초록 ▼

Apparatus for producing low cost, high purity solar grade Si wherein a reduction reaction, preferably the reduction of SiF4, by an alkali metal (Na preferred) is carried out by jetting a spray of reactants into a reaction chamber at a rate and temperature which causes the reaction to take place far

Apparatus for producing low cost, high purity solar grade Si wherein a reduction reaction, preferably the reduction of SiF4, by an alkali metal (Na preferred) is carried out by jetting a spray of reactants into a reaction chamber at a rate and temperature which causes the reaction to take place far enough away from the entry region to avoid plugging of reactants at the entry region and wherein separation in the melt is carried out continuously from the reaction and the Si can be cast directly from the melt. The melt separation is provided by openings in the reaction chamber wall between about 2 and 3.5 millimeters in width. The Si is retained within the reaction chamber due to its surface tension.

대표청구항 ▼

A reactor for producing low cost, high purity, solar grade silicon by reaction of gaseous silicon tetrafluoride with sodium in substantially stoichiometric quantities to produce a reaction product from which silicon is recovered and wherein the silicon tetrafluoride gas used in the reaction is obtai

A reactor for producing low cost, high purity, solar grade silicon by reaction of gaseous silicon tetrafluoride with sodium in substantially stoichiometric quantities to produce a reaction product from which silicon is recovered and wherein the silicon tetrafluoride gas used in the reaction is obtained by thermal decomposition of sodium fluosilicate, which is precipitated from aqueous fluosilicic acid generated from phosphate rock conversion to fertilizer, said reactor comprising a reaction chamber formed of graphite , a NaF collection and dispensing chamber substantially surrounding said reaction chamber, said dispensing chamber having an outlet for said NaF, said reaction chamber configured to receive a jet spray of sodium from at least one liquid sodium inlet and silicon tetrafluoride from a silicon tetrafluoride inlet, wherein said reaction takes place inside said reaction chamber, said reaction chamber comprises an open top, a cylindrical perforated wall portion, an imperforate bottom portion and an outlet located in said bottom portion; said wall portion having perforations in the walls thereof being of such size that essentially all NaF molten reaction product freely passes out through the perforations due to the surface tension of NaF compared to silicon and molten silicon is contained within said bottom portion of said reaction chamber and removed through said outlet by free flow said perforations in said wall portion are between about 2 and 3.5 millimeters in diameter.