Claims
- 1. A method of crystallization of sodium carbonate decahydrate crystals from an aqueous solution containing sodium carbonate and sodium bicarbonate comprising conducting said crystallization under conditions which maintain said solution in a supersaturated condition with respect to dissolved sodium bicarbonate.
- 2. The method of claim 1, wherein said crystallization is conducted under dynamic conditions.
- 3. The method of claim 2, wherein crystallization is conducted under substantially continuous steady-state conditions.
- 4. The method of claim 1, wherein the solution is maintained at a degree of supersaturation wherein substantially no crystals of sodium bicarbonate crystallize with the crystals of sodium carbonate decahydrate.
- 5. The method of claim 1, wherein the solution is maintained at a degree of supersaturation wherein a controlled amount of crystals of sodium bicarbonate will crystallize with the crystals of sodium carbonate decahydrate.
- 6. The method of claim 4 or claim 5, wherein the residence times of the solution containing sodium carbonate and sodium bicarbonate in which the sodium bicarbonate is in a supersaturated condition is controlled within a crystallization zone to exclude or control the quantity of sodium bicarbonate crystals which crystallize with the crystals of sodium carbonate decahydrate.
- 7. The method of claim 1, wherein the solution is cooled to cause crystallization of sodium carbonate decahydrate crystals.
- 8. The method of claim 1, wherein water is evaporated from the solution to cause crystallization of sodium carbonate decahydrate crystals.
- 9. The method of claim 1, wherein said solution is formed by dissolving an ore containing sodium bicarbonate in an aqueous media.
- 10. The method of claim 9, wherein said ore is dissolved in situ by a solution mining process.
- 11. The method of claim 1, wherein said sodium carbonate decahydrate crystals contain essentially no sodium sesquicarbonate crystals.
- 12. The method of claim 1, wherein the crystallization of sodium carbonate decahydrate crystals is conducted under supersaturation conditions of from up to about 20 degrees Celsius of supersaturation.
- 13. The method of claim 1, wherein sodium bicarbonate content of the solution is above the solid line connecting points C-D in FIG. 1.
- 14. The method of claim 1, wherein the sodium carbonate content of the solution is up to about 29 percent.
- 15. In a method of producing sodium carbonate decahydrate crystals from an aqueous solution of sodium carbonate and sodium bicarbonate in a cooling-type decahydrate crystallizer, the improvement comprising maintaining the solution in a supersaturated condition with respect to sodium bicarbonate.
- 16. The method of claim 15, wherein the residence time of the solution is controlled within certain preselected times to produce essentially pure sodium carbonate decahydrate crystals containing essentially no sodium bicarbonate or sodium sesquicarbonate crystals.
- 17. The method of claim 15, wherein the decahydrate crystallizer is operated substantially continuously under dynamic, steady-state conditions.
- 18. The method of claim 15, wherein the solution is maintained at a preselected degree of supersaturation to avoid co-crystallization of sodium sesquicarbonate.
- 19. The method of claim 15, wherein the solution contains up to about 28 percent sodium carbonate.
- 20. In a method of producing sodium carbonate decahydrate crystals from an aqueous solution of sodium carbonate and sodium bicarbonate in an evaporative-type decahydrate crystallizer, the improvement comprising maintaining the solution in a supersaturated condition with respect to dissolved sodium bicarbonate.
CROSS-REFERENCE TO RELATED APPLICATION
[0001] Pursuant to the provisions of 35 U.S.C. 119(e), this application claims the benefit of the filing date of U.S. provisional patent application Ser. No. 60/332,032, filed Nov. 21, 2001, for “CRYSTALLIZATION OF SODIUM CARBONATE DECAHYDRATE FROM LIQUORS SUPERSATURATED IN SODIUM BICARBONATE.”
Provisional Applications (1)
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Number |
Date |
Country |
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60332032 |
Nov 2001 |
US |