IP Library Granted Patent US 9,278,858
Granted Patent B2
US 9,278,858 · App. 14/175,629 · Granted Mar 8, 2016

Micronized sulphur powder and method of production of same

Inventor: Satish Iyer (Calgary, CA)
Assignee: SULVARIS INC.
C01B17/10C01B17/0216C10L1/04C01P2004/61
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Quick Facts
Patent No.
US 9,278,858
App. No.
14/175,629
Granted
Mar 8, 2016
Kind
B2
Abstract

A process is provided for the production of a micronized sulphur powder product as well as a micronized sulphur cake intermediate. Production of the micronized sulphur powder using this process, which comprises preparation of a micronized sulphur emulsion from molten sulphur and a dispersant solution, from which the dispersant solution is subsequently removed, produces a product superior quality, and the method of production itself has enhanced safety and economic attributes.

Claims (31)

1. A method for the production of micronized sulphur particles, the method comprising:

(a) producing an emulsion of liquid sulphur in an aqueous dispersant solution above a melting point of sulphur, wherein dispersant is present at between about 1 and about 100 parts per thousand of the dispersant solution;

(b) cooling the sulphur emulsion to a temperature below the melting point of sulphur to solidify sulphur particles; and

(c) separating the dispersant solution from the sulphur particles to leave a sulphur particle cake, wherein the dispersant aids the separation of water from the sulphur particles.

2. The method of claim 1 wherein the dispersant agent comprises a naphthalene sulfonate compound, carboxymethyl cellulose, or a surfactant, or combination thereof.

3. The method of claim 1 wherein the dispersant comprises a naphthalene sulfonate compound and is present at 0.5% to 1.5% by weight.

4. The method of claim 1 wherein the dispersant solution is filtered or centrifuged from the emulsified sulphur suspension to leave the sulphur particle cake.

5. The method of claim 4 wherein the dispersant solution is removed by a filter press.

6. The method of claim 5 wherein the filter press uses a combination of mechanical pressure and air pressure to accelerate filtration.

7. The method of claim 1 wherein the separated dispersant solution is recycled back to step (a).

8. The method of claim 1 wherein the average sulphur particle size is less than about 100 microns.

9. The method of claim 8 , wherein the average sulphur particle size is less than about 30 microns.

10. A filter cake comprising sulphur particles filtered from a dispersed suspension of sulphur particles in water, where 95% of the particles are less than about 100 microns in size.

11. The filter cake of claim 10 , wherein 95% of the particles are less than about 30 microns in size.

12. The filter cake of claim 11 having a moisture content of less than about 12% by weight.

13. The filter cake of claim 12 having a moisture content of less than about 10% by weight.

14. A method for the production of micronized sulphur particles, the method comprising:

(a) producing an emulsion of liquid sulphur in an aqueous dispersant solution above a melting point of sulphur;

(b) cooling the sulphur emulsion to a temperature below the melting point of sulphur to solidify sulphur particles; and

(c) separating the dispersant solution from the sulphur particles to leave a sulphur particle cake having a moisture content of between about 7% and about 12% by weight after separation, wherein the dispersant aids the separation of water from the sulphur particles.

15. The method of claim 14 comprising the further steps of drying the sulphur particles, and mixing the sulphur particles with ingredients to form dispersible micronized sulphur pellets.

16. The method of claim 15 wherein the dried sulphur particles comprise residual dispersant.

17. The method of claim 14 wherein the dispersant agent comprises a naphthalene sulfonate compound, carboxymethyl cellulose, or a surfactant, or combination thereof.

18. The method of claim 14 wherein dispersant is present at between 1 and 100 parts per thousand of the dispersant solution.

19. The method of claim 18 wherein the dispersant comprises a naphthalene sulfonate compound and is present at 0.5% to 1.5% by weight.

20. The method of claim 14 wherein the dispersant solution is filtered or centrifuged from the emulsified sulphur suspension to leave the sulphur particle cake.

21. The method of claim 20 wherein the dispersant solution is removed by a filter press.

22. The method of claim 21 wherein the filter press uses a combination of mechanical pressure and air pressure to accelerate filtration.

23. The method of claim 14 wherein the separated dispersant solution is recycled back to step (a).

24. The method of claim 14 wherein the average sulphur particle size is less than about 100 microns.

25. The method of claim 24 wherein the average sulphur particle size is less than about 30 microns.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 2, 2015
From: IYER, SATISH
To: SULPHUR SOLUTIONS INC.
Reel/Frame 035319/0214 →
CHANGE OF NAME Recorded Apr 2, 2015
From: SULPHUR SOLUTIONS INC.
To: SULVARIS INC.
Reel/Frame 035355/0888 →
Priority Claims (1)
CA 2657531 · Mar 9, 2009 · national
Continuity (2)
Continuation In Part 13263879
Related Publication 20140193324A1 · Jul 10, 2014