“…Moreover, slag refining can be performed on a large scale, which makes it more economic than many other process candidates, which are not as scalable. The potential of slags for B removal includes silicate slag compositions such as CaO-SiO 2 , [5][6][7][8][9][10] CaO-Ca F 2 -SiO 2 , [6,8,11,12] CaO-BaO-SiO 2 , [6] CaO-MgO-SiO 2 , [5,6,13] CaO-Al 2 O 3 -SiO 2 , [14] CaO-Na 2 O-SiO 2 , [14,15] Al 2 O 3 -CaOMgO-SiO 2 , [16] Al 2 O 3 -BaO-SiO 2 , [16] and Al 2 O 3 -CaO-MgOSiO 2 . [16] The thermodynamic equilibrium for B distribution between liquid silicon and molten slags has been most studied and the ratio of the concentrations of B in slag and silicon phases, the distribution coefficient denoted L B (L B ¼ pct B ð Þ wt pct B ½ ), has been determined.…”