| 摘要 |
1,239,078. Silica; calcium fluoride. FARBENFABRIKEN BAYER A.G. 17 July, 1968 [12 Aug., 1967], No. 33972/68. Heading C1A. SiO 2 and CaF 2 are obtained by (a) reacting H 2 SiF 6 and/or Na 2 SiF 6 with CaCl 3 in a mole ratio of 1: 3 to 1: 2, in aqueous medium, at a CaCO 3 concentration of at least 100 g/l., and at a temperature of at least 50‹ C., (b) reacting the resulting mixture with an at least 10% NaOH solution in an amount of 1-3 moles NaOH per mole SiO 2 , and separating the CaF 2 precipitate, and (c) adding acid to the Na silicate solution from (b) at a temperature above 50‹ C. until the pH is 7-9 to precipitate SiO 2 . In step (a), a 10-40% solution of H 2 SiF 6 , or powdered Na 2 SiF 6 , may be added to a suspension of powdered calcite containing 100-300 g/1 CaCO 3 . In step (b), the mixture is preferably added to a 10-50% NaOH solution, and the CaF 2 may be flocculated with the aid of a polyamine, then washed, dried, and ground, and may be reacted with H 2 SO 4 to form CaSO 4 and HF. In step (c) the acid may be H 2 SiF 6 or H 2 SO 4 , optionally together with the CO 2 liberated in step (a), and the temperature may be 50-80‹ C. The mixture may then be maintained at at least 90‹ C. for 10-180 mins. The precipitated SiO 2 may be neutralized to pH 5-6À5 with H 2 SO 4 then washed, dried, and ground. It has a surface area of 50-200 m.<SP>2</SP>/g. The H 2 SiF 6 for step (a) may be obtained by hydrolysing SiF 4 with H 2 O or dilute H 2 SiF 6 , and the SiO 2 which is also formed may be dissolved in 5-15% NaOH solution at a SiO 2 / NaOH ratio of at least 1-0À5, then added to the solution from step (b). The Na 2 SiF 6 may be obtained from wet process H 3 PO 4 production. The dilute solution of NaF obtained from step (c) may be used to produce cryolite or reacted with lime to produce CaF 2 . |
