Analytical method for determining the concentration of oxidized nanofibrillar cellulose in a sample
US-2016299119-A1 · Oct 13, 2016 · US
US10053817B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10053817-B2 |
| Application number | US-201514808480-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 24, 2015 |
| Priority date | Apr 27, 2010 |
| Publication date | Aug 21, 2018 |
| Grant date | Aug 21, 2018 |
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A process for manufacturing structured material 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, fibrillating the cellulose fibers in the presence of the at least one filler and/or pigment until a gel is formed, subsequently providing additional non-fibrillated fibers, and combining the gel with the additional non-fibrillated fibers.
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The invention claimed is: 1. A process for manufacturing a structured material comprising the steps of: (a) providing cellulose fibres; (b) providing at least one filler comprising calcium carbonate; (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; (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 larger 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 additional non-fibrillated fibres in the form of a fibre web; wherein before, during or after the addition of further non-fibrillated fibres in the form of a fibre web in step e), but after step d) and before step f), at least one further filler is added, wherein the at least one further filler and/or pigment comprises at least a fraction of particles having a median diameter d 50 in the nanometer range; (f) combining the nano-fibrillar gel of step d) with the non-fibrillated fibres in the form of a fibre web of step e), so that the combination of the nano-fibrillar cellulose gel and the non-fibrillated fibres in the form of a fibre web includes 0.5 to 20 wt. % of the nano-fibrillar cellulose gel, expressed by the cellulosic content of the nano-fibrillar cellulose gel, on a dry/dry basis; and (g) manufacturing a structured material from the combination of the nano-fibrillar cellulose gel and non-fibrillated fibres in the form of a fibre web. 2. The process according to claim 1 , wherein the combination of the nano-fibrillar cellulose gel and the non-fibrillated fibres in the form of a fibre web from step f) is subjected to dewatering. 3. The process according to claim 1 , wherein the cellulose fibres of steps a) and/or e) are independently selected from the group consisting of eucalyptus pulp, spruce pulp, pine pulp, beech pulp, hemp pulp, cotton pulp, bamboo pulp, bagasse, recycled pulp, deinked pulp, or any mixture thereof. 4. The process according to claim 1 , wherein the cellulose fibres of step a) are provided in the form of a suspension. 5. The process according to claim 1 , 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 %. 6. The process according to claim 1 , 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 %. 7. The process according to claim 1 , wherein the cellulose fibres of step a) are provided in the form of a suspension at a solids content of from 1.3 to 3 wt %. 8. The process according to claim 1 , wherein the filler of step b) is selected from the group consisting of precipitated calcium carbonate (PCC), natural ground calcium carbonate (GCC), surface modified calcium carbonate, and calcium carbonate in admixture with one or more of dolomite, talc, bentonite, clay, magnesite, satin white, sepiolite, huntite, diatomite, or a silicate. 9. The process according to claim 1 , wherein the filler of step b) is selected from the group consisting of precipitated calcium carbonate having vateritic, calcitic or aragonitic crystal structure, ultrafine discrete prismatic, scalenohedral or rhombohedral precipitated calcium carbonate, natural ground calcium carbonate, marble, limestone, and chalk, or any mixture thereof. 10. The process according to claim 1 , wherein the at least one further filler of step e) is 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, and silicate, or any mixture thereof. 11. The process according to claim 10 , wherein the at least one further filler of step e) is selected from the group consisting of precipitated calcium carbonate having vateritic, calcitic or aragonitic crystal structure, ultrafine discrete prismatic, scalenohedral or rhombohedral precipitated calcium carbonate, natural ground calcium carbonate, marble, limestone, and chalk, or any mixture thereof. 12. The process according to claim 1 , 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. 13. The process according to claim 1 , wherein the filler of step b) and/or the at least one further filler of step e) is associated with a dispersing agent selected from the group consisting of homopolymers or copolymers of polycarboxylic acids and/or their salts or derivatives or esters thereof; esters based on acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid; acryl amide or acrylic esters, methylmethacrylate, or any mixture thereof; and alkali polyphosphates, phosphonic-, citric- and tartaric acids and the salts or esters thereof; or any mixture thereof. 14. The process according to claim 1 , wherein the step c) is carried out by adding the filler to the fibres, or the fibres to the filler in one or several steps. 15. The process according to claim 1 , wherein the filler of step b) and/or the fibres of step a) are added entirely or in portions before or during the fibrillating step d). 16. The process according to claim 1 , wherein the weight ratio of fibres to filler of step b) on a dry weight basis is from 1:2 to 2:1. 17. The process according to claim 1 , wherein the fibrillating is carried out with a homogenizer or a friction grinder. 18. The process according to claim 1 , wherein the combination of the nano-fibrillar cellulose gel and the non-fibrillated fibres in the form of a fibre web includes 3 to 6 wt % of the nano-fibrillar cellulose gel, expressed by the cellulosic content of the nano-fibrillar gel, on dry/dry weight basis. 19. The process according to claim 1 , wherein the total content of filler comprising calcium carbonate on a dry weight basis of the structured material is from 1 wt % to 60 wt %. 20. The process according to claim 1 , wherein the total content of filler comprising calcium carbonate on a dry weight basis of the structured material is from 25 wt % to 40 wt %. 21. The process according to claim 1 , wherein the total content of filler comprising calcium carbonate on a dry weight basis of the structured material is from 30 wt % to 35 wt %. 22. The process according to claim 1 , wherein the structured material is a paper. 23. The process according to claim 1 , wherein the structured material is a material composite. 24. A process for manufacturing a structured material comprising the steps of: (a) providing cellulose fibres; (b) providing at least one filler comprising calcium carbonate and one or more of dolomite, talc, bentonite, clay, magnesite, satin white, sepiolite, huntite, diatomite, and a silicate; (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; (d) fibrillating the cellulose fibres in an aqueous environment in the presence of the at least one filler fro
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