Method for the production of granules comprising surface-reacted calcium carbonate

Patent metadata

Field	Value
Publication number	US-10351710-B2
Application number	US-201515308894-A
Country	US
Kind code	B2
Filing date	May 28, 2015
Priority date	May 30, 2014
Publication date	Jul 16, 2019
Grant date	Jul 16, 2019

Abstract

The present invention relates to a method for the production of granules comprising surface-reacted calcium carbonate by a) providing surface-reacted calcium carbonate, b) saturating the surface-reacted calcium carbonate with one or more liquids; c) providing one or more binder; d) combining the liquid saturated surface-reacted calcium carbonate with the one or more binder under agitation in an agitation device; e) removing the liquid from the mixture of step d); as well as to the granules comprising surface-reacted calcium carbonate obtained by this method.

First claim

The invention claimed is:

1. A method for producing granules comprising surface-reacted calcium carbonate, the method comprising the steps of:
a) providing surface-reacted calcium carbonate, wherein the surface-reacted calcium carbonate is a reaction product of natural ground or precipitated calcium carbonate with carbon dioxide and one or more acids, wherein the carbon dioxide is formed in situ by the acid treatment and/or is supplied from an external source;
b) saturating the surface-reacted calcium carbonate of step a) with one or more liquids in order to obtain a liquid saturated surface-reacted calcium carbonate that is not oversaturated;
c) providing one or more binders;
d) combining the liquid saturated surface-reacted calcium carbonate of step b) with the one or more binders of step c) under agitation in an agitation device to form granules comprising surface-reacted calcium carbonate; and
e) removing the liquid from the granules of step d).

2. The method according to claim 1 , wherein the surface-reacted calcium carbonate in step a) is a reaction product of natural ground calcium carbonate with carbon dioxide and one or more acids, wherein the carbon dioxide is formed in situ by the acid treatment and/or is supplied from an external source, and wherein the natural ground calcium carbonate comprises marble, chalk, dolomite, limestone or any mixture thereof.

3. The method according to claim 1 , wherein the surface-reacted calcium carbonate in step a) is a reaction product of precipitated calcium carbonate with carbon dioxide and one or more acids, wherein the carbon dioxide is formed in situ by the acid treatment and/or is supplied from an external source, and wherein the precipitated calcium carbonate comprises one or more aragonitic, vateritic and calcitic mineralogical crystal forms.

4. The method according to claim 1 , wherein the surface-reacted calcium carbonate has a specific surface area of from 1 m 2 /g to 200 m 2 /g, measured using nitrogen and the BET method according to ISO 9277.

5. The method according to claim 1 , wherein the surface-reacted calcium carbonate has a specific surface area of from 20 m 2 /g to 80 m 2 /g, measured using nitrogen and the BET method according to ISO 9277.

6. The method according to claim 1 , wherein the surface-reacted calcium carbonate has a volume median grain diameter d 50 of from 0.5 to 50 μm.

7. The method according to claim 1 , wherein the surface-reacted calcium carbonate has a volume median grain diameter d 50 of from 1 to 10 μm.

8. The method according to claim 1 , wherein the surface-reacted calcium carbonate has an intra-particle porosity within the range of from 5 vol. % (v/v) to 50 vol. % (v/v), calculated from a mercury porosimetry measurement.

9. The method according to claim 1 , wherein the surface-reacted calcium carbonate has an intra-particle porosity within the range of from 20 vol. % (v/v) to 50 vol. % (v/v), calculated from a mercury porosimetry measurement.

10. The method according to claim 1 , wherein the surface-reacted calcium carbonate has an intra-particle intruded specific pore volume within the range of 0.150 to 1.300 cm 3 /g, calculated from mercury porosimetry measurement.

11. The method according to claim 1 , wherein the surface-reacted calcium carbonate has an intra-particle intruded specific pore volume within the range of 0.178 to 1.244 cm 3 /g, calculated from mercury porosimetry measurement.

12. The method according to claim 1 , wherein in step b), the liquid is selected from the group consisting of water, methanol, ethanol, n-butanol, isopropanol, n-propanol, and any mixture thereof.

