Biomass liquefaction processes, and uses of same

Patent metadata

Field	Value
Publication number	US-9359619-B2
Application number	US-201313754352-A
Country	US
Kind code	B2
Filing date	Jan 30, 2013
Priority date	Jul 30, 2010
Publication date	Jun 7, 2016
Grant date	Jun 7, 2016

Abstract

Described are processes for the liquefaction of lignocellulosic biomass under the digestive action of dicarboxylic acid(s). Such digests can exhibit enhanced flowability, reduced volume, and significant biomass conversion to dissolved components, and can in some embodiments be further liquefied by contact with an enzyme. Products resultant of these steps can be used for their sugar content to manufacture biofuels or other products.

First claim

The invention claimed is:

1. A method for liquefaction of solid lignocellulosic biomass, comprising:
(a) contacting the solid lignocellulosic biomass with a dicarboxylic acid for a period of time and under conditions effective to form an acidic mixture containing liquefied lignocellulosic biomass components and unliquefied lignocellulosic biomass components, wherein said contacting is conducted in the presence of from about 0.1% to 2% of the dicarboxylic acid relative to the lignocellulosic biomass on a dry weight basis, wherein said contacting is conducted with said dicarboxylic acid in an aqueous medium, and wherein the aqueous medium is at least 80% by weight aqueous;
(b) neutralizing the acidic mixture to form a neutralized mixture containing the liquefied lignocellulosic biomass components and unliquefied lignocellulosic biomass components, wherein said liquefied lignocellulosic biomass components in the neutralized mixture comprise phenols; and
(c) after said neutralizing, enzymatically hydrolyzing the unliquefied lignocellulosic biomass components in the presence of at least a portion of the liquefied lignocellulosic biomass components, wherein said enzymatically hydrolyzing is conducted sufficiently to form a flowable enzyme-hydrolyzed composition fluid having a yield stress of less than about 1000 Pascals, and wherein said enzymatically hydrolyzing is conducted in the presence of a cellulase enzyme at a level of 3 Filter Paper Units or less per gram of glucan in the solid lignocellulosic biomass.

2. The method of claim 1 , wherein the dicarboxylic acid is selected from maleic acid, succinic acid, and oxalic acid.

3. The method of claim 2 , wherein the dicarboxylic acid is maleic acid.

4. The method of claim 1 , wherein the lignocellulosic biomass is wood.

5. The method of claim 1 , wherein said contacting the lignocellulosic biomass is at a temperature of at least about 100° C.

6. The method of claim 1 , wherein said contacting the lignocellulosic biomass is for a period of up to about 60 minutes.

7. The method of claim 1 , wherein said enzymatically hydrolyzing is performed with the cellulase enzyme at a concentration of less than about 2 milligrams per gram of the lignocellulosic biomass dry matter.

8. The method of claim 1 , wherein said liquefied lignocellulosic biomass components in the neutralized mixture comprise furfural and 5-hydroxymethylfurfural.

9. A method for liquefaction of wood biomass, comprising:
(a) forming a mixture including an aqueous solution of a dicarboxylic acid and solid, particulate wood biomass containing hemicellulose, wherein said aqueous solution of a dicarboxylic acid is at least 80% by weight aqueous, wherein said mixture contains about 0.1 to 2% of the dicarboxylic acid relative to the wood biomass on a dry weight basis, and wherein the solid, particulate wood biomass comprises elongate fibrous particles having an average length of at least 1 mm; and
(b) incubating the mixture for a period of time and under conditions effective to cause hydrolysis of the wood biomass substantially by the dicarboxylic acid to form a flowable composition and to achieve greater than 70% hydrolysis of the hemicellulose to xylose; and further wherein the formed flowable composition has a total monomeric xylose content of at least 15 g/L and a total furfural content of less than 5 g/L.

