IP Library Granted Patent US 8,871,056
Granted Patent B2
US 8,871,056 · App. 13/138,646 · Granted Oct 28, 2014

Process for the production of nano-fibrillar cellulose gels

Inventors: Patrick A. C. Gane (Rothrist, CH); Joachim Schoelkopf (Killwangen, CH); Daniel Gantenbein (Basel, CH); Michel Schenker (Oftringen, CH)
Assignee: Omya International AG
D01D5/423D21C9/007C08J3/075D21C9/004B82Y30/00C08J5/005D21B1/30C08J3/00D21B1/04D01F2/00
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Quick Facts
Patent No.
US 8,871,056
App. No.
13/138,646
Granted
Oct 28, 2014
Kind
B2
Abstract

The present invention relates to a process for the production of nano-fibrillar cellulose gels by providing cellulose fibers and at least one filler and/or pigment; combining the cellulose fibers and the at least one filler and/or pigment; and fibrillating the cellulose fibers in the presence of the at least one filler and/or pigment until a gel is formed, as well as the nano-fibrillar cellulose gel obtained by this process and uses thereof.

Claims (37)

1. A process for the production of a nano-fibrillar cellulose gel comprising the steps of:

(a) providing cellulose fibres;

(b) providing a filler;

(c) combining the cellulose fibres of step (a) and the filler of step (b); and

(d) fibrillating the cellulose fibres and the filler from step (c) until a nano-fibrillar cellulose gel is formed,

wherein the filler is calcium carbonate, and wherein in step (d) the weight ratio of fibres to filler on a dry weight basis is from 1:33 to 10:1.

2. The process according to claim 1 , wherein the Brookfield viscosity of the nano-fibrillar cellulose gel formed in step (d) is lower than the Brookfield viscosity of a corresponding nano-fibrillar cellulose suspension having been fibrillated in the absence of the filler.

3. The process according to claim 1 , wherein the cellulose fibres in step (a) are eucalyptus pulp, spruce pulp, pine pulp, beech pulp, hemp pulp, cotton pulp, or any mixture thereof.

4. The process according to claim 1 , wherein the cellulose fibres in step (a) are provided in the form of a suspension.

5. The process according to claim 1 , wherein the cellulose fibres in step (a) are provided in the form of a suspension at a solids content of from 0.2 to 35 wt-%.

6. The process according to claim 1 , wherein the cellulose fibres in step (a) are provided in the form of a suspension at a solids content of from 0.25 to 10 wt-%.

7. The process according to claim 1 , wherein the cellulose fibres in step (a) are provided in the form of a suspension at a solids content of from 0.5 to 5 wt-%.

8. The process according to claim 1 , wherein the cellulose fibres in step (a) are provided in the form of a suspension at a solids content of from 1 to 4 wt-%.

9. The process according to claim 1 , wherein the cellulose fibres in step (a) are provided in the form of a suspension at a solids content of from 1.3 to 3 wt-%.

10. The process according to claim 1 , wherein the filler and/or pigment in step (b) is precipitated calcium carbonate.

11. The process according to claim 1 , wherein the filler in step (b) is precipitated calcium carbonate having a vateritic, a calcitic or an aragonitic crystal structure.

12. The process according to claim 1 , wherein the filler in step (b) is ultrafine discrete prismatic, scalenohedral or rhombohedral precipitated calcium carbonate.

13. The process according to claim 1 , wherein the filler in step (b) is natural ground calcium carbonate.

14. The process according to claim 1 , wherein the filler in step (b) is natural ground calcium carbonate selected from marble, limestone and/or chalk.

15. The process according to claim 1 , wherein the filler in step (b) is in the form of particles having a medium particle size of from 0.01 to 15 μm.

16. The process according to claim 1 , wherein the filler in step (b) is in the form of particles having a medium particle size of from 0.1 to 10 μm.

17. The process according to claim 1 , wherein the filler in step (b) is in the form of particles having a medium particle size of from 0.3 to 5 μm.

18. The process according to claim 1 , wherein the filler in step (b) is in the form of particles having a medium particle size of from 0.5 to 4 μm.

19. The process according to claim 1 , wherein the filler in step (b) comprises a dispersing agent.

20. The process according to claim 19 , wherein the dispersing agent is selected from homopolymers or copolymers of polycarboxylic acids and/or their salts or esters, acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, acryl amide or acrylic esters, or mixtures thereof alkali polyphosphates, phosphonic-, citric- and tartaric acids, salts or esters thereof or mixtures thereof.

21. The process according to claim 1 , wherein in step (d) the weight ratio of fibres to filler on a dry weight basis is from 1:10 to 7:1.

22. The process according to claim 1 , wherein in step (d) the weight ratio of fibres to filler on a dry weight basis is from 1:5 to 5:1.

23. The process according to claim 1 , wherein in step (d) the weight ratio of fibres to filler on a dry weight basis is from 1:3 to 3:1.

24. The process according to claim 1 , wherein in step (d) the weight ratio of fibres to filler on a dry weight basis is from 1:2 to 2:1.

25. The process according to claim 1 , wherein in step (d) the weight ratio of fibres to filler on a dry weight basis is from 1:1.5 to 1.5:1.

26. The process according to claim 1 , wherein the fibrillating in step (d) is carried out by a homogenizer or an ultra fine friction grinder.

27. A process for the production of a nano-fibrillar cellulose gel comprising the steps of:

(a) providing cellulose fibres;

(b) providing a filler;

(c) combining the cellulose fibres of step (a) and the filler of step (b); and

(d) fibrillating the cellulose fibres and the filler from step (c) until a nano-fibrillar cellulose gel is formed,

wherein the filler comprises calcium carbonate and one or more of dolomite, talc, bentonite, clay, magnesite, satin white, sepiolite, huntite, diatomite, and a silicate, and wherein in step (d) the weight ratio of fibres to filler on a dry weight basis is from 1:33 to 10:1.

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 21, 2016
From: OMYA INTERNATIONAL AG
To: OMYA-HOLDING AG
Reel/Frame 041119/0481 →
CHANGE OF NAME Recorded Nov 14, 2016
From: FIBERLEANTM TECHNOLOGIES LIMITED
To: FIBERLEAN TECHNOLOGIES LIMITED
Reel/Frame 040308/0951 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 14, 2016
From: OMYA HOLDING AG
To: FIBERLEANTM TECHNOLOGIES LIMITED
Reel/Frame 040309/0067 →
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 Oct 14, 2011
From: GANE, PATRICK A.C.; SCHOELKOPF, JOACHIM; GANTENBEIN, DANIEL; SCHENKER, MICHEL
To: OMYA DEVELOPMENT AG
Reel/Frame 027063/0299 →
Priority Claims (1)
EP 09156703 · Mar 30, 2009 · regional
Continuity (2)
Provisional Application 61212073 · Apr 6, 2009
Related Publication 20120107480A1 · May 3, 2012