Method for the production of free flowing synthetic calcium fluoride and use thereof
The invention relates to a process for producing free-flowing calcium fluoride particles from a diluted aqueous solution of hydrogen fluoride comprising the step of reacting the diluted aqueous solution of hydrogen fluoride with calcium carbonate particles at a temperature of less than 50° C. The invention further relates to the use of the free-flowing calcium fluoride particles for the manufacturing of anhydrous hydrogen fluoride.
1. A process for producing free-flowing calcium fluoride particles from an aqueous solution of hydrogen fluoride comprising the step of reacting the aqueous solution of hydrogen fluoride with calcium carbonate particles at a temperature of less than 50° C., further wherein the aqueous solution of hydrogen fluoride has a concentration of hydrogen fluoride of from 0.5 to 40% and the calcium carbonate particles have a mean particle size (d 50 ) of from more than 30 to less than 50 μm.
2. The process of claim 1 , wherein the diluted aqueous solution of hydrogen fluoride has a concentration of hydrogen fluoride of from 1 to 30%.
3. The process of claim 1 , wherein the specific surface area (BET) of the calcium carbonate particles is ≦10 m 2 /g.
4. The process of claim 1 , wherein the diluted aqueous solution of hydrogen fluoride and the calcium carbonate particles are reacted for from 1 to 10 hours.
5. The process of claim 1 , wherein the reaction temperature is in the range of from 20° C. to less than 50° C.
6. The process of claim 1 , wherein the calcium fluoride content of the free-flowing calcium fluoride particles is at least 88%.
7. The process of claim 1 , wherein the content of calcium carbonate in the free-flowing calcium fluoride particles is 12% or less.
8. The process of claim 1 , wherein the mean particle size (d 50 ) of the free-flowing calcium fluoride particles is from more than 30 to less than 50 μm.
9. The process of claim 1 , wherein the specific surface area (BET) of the calcium fluoride particles is from 40 to 80 m 2 /g.
10. The process of claim 1 , further comprising a neutralization step for unreacted hydrofluoric acid.
11. The process of claim 1 , further comprising the step of adding calcium sulfate.
12. The process of claim 1 , wherein the step of reacting the diluted aqueous solution of hydrogen fluoride with calcium carbonate particles is a continuous flow process.
13. The process of claim 1 , wherein the step of reacting the diluted aqueous solution of hydrogen fluoride with calcium carbonate particles is a batch process.