10. The method of claim 9 , wherein the elongate fibrous particles have an average length of about 2 to 4 cm.

11. The method of claim 9 , wherein the dicarboxylic acid is selected from maleic acid, succinic acid, and oxalic acid.

12. The method of claim 11 , wherein the dicarboxylic acid is maleic acid.

13. The method of claim 9 , wherein said forming is conducted so as to achieve an initial loading of the wood biomass in the mixture of at least 15% by weight based on the dry weight of the wood biomass.

14. The method of claim 9 , wherein said incubating is conducted sufficiently to liquefy at least 10% by weight of the wood biomass dry matter.

15. The method of claim 9 , further comprising the step of neutralizing the flowable composition to form a neutralized composition.

16. The method of claim 9 , wherein the dicarboxylic acid constitutes greater than 50%, on a molar basis, of the organic protic species in the aqueous solution.

17. The method of claim 9 , wherein the aqueous solution is essentially free of organic protic species other than the dicarboxylic acid.

18. A method for liquefaction of lignocellulosic wood biomass, comprising:
(a) forming a mixture including an aqueous solution of a dicarboxylic acid and solid, particulate lignocellulosic wood biomass containing hemicellulose, with the biomass present at a level of at least 10% by weight in the mixture, wherein said mixture contains about 0.1 to 2% of the dicarboxylic acid relative to the lignocellulosic wood biomass on a dry weight basis, wherein said aqueous solution of a dicarboxylic acid is at least 80% by weight aqueous, and wherein the particulate lignocellulosic wood biomass has an average maximum particle dimension of at least 3 mm; and
(b) incubating the mixture at a temperature and for a period of time (i) sufficient to form a flowable biomass composition in which at least about 20% of the biomass solids have been converted to biomass components dissolved in the solution, (ii) sufficient to achieve greater than 70% hydrolysis of the hemicellulose to xylose, and (iii) sufficient to form the flowable biomass composition having a total monomeric xylose content of at least 15 g/L and a total furfural content of less than 5 g/L.

19. The method of claim 18 , wherein the incubating is effective to increase the bulk density of the solids by at least about 15%.

20. The method of claim 18 , wherein said incubating occurs in a first vessel, and also comprising the step of pumping the flowable biomass composition through a conduit to a second vessel.

21. A method for treating lignocellulosic wood biomass, comprising:
contacting a starting lignocellulosic wood biomass with a dicarboxylic acid for a period of time and under conditions effective to form an acidic mixture containing liquefied lignocellulosic biomass components and unliquefied lignocellulosic biomass components, wherein said contacting is conducted with said dicarboxylic acid in a liquid aqueous medium, and wherein the aqueous medium is at least 80% by weight aqueous;
neutralizing the acidic mixture to form a mixture containing dicarboxylate anions, cations, liquefied lignocellulosic wood biomass components including xylose, glucose phenols, and unliquefied lignocellulosic wood biomass components; and
contacting the mixture containing dicarboxylate anions, cations, liquefied lignocellulosic wood biomass components including xylose, glucose, phenols, and unliquefied lignocellulosic wood biomass components, with a cellulase enzyme at a level of 3 Filter Paper Units or less per gram of glucan in the starting lignocellulosic wood biomass for a period of time and under conditions effective to hydrolyze at least a portion of the unliquefied lignocellulosic biomass components, wherein said contacting is conducted sufficiently to form a flowable enzyme-hydrolyzed composition fluid having a yield stress of less than about 1000 Pascals.

22. The method of claim 21 , wherein the dicarboxylate anions are maleate anions.

23. The method of claim 21 , wherein the lignocellulosic biomass components are wood components.

24. The method

Assignees

• Purdue Research Foundation

Inventors

• Ladisch Michael R
• Mosier Nathan
• Kim Youngmi

Classifications

• C12P2201/00

  Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis · CPC title

• C12P7/10 Primary

  substrate containing cellulosic material · CPC title

• C12P7/14 Primary

  Multiple stages of fermentation; Multiple types of microorganisms or re-use of microorganisms · CPC title

• C12P19/02

  Monosaccharides (2-ketogulonic acid C12P7/60) · CPC title

• C12Y302/01004

  Cellulase (3.2.1.4), i.e. endo-1,4-beta-glucanase · CPC title