13. The method according to claim 1 , wherein in step b), the liquid is water.

14. The method according to claim 1 , wherein the one or more binders of step c) is selected from the group consisting of a synthetic polymer, methylcellulose, ethylcellulose, sodium carboxymethylcellulose, hydroxypropyl methylcellulose (HPMC), hydroxypropylcellulose (HPC), ethylhydroxyethylcellulose (EHEC), polyvinyl pyrrolidone (PVP), polyethylene glycol (PEG), a polyvinyl alcohol, apolymethacrylate, a natural binder, a plant gum, acacia, tragacanth, sandarac, ghatti, karaya, locust bean, guar, a protein, gelatin, casein, collagen, a saccharide, a polysaccharide, starch, a starch derivatives, inulin, cellulose, a pectin, a carrageenan, a sugar, an animal exudate, shellac, alginic acid, and any mixture thereof.

15. The method according to claim 1 , wherein the one or more binders of step c) is selected from the group consisting of sodium carboxymethylcellulose, hydroxypropyl methylcellulose (HPMC), polyvinyl pyrrolidone (PVP), pectin, and locus beam gum.

16. The method according to claim 1 , wherein the one or more binders of step c) is added in an amount of from 0.5 to 50 wt %, based on the weight of surface-reacted calcium carbonate of step a).

17. The method according to claim 1 , wherein the one or more binders of step c) is added in an amount of from 2.5 to 15 wt %, based on the weight of surface-reacted calcium carbonate of step a).

18. The method according to claim 1 , wherein the one or more binders of step c) is added in an amount of from 5 to 10 wt %, based on the weight of surface-reacted calcium carbonate of step a).

19. The method according to claim 1 , wherein in step d), the agitation device is selected from the group consisting of an Eirich mixer, a fluidized bed dryer/granulator, a plate granulator, a table granulator, a drum granulator, a disc granulator, a dish granulator, a plowshare mixer, a high speed blender, and a rapid mixer granulator.

20. The method according to claim 1 , wherein in step d), the one or more binders is added to the agitation device simultaneously with or after the liquid saturated surface-reacted calcium carbonate.

21. The method according to claim 1 , wherein after the combination of the liquid saturated surface-reacted calcium carbonate and the one or more binders in step d), further surface-reacted calcium carbonate or liquid saturated surface-reacted calcium carbonate or a mixture thereof, and/or liquid is added until an agglomeration of the particles is observed.

22. The method according to claim 21 , wherein the further surface-reacted calcium carbonate or liquid saturated surface-reacted calcium carbonate or mixture thereof is added in an amount of from 1 to 30 wt %, based on the weight of the surface-reacted calcium carbonate provided in step a).

23. The method according to claim 21 , wherein the further surface-reacted calcium carbonate or liquid saturated surface-reacted calcium carbonate or mixture thereof is added in an amount of from 5 to 15 wt %, based on the weight of the surface-reacted calcium carbonate provided in step a).

24. The method according to claim 1 , wherein in step e), the liquid is removed by separating the liquid from the granules.

25. The method according to claim 1 , wherein in step e), the liquid is removed by drying in a rotational oven, jet-drying, fluidized bed drying, freeze drying or flash drying.

26. The method according to claim 1 , wherein the granules obtained after step e) have a volume median particle size of from 0.1 to 6 mm, determined by sieve fractioning.

27. The method according to claim 1 , wherein the granules obtained after step e) have a volume median particle size of from 0.2 to 2 mm, determined by sieve fractioning.

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Assignees

• Omya Int Ag

Inventors

• Gerard Daniel E
• Schoelkopf Joachim
• Gane Patrick A C

Classifications

• C01P2006/90

  Other properties not specified above · CPC title

• C09C3/10

  Treatment with macromolecular organic compounds {(C09C3/006 takes precedence)} · CPC title

• C01P2006/12

  Surface area · CPC title

• C09C3/045

  Agglomeration, granulation, pelleting · CPC title

• C01P2006/16

  Pore diameter · CPC title