Method for external refining purification of industrial silicon
A technology for refining, purifying and industrial silicon, applied in chemical instruments and methods, silicon compounds, inorganic chemistry, etc., can solve the problems of small amount of silicon, difficult conversion of technology, high cost, low cost, improved kinetic conditions, and production efficiency. high effect
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Embodiment 1
[0026] (1) Continuously inject compressed air into the ladle first, then release the silicon melt with a purity of 98% in the submerged arc furnace into the ladle, and at the same time use plasma to touch the silicon water surface in the ladle above the ladle Heating is carried out and the silicon melt is stirred at the same time. The carrier gas of the plasma is a mixture of argon, hydrogen and water vapor, and the power is 60KW, and the temperature of the industrial silicon melt is kept at 1700°C;
[0027] (2) After the temperature rise in step (1), add refining agent SiO to the ladle 2 , CaO, CaF 2 , the mass ratio of the added refining agent to the silicon melt is 10:1, and the refining gas air and oxygen are introduced, the pressure of the refining gas is 1MPa, and the flow rate is 20m 3 / h, the ventilation time is 1h, blowing outside the furnace, slagging and refining;
[0028] (3) After the refining in step (2), the slag and silicon are separated, and then poured to o...
Embodiment 2
[0030] (1) Continuously inject compressed air into the ladle first, then release the silicon melt with a purity of 98% in the submerged arc furnace into the ladle, and at the same time use plasma to touch the silicon water surface in the ladle above the ladle Heating is carried out, and at the same time, the silicon melt is stirred. The carrier gas of the plasma is a mixture of argon and hydrogen, and the power is 60KW, and the temperature of the industrial silicon melt is kept at 1650°C;
[0031] (2) After the temperature rise in step (1), add refining agent SiO to the ladle 2 , CaO, Al 2 o 3 , CaF 2 , the mass ratio of the added refining agent to silicon melt is 20:1, and the refining gas, oxygen-enriched air, H 2 O, the pressure of the refined gas is 10MPa, and the flow rate is 10m 3 / h, the ventilation time is 10h, blowing outside the furnace, slagging and refining;
[0032] (3) After the refining in step (2), the slag and silicon are separated, and then poured to obt...
Embodiment 3
[0034] (1) Continuously inject compressed air into the ladle first, then release the silicon melt with a purity of 98% in the submerged arc furnace into the ladle, and at the same time use plasma to touch the silicon water surface in the ladle above the ladle Heating is carried out while stirring the silicon melt, where the carrier gas of the plasma is argon, the power is 60KW, and the temperature of the industrial silicon melt is kept at 1750°C;
[0035] (2) After the temperature rise in step (1), add refining agent LiF to the ladle. The mass ratio of the added refining agent to silicon melt is 1:20, and the refining gas N is introduced. 2 , the pressure of the refined gas is 20MPa, and the flow rate is 0.5m 3 / h, the ventilation time is 0.5h, blowing outside the furnace, slagging and refining;
[0036] (3) After the refining in step (2), the slag and silicon are separated, and then poured to obtain high-purity industrial silicon. The purity of industrial silicon reaches 3N...
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