PROCESS FOR THE PRODUCTION OF GEL-BASED COMPOSITE MATERIALS

Abstract

A process for the production of composite materials comprising nano-fibrillar cellulose gels, by providing cellulose fibres and at least one filler and/or pigment, combining the cellulose fibres and the at least one filler and/or pigment, fibrillating the cellulose fibres in the presence of the at least one filler and/or pigment until a gel is formed, subsequently providing at least one further filler and/or pigment and combining the gel with the at least one further filler and/or pigment.

Claims

1-17. (canceled)

18. A process for the production of composite materials comprising nano-fibrillar cellulose gels from recycled and/or deinked pulp.sup.1, characterized by the steps of: (a) providing cellulose fibres in the form of recycled and/or deinked pulp; (b) providing at least one filler, wherein the filler of step (b) consists of particles having a median particle size of from 0.5 to 4 μm; (c) combining the cellulose fibres of step (a) and the at least one filler of step (b) at a weight ratio of fibres to filler on a dry weight basis of from 1:33 to 10:1 by adding the fibres and at least one filler entirely or in portions before or during the fibrillating step (d); d) fibrillating the cellulose fibres in an aqueous environment in the presence of the at least one filler from step (c) until a nano-fibrillar cellulose gel is formed, wherein the formation of the gel is verified by monitoring the viscosity of the mixture in dependence of the shearing rate, wherein the viscosity decrease of the mixture upon step-wise increase of the shearing rate is stronger than the corresponding viscosity increase upon subsequent step-wise reduction of the shearing rate over at least part of the shear rate range as shearing approaches zero; e) providing at least one further filler, wherein the at least one further filler from step (e) consists of particles having a median particle size of from 0.01 to 15 μm; and f) combining the nano-fibrillar gel obtained in step (d) with the at least one further filler from step (e), wherein the combination of the gel and the at least one further filler from step (e) is subjected to dewatering to obtain a compacted composite material.

19. The process according to claim 18, wherein the cellulose fibres of step (a) are provided in the form of a suspension.

20. The process according to claim 18, wherein the cellulose fibres of step (a) are provided in the form of a suspension at a solids content of from 0.2 to 35 wt %.

21. The process according to claim 18, wherein the cellulose fibres of step (a) are provided in the form of a suspension at a solids content of from 1 to 4 wt %.

22. The process according to claim 18, wherein the filler of step (b) and step (e) are independently selected from the group consisting of precipitated calcium carbonate (PCC), natural ground calcium carbonate (GCC), surface modified calcium carbonate, dolomite, talc, bentonite, clay, magnesite, satin white, sepiolite, huntite, diatomite, a silicate, or any mixture thereof.

23. The process according to claim 18, wherein the filler of steps (b) and (e) are independently selected from the group consisting of precipitated calcium carbonate (PCC) having vateritic, calcitic or aragonitic crystal structure, ultrafine discrete prismatic, scalenohedral or rhombohedral precipitated calcium carbonate, natural ground calcium carbonate, marble, limestone, chalk, or any mixture thereof.

24. The process according to claim 18, wherein the cellulose fibres are provided in the form of a suspension having a solids content of from 0.2 to 35 wt-%.

25. The process according to claim 18, wherein the cellulose fibres are provided in the form of a suspension having a solids content of from 0.25 to 10 wt-%.

26. The process according to claim 18, wherein the cellulose fibres are provided in the form of a suspension having a solids content of from 0.5 to 5 wt-%.

27. The process according to claim 18, wherein the cellulose fibres are provided in the form of a suspension having a solids content of from 1 to 4 wt-%.

28. The process according to claim 18, wherein the at least one further filler of step (e) consists of particles having a median particle size of from 0.01 to 5 μm.

29. The process according to claim 18, wherein the at least one further filler of step (e) consists of particles having a median particle size of from 0.05 to 1.5 μm.

30. The process according to claim 18, wherein the at least one further filler of step (e) consists of particles having a median particle size of from 0.1 to 0.8 μm.

31. The process according to claim 18, wherein the filler of steps (b) and/or (e) is associated with dispersing agents selected from homopolymers or copolymers of polycarboxylic acids and/or their salts or derivatives or esters thereof; ester based on acrylic acid, methyacryloic acid, maleic acid, fumaric acid itaconic acid; acryl amide, or acrylic acid esters, methylmethacrylate or any mixtures thereof; alkali polyphosphates, phosphonic-, citric- and tartaric acids and the salts or esters thereof; or mixture thereof.

32. The process according to claim 18, wherein the combination of fibres and of at least one filler of step (b) is carried out by adding the filler to the fibres, or the fibres to the filler and/or pigment, in one or several steps.

33. The process according to claim 18, wherein the weight ratio of fibres to filler in step (c) on a dry weight basis is from 1:10 to 7:1.

34. The process according to claim 18, wherein the weight ratio of fibres to filler in step (c) on a dry weight basis is from 1:2 to 2:1.

35. The process according to claim 18, wherein the fibrillating is carried out with a homogenizer or a friction grinder.

36. The process according to claim 18, wherein the weight ratio of fibres from step (a) to filler of step (e) on a dry weight basis is from 1:3 to 9:1.

37. The process according to claim 18, wherein the weight ratio of fibres from step (a) to filler of step (e) on a dry weight basis is from 1:2 to 3:1.

38. The process according to claim 18, wherein the total content of filler of steps (b) and (e) on a dry weight basis of the composite material is from 10 wt-% to 95 wt-%.

