IP Library Granted Patent US 9,580,605
Granted Patent B2
US 9,580,605 · App. 13/640,325 · Granted Feb 28, 2017

Process to prepare surface-modified mineral material, resulting products and uses thereof

Inventors: Guenter Wimmer (Meerbusch, DE); Joachim Schölkopf (Killwangen, CH); Hans-Joachim Weitzel (Suhr, CH)
Assignee: Omya International AG
C09C1/022C09C1/021C09C1/028C09C1/42C01P2004/61C01P2004/62C01P2006/12C01P2006/88
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Quick Facts
Patent No.
US 9,580,605
App. No.
13/640,325
Granted
Feb 28, 2017
Kind
B2
Abstract

The present invention refers to a process to modify at least part of the surface of at least one mineral material, and to the use, as an additive in an aqueous suspension of mineral materials having a pH between 5 and 10, of at least one agent, wherein the additive allows for the formation of a low volume, high solids content filter or centrifuge cake on dewatering the suspension.

Claims (44)

1. A process for manufacturing a surface-modified mineral material in which at least part of the surface of a mineral material is modified, the process comprising the following steps:

(a) preparing an aqueous suspension of mineral material having a solids content of from 10 to 80% by weight, based on the weight of the suspension, and at a pH of 5 to 10, wherein the mineral matter comprises calcium carbonate or talc;

(b) contacting the aqueous suspension of mineral matter of step (a) with at least one agent so that at least part of the surface of the mineral matter is modified;

(c) obtaining a suspension of the surface-modified mineral material from step (b) having a pH which is less than 10 and which is greater than 7 if the isoelectric point of the mineral material provided in step (a) is greater than 7, or a pH that is greater than the isoelectric point of the mineral material provided in step (a) if the isoelectric point is 7 or lower; and

(d) subjecting the suspension of the surface-modified mineral material from step (c) to one or more of: (i) filtration on a filtration medium to form a filter cake of surface-modified mineral material, (ii) centrifugation to form a centrifuge cake of surface-modified mineral material, (iii) concentration by thermal or mechanical methods to form a concentrated surface-modified mineral material, and (iv) drying to form a dried surface-modified mineral material;

wherein the agent is:

(i) in the form of an aqueous solution or a stable aqueous colloid having a pH of less than 6;

(ii) formed by mixing, in an aqueous environment, at least one phosphonic acid-comprising compound with one or more metal cations or metal-comprising cationic compounds, wherein the metal is selected from the group consisting of aluminium, zirconium, zinc, cobalt, chrome, iron, copper, tin, titanium and mixtures thereof, and wherein the phosphonic acid-comprising compound and the metal cations or metal-comprising cationic compounds are dosed such that the molar ratio of phosphonate hydroxyl groups: metal cation or metal comprising cationic compound is from 10:1 to 2:1; and

(iii) added in step (b) in an amount corresponding to from 0.04 to 1 mg by dry weight of agent per m 2 of the total surface of the mineral material.

2. The process according to claim 1 , wherein the suspension of step (a) has a pH of 7 to 10.

3. The process according to claim 1 , wherein the suspension of step (a) has a pH of 8 to 9.

4. The process according to claim 1 , wherein the mineral material is talc.

5. The process according to claim 1 , wherein the mineral material comprises calcium carbonate and dolomite.

6. The process according to claim 1 , wherein the mineral material comprises surface-reacted calcium carbonate.

7. The process according to claim 1 , wherein the mineral material comprises calcium carbonate and one or more of dolomite, a Group IIA and/or IIIA element-comprising phyllosilicate, montmorillonite, talc, magnesite, magnesium-comprising chlorite, and kaolin clay.

8. The process according to claim 1 , wherein the mineral material is a calcium carbonate.

9. The process according to claim 1 , wherein the aqueous suspension of step (a) comprises less than 0.1% by weight, based on the weight of dry mineral material, of a polyacrylate-based dispersant.

10. The process according to claim 1 , wherein the mineral material provided in step (a) has a BET specific surface area of 5 to 150 m 2 /g.

11. The process according to claim 1 , wherein the mineral material provided in step (a) has a BET specific surface area of 5 to 60 m 2 /g.

12. The process according to claim 1 , wherein the mineral material provided in step (a) has a BET specific surface area of 10 to 50 m 2 /g.

13. The process according to claim 1 , wherein the mineral material provided in step (a) has a weight median diameter (d 50 ) of 0.2 to 5 μm.

