IP Library Granted Patent US 7,416,714
Granted Patent B2
US 7,416,714 · App. 11/391,028 · Granted Aug 26, 2008

Preparation of hydroxysodalite

Assignee: Unimin Corporation
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Quick Facts
Patent No.
US 7,416,714
App. No.
11/391,028
Granted
Aug 26, 2008
Kind
B2
Abstract

The invention is directed to a process and method for forming synthetic hydroxysodalite from nepheline and feldspar and/or nepheline syenite. A caustic material such as a solution of sodium hydroxide is combined with the nepheline and feldspar and/or nepheline syenite to form the synthetic hydroxysodalite.

Claims (38)

1. A method for forming synthetic hydroxysodalite from nepheline comprising the steps of:

a) providing a source of nepheline and feldspar;

b) providing a solution of caustic material;

c) combining together the source of nepheline and feldspar and solution caustic material to form a reaction mixture; and,

d) separating synthetic hydroxysodalite from said reaction mixture after a period of time.

2. The method as defined in claim 1 , wherein said source of nepheline and feldspar includes nepheline syenite.

3. The method as defined in claim 2 , wherein said source of nepheline and felspar includes at least about 90 weight percent nepheline syenite.

4. The method as defined in claim 2 , wherein said solution of caustic material includes sodium hydroxide.

5. The method as defined in claim 4 , wherein a weight ratio of solid caustic material to nepheline is at least about 2:1.

6. The method as defined in claim 5 , including the step of heating reaction mixture to a temperature of at least about 90° C.

7. The method as defined in claim 6 , wherein said period of time is at least about one hour.

8. The method as defined in claim 1 , wherein said solution of caustic material includes sodium hydroxide.

9. The method as defined in claim 8 , wherein said solution of caustic material includes at least about 40 weight percent sodium hydroxide.

10. The method as defined in claim 1 , wherein a weight ratio of solid caustic material to nepheline is at least about 2:1.

11. The method as defined in claim 10 , wherein a weight ratio of solid caustic material to nepheline is at least about 4:1.

12. The method as defined in claim 1 , including the step of heating reaction mixture to a temperature of at least about 90° C.

13. The method as defined in claim 12 , including the step of heating reaction mixture to a temperature of about 110-140° C.

14. The method as defined in claim 1 , wherein said period of time is at least about one hour.

15. The method as defined in claim 14 , wherein said period of time is at least about twelve hours.

16. The method as defined in claim 1 , wherein said step of separating synthetic hydroxysodalite from said reaction mixture includes a vacuum filtration process.

17. The method as defined in claim 1 , including the step of washing said synthetic hydroxysodalite after said separation step.

18. The method as defined in claim 17 , wherein said step of washing includes the application of deionized water on said synthetic hydroxysodalite.

19. The method as defined in claim 17 , including the step of drying said synthetic hydroxysodalite after said washing step.

20. The method as defined in claim 19 , wherein said step of drying includes the use of heated air.

21. The method as defined in claim 1 , including the step of classifying said synthetic hydroxysodalite to obtain a desired particle size distribution of said synthetic hydroxysodalite.

22. The method as defined in claim 1 , including the step of adding an aluminum source to said reaction mixture.

23. A method for forming synthetic hydroxysodalite from nepheline comprising the steps of:

a) providing a source of nepheline syenite having an average particle size of about 2-20 μm

b) providing a 40-60 weight percent solution of sodium hydroxide;

c) combining together the source of nepheline syenite and solution of sodium hydroxide to form a reaction mixture, a weight ratio of solid sodium hydroxide to nepheline syenite is 4-10:1;

d) heating said reaction mixture at about 100-130° C. for about 8-72 hours until a conversion percentage of nepheline syenite to synthetic hydroxysodalite of least about 60% is achieved;

e) separating said synthetic hydroxysodalite from said reaction mixture; and,

f) washing and drying said separated synthetic hydroxysodalite.

24. The method as defined in claim 23 , wherein said step of separating synthetic hydroxysodalite from said reaction mixture includes a vacuum filtration process.

25. The method as defined in claim 23 , wherein said step of washing includes the application of deionized water on said synthetic hydroxysodalite.

26. The method as defined in claim 23 , wherein said step of drying includes the use of heated air.

27. The method as defined in claim 23 , including the step of classifying said synthetic hydroxysodalite to obtain a desired particle size distribution of said synthetic hydroxysodalite.

28. The method as defined in claim 23 , including the step of adding aluminum hydroxide to said reaction mixture.

Assignments (2)
CHANGE OF NAME Recorded Aug 10, 2018
From: UNIMIN CORPORATION
To: COVIA HOLDINGS CORPORATION
Reel/Frame 046773/0160 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 28, 2006
From: KRAGTEN, DAVID D.
To: UNIMIN CORPORATION
Reel/Frame 017694/0678 →
Continuity (1)
Related Publication 20070237700A1 · Oct 11, 2007