39. The process according to claim 18, wherein the total content of filler of steps (b) and (e) on a dry weight basis of the composite material is from 20 wt-% to 75 wt-%.

40. The process according to claim 18, wherein the total content of filler of steps (b) and (e) on a dry weight basis of the composite material is from 25 wt-% to 67 wt-%.

41. The process according to claim 18, wherein the total content of filler of steps (b) and (e) on a dry weight basis of the composite material is from 33 wt-% to 50 wt-%.

42. A composite material obtained by the process according to claim 18.

43. A composite material obtained by a process for the production of composite materials comprising nano-finrillar cellulose gels, characterized by the steps of: a) providing cellulose fibres; b) providing at least one filler and/or pigment; c) combining the cellulose fibres of step a) and the at least one filler and/or pigment of step b); d) fibrillating the cellulose fibres in the presence of the at least one filler and/or pigment until a gel is formed; e) providing at least one further filler and/or pigment; f) combining the gel of step d) with the at least one further filler and/or pigment of step e).

44. The composite material according to claim 43, characterized in that the combination of step f) is dewatered in dewatering step g).

45. A construction material comprising the composite material of claim 42.

46. A construction material comprising the composite material of claim 43.

47. A construction material comprising the composite material of claim 44.

48. A packaging material comprising the composite material of claim 42.

49. A packaging material comprising the composite material of claim 43.

50. A packaging material comprising the composite material of claim 44.

Description

EXAMPLES

[0066] Material [0067] OC-GCC: Omyacarb© 10-AV available from Omya AG; Fine calcium carbonate powder manufactured from a high purity, white marble; the weight median particle size d.sub.50 is 10 μm measured by Malvern Mastersizer X. [0068] HO-ME: Hydrocarb® HO-ME available from Omya AG; Selected, natural ground calcium carbonate (marble), microcrystalline, rhornbohedral particle shape of high fineness in the form of a pre-dispersed slurry (solids content 62 wt-%); the weight median particle size d.sub.50 is 0.8 μm measured by Sedigraph 5100. [0069] Nano-GCC: Natural ground calcium carbonate (marble from Vermont); dispersed slurry (solids content 50 w-%); the volume median particle size is d.sub.50 of 246 nm measured by Malvern Zetasizer Nano ZS. [0070] Pulp: Eucalyptus pulp with 25° SR.

Gel Formation

[0071] 120 g Eucalyptus pulp in the form of dry mats was torn into pieces and mixed with 5880 g tap water and the respective amount of OC-GCC (see Table 1) was added. The resulting mixture was stirred for at least 15 minutes using a Pendraulik (dissolver disk) at 4000 rpm. The fibrillar content of the formulations was 3 wt %.

[0072] The resulting mixtures subsequently were fibrillated in an ultra-fine friction grinder (Supermasscolloider from Masuko Sangyo Co. Ltd, Japan (Model MKCA 6-2) in single passes at a “gap” of −50 μm (dynamic 0-point) with the following setup:

[0073] 5 passes at 2500 rpm,

[0074] 2 passes at 2000 rpm,

[0075] 2 passes at 1500 rpm,

[0076] 2 passes at 1000 rpm,

[0077] 2 passes at 750 rpm,

[0078] 2 passes at 500 rpm.

[0079] The grinding stones were silicon carbide with a grit class of 46 (grit size 297-420 μm).

TABLE-US-00001 TABLE 1 Composition and characteristics of the gel used for compact formulations Parts GCC Energy Brookfield viscosity on pulp input at 2 wt- fibres [MWh/ % solids content Sample [dry/dry] dmt] [MPa .Math. s] 1 1 5.38 1612

Production of Formulations

[0080] In order to obtain and test compacts of the nano cellulosic gels, the following formulations for the specimen production were produced according to Table 2.

TABLE-US-00002 TABLE 2 Composition of compact formulations GCC in gel Additional Total GCC in formulation GCC formulation [parts dry on [parts dry [parts dry on fibres on fibres fibres dry] (wt % dry] (wt % on dry] (wt % on on overall overall overall Sample formulation) formulation) formulation) 1 1 p (50 wt %) 0 p (0 wt %) 1 p (50 wt %) 2 1 p (25 wt %) 2p nano GCC 3 p (75 wt %) (sample 1 + (50 wt %) 2 p Nano) 3 1 p (25 wt %) 2p HO—ME 3 p (75 wt %) (sample 1 + (50 wt %) 2 p HO—ME (disp.))

[0081] The gel of sample 1 was mixed with the corresponding amount of additional GCC as mentioned in Table 2 and blended by hand with a spatula.

[0082] Subsequently, the formulations were put into a small filter press (filter paper of Whatman Schleicher & Schuell, 589/2, white ribbon; filter press: fann filter press, series 3000, fann instrument company, Houston Tex., USA) in such amounts that a final thickness of the specimen of about 3 mm (calculated via densities) was achieved. A PMMA disc (thickness: 10 mm, diameter: 78 mm (fitting the inner diameter of the filter press) was placed on top of the formulation which again was covered by additional material of the same formulation (around 10-20 wt % of the amount of formulation already present).

[0083] The filter press then was closed and the following pressure profile was applied:

[0084] 15 min at 1 bar,

[0085] 120 min at 4 bar,

[0086] 45 min at 6 bar.

[0087] Subsequently, the “semi-dry” disc (solids content: about 50 wt %) was taken out of the filter press and cut into five identical rectangles (40 mm×10 mm). These rectangles were placed between two filter papers and two aluminium plates weighted with steel balls (about 3000 g), and dried in an oven at about 80° C. over night.