Method for removing impurity B in metallurgical silicon through wet process
A technology for metallurgical grade silicon and wet removal, applied in the field of metallurgy, can solve the problems of high cost, difficult operation, strong corrosion of equipment, etc., and achieve the effects of low cost, easy operation and improved product recovery rate.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0023] (1) Crushing and finely grinding metallurgical grade silicon into -100 mesh silicon powder, in which the B content is 25ppmw;
[0024] (2) Add the silicon powder in step (1) to the mixed aqueous solution composed of ammonium chloride, sodium fluoride and methanol according to the liquid-solid ratio of 2:1, wherein the mass fraction of ammonium chloride in the mixed aqueous solution is 5% , the mass fraction of sodium fluoride is 2%, the volume fraction of methanol is 5%, and then heated to 40°C for stirring and leaching for 0.5h;
[0025] (3) After the liquid-solid separation of the mixture in step (2) is carried out with a conventional filter press, the filter cake is washed twice with pure water to neutrality and then dried to obtain metallurgical-grade silicon without impurity B. The content of impurity B in the obtained high-purity silicon is 9.8 ppmw.
Embodiment 2
[0027] (1) Crushing and finely grinding metallurgical grade silicon into -300~-400 mesh silicon powder, of which the B content is 34ppmw;
[0028] (2) Add the silicon powder in step (1) to the mixed aqueous solution composed of ammonium chloride, sodium fluoride and methanol according to the liquid-solid ratio of 5:1, wherein the mass fraction of ammonium chloride in the mixed aqueous solution is 15% , the mass fraction of sodium fluoride is 10%, the volume fraction of methanol is 10%, and then heated to 70°C for stirring and leaching for 4h;
[0029] (3) After the mixture in step (2) is subjected to liquid-solid separation by conventional vacuum filtration, the filter cake is washed several times with distilled water until it becomes neutral, and then dried to obtain metallurgical-grade silicon without impurity B. The impurity B in the obtained high-purity silicon is 15 ppmw.
Embodiment 3
[0031] (1) Crushing and finely grinding metallurgical grade silicon into -600 mesh silicon powder;
[0032] (2) Add the silicon powder in step (1) to the mixed aqueous solution composed of ammonium chloride, sodium fluoride and methanol according to the liquid-solid ratio of 10:1, wherein the mass fraction of ammonium chloride in the mixed aqueous solution is 30% , the mass fraction of sodium fluoride is 20%, the volume fraction of methanol is 60%, and then heated to 100°C for stirring and leaching for 7h;
[0033] (3) After the mixture in step (2) is subjected to liquid-solid separation by conventional vacuum filtration, the filter cake is washed several times with deionized water until it becomes neutral, and then dried to obtain metallurgical-grade silicon without impurity B. The impurity B in the obtained high-purity silicon was 7.3 ppmw.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
