the field of metallurgy and chemical industry, can solve the problems of low reduction efficiency, uneven size, difficult processing, etc., and achieves reduction of electric furnace silicon smelting power consumption, increase of fixed carbon content, and obvious deashing effect. Effect
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Embodiment 1
[0024] Such as figure 1 Shown, the preparation method of lignite semi-coke reducing agent for industrial silicon production, the specific steps are:
[0025] (1) Firstly, lignite (fixed carbon 47.36wt%, ash 8.2wt%, volatile 44.44wt%) was naturally air-dried, and carbonized at 700°C for 1 hour to prepare lignite semi-coke (ash 14.43wt%, fixed carbon 74.09wt%, volatile matter 11.48wt%), the flue gas produced in this process is fractionated by a fractionating tower to obtain coal tar and gas, and the gas is returned to the lignite process;
[0026] (2) Finely grind and classify lignite semi-coke to obtain pulverized coal with a particle size of 200-300 mesh, accounting for 80%, add water to the pulverized coal to prepare a slurry with a concentration of 10% (90 parts of water to 10 parts of pulverized coal) , then add the dispersant Na 2 SiO 3 , the addition amount is 50g / m 3 pulp. Finally, according to the volume ratio of flocculant and pulp as 1:60, waste oil is added to c...
Embodiment 2
[0030] Such as figure 1 Shown, the preparation method of lignite semi-coke reducing agent for industrial silicon production, the specific steps are:
[0031](1) Firstly, lignite (fixed carbon 47.36wt%, ash 8.2wt%, volatile 44.44wt%) was naturally air-dried, then carbonized at 700°C for 2 hours to prepare lignite semi-coke (ash content 16.58wt%, volatile Divided into 9.4wt%, fixed carbon is 74.02wt%), the flue gas produced in this process is fractionated by the fractionating tower to obtain coal tar and gas, and the gas is returned to the lignite process;
[0032] (2) Finely grind and classify lignite semi-coke to obtain pulverized coal with a particle size of 200-300 mesh, accounting for 80%, add water to the pulverized coal to make a slurry with a concentration of 15% (85 parts of water to 15 parts of pulverized coal) , and add 60g of Na to each cubic pulp 2 SiO 3 As a dispersant, finally add waste oil according to the volume ratio of waste oil to coal water slurry of 1:75...
Embodiment 3
[0035] Such as figure 1 Shown, the preparation method of lignite semi-coke reducing agent for industrial silicon production, the specific steps are:
[0036] (1) Firstly, lignite (fixed carbon 47.36wt%, ash 8.2wt%, volatile 44.44wt%) was naturally air-dried, then carbonized at 800°C for 2 hours to prepare lignite semi-coke (ash content 20.73wt%, volatile Divided into 6.4wt%, fixed carbon is 72.87wt%), the flue gas produced in this process is fractionated by the fractionating tower to obtain coal tar and gas, and the gas returns to the lignite process;
[0037] (2) Finely grind and classify lignite semi-coke to obtain pulverized coal with a particle size of 200-300 meshes accounting for 80%, add water to the pulverized coal to make a slurry with a concentration of 20% (80 parts of water to 20 parts of pulverized coal) , and add 70g of dispersant Na to each cubic pulp 2 SiO 3 , and finally according to the volume ratio of waste oil and pulp of 1:75, add waste oil to carry out...
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