Processing biomass
US-2015353974-A1 · Dec 10, 2015 · US
US12247353B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12247353-B2 |
| Application number | US-201917254317-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 20, 2019 |
| Priority date | Jun 21, 2018 |
| Publication date | Mar 11, 2025 |
| Grant date | Mar 11, 2025 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The present invention concerns a process for the dissolution of cellulose using an enzymatic treatment, followed by a chemical dissolution. Particularly, the invention relates to the utilization of oxidizing enzymes for said enzyme treatment step. The process of the invention will cause an improved dissolution of high molar mass cellulose fibres. The improved dissolution properties also cause an improved reactivity of the cellulose in subsequent reactions.
Opening claim text (preview).
The invention claimed is: 1. A process for the dissolution of cellulose fibres comprising: subjecting a cellulose raw material to an enzymatic treatment step using a lytic polysaccharide monooxygenase (LPMO) as an oxidative enzyme; and dissolving the thus obtained enzyme-treated cellulose in a non-derivatising solvent, wherein the LPMO is used at a concentration of 0.25-7 mg/g of the cellulose raw material in the enzymatic treatment step, and wherein the enzymatic treatment step is carried out in the presence of an electron donor, wherein the electron donor is gallic acid, and wherein the gallic acid is provided at a concentration of 1-5 mM in the enzymatic treatment step. 2. The process of claim 1 , wherein the cellulose raw material is selected from softwood kraft fibres, dissolving grade pulps, recycled fibres or cotton cellulose. 3. The process of claim 1 , further comprising carrying out the enzyme treatment at ambient conditions, at a pH level of 5-8, and for 0.5-24 h. 4. The process of claim 1 , further comprising carrying out the enzyme treatment in the presence of oxygen, hydrogen peroxide, or both. 5. The process of claim 1 , further comprising selecting the non-derivatising solvent from those containing one or more metal ligands. 6. The process of claim 1 , further comprising using the solvent in an amount sufficient to cause wetting of the cellulose fibres. 7. The process of claim 1 , further comprising carrying out the dissolution treatment, using the non-derivatising solvent, at ambient conditions or sub-zero temperatures for a duration of 10 minutes or more. 8. The process of claim 1 , wherein the concentration of LPMO is 0.5-6 mg/g of cellulose raw material. 9. The process of claim 1 , wherein the concentration of LPMO is 1-5 mg/g of cellulose raw material. 10. The process of claim 1 , wherein the solvent comprises one or more metal ligands selected from the group consisting of copper, cadmium, lithium, and zinc. 11. The process of claim 1 , wherein the solvent comprises cupriethylenediamine (CED) or NaOH/ZnO. 12. The process of claim 1 , wherein the (LPMO) LPMO produced from a strain of Trichoderma reesei lacking genes encoding for cbh1, cbh2, egl1, and egl2. 13. The process of claim 1 , wherein the solvent comprises cupriethylenediamine (CED).
Related publications grouped by family.
Answers are generated from the same data shown on this page.