Production of Fermentable Sugars and Lignin from Biomass Using Supercritical Fluids
US-2016244852-A1 · Aug 25, 2016 · US
US10385140B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10385140-B2 |
| Application number | US-201515511183-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 25, 2015 |
| Priority date | Sep 26, 2014 |
| Publication date | Aug 20, 2019 |
| Grant date | Aug 20, 2019 |
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Cellulose-containing compositions and method of making same are disclosed. The compositions comprise a cellulose product comprising a type-I cellulose, a type-II cellulose, amorphous cellulose, or a combination thereof. Further, methods are disclosed for making these compositions and for further hydrolyzing these compositions. Additionally, uses for the cellulose-containing compositions are disclosed.
Opening claim text (preview).
What is claimed: 1. A method comprising: providing a feedstock comprising a type-I cellulose; converting at least a portion of the type-I cellulose by contacting the feedstock with a fluid comprising a near critical or a supercritical water at a temperature above about 300° C. to form a cellulose product comprising a type-II cellulose; and hydrolyzing at least a portion of the type-II cellulose to form a hydrolyzed cellulose product. 2. The method of claim 1 , wherein the cellulose product comprises an unconverted type-I cellulose and the type-II cellulose. 3. The method of claim 2 , wherein at least one of conditions (1) and (2) is satisfied: (1) the cellulose product comprises cellulose having a weight-average molecular weight of about 3,000 g/mol to about 25,000 g/mol as determined on a sample of the cellulose product that has been prepared for gel-permeation chromatography analysis according to a first condition; and (2) cellulose in the cellulose product has a carbonyl content of at least about 60 μmol/g, as determined on a sample of the cellulose product that has been prepared for gel-permeation chromatography analysis according to a second condition. 4. The method of claim 2 , wherein the composition further comprises lignin. 5. The method of claim 2 , wherein the cellulose product has a weight-average molecular weight that is less than about 0.5 times the weight-average molecular weight of microcrystalline cellulose. 6. The method of claim 2 , further comprising separating the lignin from the cellulose product using a hydrocyclone; wherein at least a portion of the lignin is removed in an underflow of the hydrocyclone and at least a portion of the cellulose product is removed in an overflow of the hydrocyclone. 7. The method of claim 1 , wherein the hydrolyzing is carried out at a lower temperature than the converting. 8. The method of claim 1 , wherein the hydrolyzing comprises employing a fluid comprising hot compressed water. 9. The method of claim 1 , wherein the hydrolyzing is carried out using thermal energy originating from the converting. 10. The method of claim 1 , wherein the converting is conducted at a temperature above 100° C., and the type-II cellulose produced in the converting is maintained at a temperature above 100° C. prior to the hydrolyzing, and optionally during the hydrolyzing. 11. The method of claim 1 , wherein the converting produces a stream at a first temperature, and the method further comprises: lowering the first temperature of the stream to a second temperature; maintaining the stream at the second temperature for a period of time, and changing the stream to a third temperature prior to the hydrolyzing; wherein the hydrolyzing is conducted at a fourth temperature that is the same as or different from the third temperature. 12. The method of claim 1 , wherein the hydrolyzing comprises acid hydrolysis. 13. The method of claim 2 , further comprising hydrolyzing the type-II cellulose, wherein the type-II cellulose is selectively hydrolyzed over the unconverted type-I cellulose. 14. The method of claim 2 , further comprising recovering the unconverted type-I cellulose. 15. The method of claim 1 , wherein the cellulose product acts as a rheology modifier. 16. The method of claim 2 , further comprising employing at least a portion of the cellulose product as at least a portion of the feedstock, and repeating the method at least one time. 17. The method of claim 1 , wherein at least a portion of the feedstock is fractionated biomass. 18. The method of claim 1 , further comprising incorporating the hydrolyzed cellulose product into an adhesive selected from the group consisting of a phenolic resin, a phenol-formaldehyde resin, or a combination thereof. 19. A method comprising: providing a feedstock comprising a type-I cellulose; converting at least a portion of the type-I cellulose by contacting the feedstock with a fluid comprising a sub-critical, near-critical, or a supercritical water to form a composition comprising a cellulose product, wherein the cellulose product comprises unconverted type-I cellulose and a type-II cellulose, and hydrolyzing, in a different step from the converting, at least a portion of the unconverted type-I cellulose at the same or different conditions as the converting. 20. A method comprising: providing a feedstock comprising a type-I cellulose; converting at least a portion of the type-I cellulose to a type-II cellulose; and hydrolyzing at least a portion of the type-II cellulose; wherein the converting produces a composition comprising a cellulose product, wherein the cellulose product comprises an unconverted type-I cellulose and the type-II cellulose; and wherein the uncoverted type-I cellulose is recovered.
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