14. The process according to claim 1 , wherein the mineral material provided in step (a) has a weight median diameter (d 50 ) of 0.5 to 2 μm.

15. The process according to claim 1 , wherein the suspension in step (a) has a solids content of 20 to 80% by weight, based on the weight of the suspension.

16. The process according to claim 1 , wherein the suspension in step (a) has a solids content of 40 to 75% by weight, based on the weight of the suspension.

17. The process according to claim 1 , wherein the suspension in step (a) has a solids content of 50 to 70% by weight, based on the weight of the suspension.

18. The process according to claim 1 , wherein the agent is dosed in step (b) in an amount corresponding to from 0.1 to 0.75 mg by dry weight of agent per m 2 of the total surface of the mineral material.

19. The process according to claim 1 , wherein the agent is dosed in step (b) in an amount corresponding to from 0.1 to 5%, by dry weight relative to the dry weight of mineral material.

20. The process according to claim 1 , wherein the agent is dosed in step (b) in an amount corresponding to from 0.15 to 0.75%, by dry weight relative to the dry weight of mineral material.

21. The process according to claim 1 , wherein the agent is dosed in step (b) in an amount corresponding to from 0.15 to 0.5%, by dry weight relative to the dry weight of mineral material.

22. The process according to claim 1 , wherein the agent is provided in the form of an aqueous solution having a pH of 0 to 5.

23. The process according to claim 1 , wherein the agent is provided in the form of an aqueous solution having a pH of between 0.5 to 4.5.

24. The process according to claim 1 , wherein the phosphonic acid-comprising compound is an alkyl diphosphonic acid.

25. The process according to claim 1 , wherein the phosphonic acid-comprising compound is 1-hydroxyethane 1,1-diphosphonic acid (HEDP).

26. The process according to claim 1 , wherein the phosphonic acid-comprising compound is a selected from the group consisting of methylene diphosphonic acid (MDP), hydroxymethylene diphosphonic acid (HMDP), hydroxycyclomethylene diphosphonic acid (HCMDP), 1-hydroxy-3-aminopropane-1,1-diphosphonic acid (APD), aminotri (methylenephosphonic acid) (ATMP), diethylenetriaminepenta(methylenephosphonic acid) (DTPMP) and phosphonosuccinic acid (PSA).

27. The process according to claim 1 , wherein the metal of the metal cation or metal-comprising cationic compound is aluminium or zirconium.

28. The process according to claim 1 , wherein a base is added before and/or after the agent.

29. The process according to claim 28 , wherein the base is selected from the group consisting of sodium silicate, sodium hydroxide, potassium hydroxide, lithium hydroxide, sodium aluminate, a basic polyphosphate, a basic phosphonate, and any mixture thereof.

30. The process according to claim 28 , wherein the base is a basic polyphosphate or a basic phosphonate.

31. The process according to claim 28 , wherein the base is a potassium salt of pyrophosphate, an alkali compound of HEDP, or a sodium and/or potassium and/or lithium compound of HEDP.

32. The process according to claim 28 , wherein the base is added in an amount of greater than or equal to 0.1% by dry weight, relative to the dry weight of mineral material.

33. The process according to claim 28 , wherein the base is added in an amount of from 0.2 to 0.5% by dry weight, relative to the dry weight of mineral material.

34. The process according to claim 1 , wherein in step (d) the suspension of step (c) is concentrated by thermal or mechanical methods, or dried.

35. The process according to claim 1 , wherein the mineral matter is precipitated calcium carbonate.

36. The process according to claim 1 , wherein the mineral matter is ground calcium carbonate.

Assignments (2)
CHANGE OF NAME Recorded Oct 14, 2013
From: OMYA DEVELOPMENT AG
To: OMYA INTERNATIONAL AG
Reel/Frame 031406/0917 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 3, 2012
From: WIMMER, GUENTER; SCHOELKOPF, JOACHIM; STAUFFER, LEGAL REPRESENTATIVE FOR HANS-JOACHIM WEITZEL (DECEASED), FRIDOLIN
To: OMYA DEVELOPMENT AG
Reel/Frame 029390/0105 →
Priority Claims (1)
EP 10160235 · Apr 16, 2010 · regional
Continuity (2)
Provisional Application 61343128 · Apr 23, 2010
Related Publication 20130137779A1 · May 30, 2013