Porous nanocrystalline cellulose structures
US-2016369078-A1 · Dec 22, 2016 · US
US12077910B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12077910-B2 |
| Application number | US-202117321990-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 17, 2021 |
| Priority date | Aug 27, 2015 |
| Publication date | Sep 3, 2024 |
| Grant date | Sep 3, 2024 |
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Some variations provide a process for producing a nanocellulose material, comprising: providing a biomass feedstock comprising a bleached or unbleached pulp material; fractionating the feedstock in the presence of an acid, a solvent for lignin, and water, to generate cellulose-rich solids and a liquid containing hemicellulose and lignin; and mechanically treating the cellulose-rich solids to form cellulose fibrils and/or cellulose crystals, thereby generating a nanocellulose material. The process is preferably co-located with, or adjacent to, a mill that generates the pulp material. There are several advantages of a bolt-on AVAP® nanocellulose plant to an existing pulp mill, as disclosed herein.
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What is claimed is: 1. A process for producing a nanocellulose material, said process comprising: (a) providing an unbleached pulp material, wherein said unbleached pulp material is a chemical pulp, a chemimechanical pulp, a chemithermomechanical pulp, or a combination thereof, wherein said unbleached pulp material is obtained from a distinct process, and wherein said unbleached pulp material received in this step (a) has already gone through complete chemical pulping, chemimechanical pulping, and/or chemithermomechanical pulping; (b) in a digestor, fractionating said unbleached pulp material in the presence of an acid, a solvent for lignin, and water, to generate cellulose-rich solids and a liquid containing hemicellulose and lignin, wherein said unbleached pulp material is fed to said digestor at a solids concentration of from 30 wt % solids to 50 wt % solids; (c) mechanically treating said cellulose-rich solids to form cellulose fibrils and/or cellulose crystals, thereby generating a nanocellulose material having a crystallinity of at least 60%; and (d) recovering said nanocellulose material, wherein said process is co-located with a pulping process that generates said unbleached pulp material. 2. The process of claim 1 , wherein said unbleached pulp material is a chemical pulp consisting of a kraft pulp, a sulfite pulp, a soda pulp, or a combination thereof. 3. The process of claim 1 , wherein said unbleached pulp material is recycled pulp from a pulp and paper mill. 4. The process of claim 1 , wherein said unbleached pulp material is recycled pulp from a paper product. 5. The process of claim 1 , wherein said acid is a sulfur-containing acid. 6. The process of claim 5 , wherein said sulfur-containing acid is selected from the group consisting of sulfur dioxide, sulfurous acid, sulfur trioxide, sulfuric acid, sulfonic acids, lignosulfonic acids, and combinations thereof. 7. The process of claim 1 , wherein said solvent for lignin is an aliphatic alcohol. 8. The process of claim 7 , wherein said aliphatic alcohol is ethanol. 9. The process of claim 1 , wherein said unbleached pulp material is obtained from a press line of a pulp machine that is part of said distinct process, and wherein said process further comprises shredding or grinding a pulp sheet into said unbleached pulp material. 10. The process of claim 1 , wherein said unbleached pulp material is never dried between said distinct process and said process. 11. A process for producing a nanocellulose material, said process comprising: (a) providing a bleached pulp material, wherein said bleached pulp material is a chemical pulp, a chemimechanical pulp, a chemithermomechanical pulp, or a combination thereof, wherein said bleached pulp material is obtained from a distinct process, and wherein said bleached pulp material received in this step (a) has already gone through complete chemical pulping with bleaching, chemimechanical pulping with bleaching, and/or chemithermomechanical pulping with bleaching; (b) in a digestor, fractionating said bleached pulp material in the presence of an acid and water, and optionally a solvent, to generate cellulose-rich solids and a liquid containing hemicellulose and lignin, wherein said bleached pulp material is fed to said digestor at a solids concentration of from 30 wt % solids to 50 wt % solids; (c) mechanically treating said cellulose-rich solids to form cellulose fibrils and/or cellulose crystals, thereby generating a nanocellulose material having a crystallinity of at least 60%; and (d) recovering said nanocellulose material, wherein said process is co-located with a pulping process that generates said bleached pulp material. 12. The process of claim 11 , wherein said bleached pulp material is a chemical pulp consisting of a kraft pulp, a sulfite pulp, a soda pulp, or a combination thereof. 13. The process of claim 11 , wherein said bleached pulp material is recycled pulp from a pulp and paper mill. 14. The process of claim 11 , wherein said bleached pulp material is recycled pulp from a paper product. 15. The process of claim 11 , wherein said acid is a sulfur-containing acid. 16. The process of claim 15 , wherein said sulfur-containing acid is selected from the group consisting of sulfur dioxide, sulfurous acid, sulfur trioxide, sulfuric acid, sulfonic acids, lignosulfonic acids, and combinations thereof. 17. The process of claim 11 , wherein said solvent is present and is an aliphatic alcohol. 18. The process of claim 17 , wherein said aliphatic alcohol is ethanol. 19. The process of claim 11 , wherein said bleached pulp material is obtained from a press line of a pulp machine that is part of said distinct process, and wherein said process further comprises shredding or grinding a pulp sheet into said bleached pulp material. 20. The process of claim 11 , wherein said bleached pulp material is never dried between said distinct process and said process.
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