Methods for producing extracted and digested products from pretreated lignocellulosic biomass

• US 9,650,657 B2
• Filed: 04/19/2011
• Issued: 05/16/2017
• Est. Priority Date: 04/19/2010
• Status: Active Grant

• Current Assignee: The Board of Trustees of Michigan State University (Michigan State University)
• Original Assignee: The Board of Trustees of Michigan State University (Michigan State University)
• Inventors: Chundawat, Shishir, Balan, Venkatesh, Sousa, Leonardo Da Costa, Cheh, Albert M., Dale, Bruce
• Primary Examiner(s): Long, Scott
• Assistant Examiner(s): Barron, Sean C
• Application Number:
  US13/642,052
• Publication Number:
  US 20130217073A1
• Time in Patent Office: 2,219 Days
• Field of Search: None
• CPC Class Codes: C08B 15/02 Oxycellulose; Hydrocellulose; Cellulosehydrate, e.g. microcrystalline cellulose
• CPC Class Codes: C08B 37/0003 General processes for their isolation or fractionation, e.g. purification or extraction from biomass
• CPC Class Codes: C08B 37/0057 beta-D-Xylans, i.e. xylosaccharide, e.g. arabinoxylan, arabinofuronan, pentosans; (beta-1,3)(beta-1,4)-D-Xylans, e.g. rhodymenans; Hemicellulose; Derivatives thereof
• CPC Class Codes: C08H 6/00 Macromolecular compounds derived from lignin, e.g. tannins, humic acids
• CPC Class Codes: C08H 8/00 Macromolecular compounds derived from lignocellulosic materials pretreatment thereof B27N
• CPC Class Codes: C12P 19/14 produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase , e.g. by cellulase, hemicellulase
• CPC Class Codes: C12P 19/20 produced by the action of an exo-1,4 alpha-glucosidase, e.g. dextrose
• CPC Class Codes: C12P 2201/00 Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: C13K 1/02 obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

Methods for producing extracted and digested products from pretreated lignocellulosic biomass are provided. The methods include converting native cellulose I_β to cellulose III_I by pretreating the lignocellulosic biomass with liquid ammonia under certain conditions, and performing extracting or digesting steps on the pretreated/converted lignocellulosic biomass.

Claims

1. A method for producing an extracted product from lignocellulosic biomass comprising:

completely converting native cellulose I_β

to cellulose III_I by pretreating the lignocellulosic biomass with anhydrous liquid ammonia or liquid ammonia comprising a solution of at least 80% ammonia at a temperature from about 50°

C. to about 140°

C. and at atmospheric pressure or higher to generate a pretreated lignocellulosic biomass, wherein the lignocellulosic biomass has a moisture content of less than 20% and a weight ratio of liquid ammonia to lignocellulosic biomass is 3;

1 to 8;

1, wherein the pretreated lignocellulosic biomass contains lignin and/or hemicellulose; and

extracting at least a portion of the lignin and/or hemicellulose from said pretreated lignocellulosic biomass to produce said extracted product and a pretreated biomass product, wherein said extracted product contains said lignin and/or hemicellulose.

2. The method of claim 1, wherein the solution further comprises a solvent.

3. The method of claim 2, wherein the solvent is water or an organic solvent.

4. The method of claim 3, wherein the organic solvent is selected from acetone, ethanol, methanol, isopropanol, dichloromethane, methyl acetate, ethyl acetate, chloroform and combinations thereof.

5. The method of claim 1, wherein the lignocellulosic biomass is pretreated with the liquid ammonia for 1 minute to 3 hours.

6. The method of claim 1, wherein the temperature is from about 50°

C. to about 120°

C.

7. The method of claim 1, wherein the lignin is one of a plurality of plant cell wall components which are extracted in the extracting step.

8. The method of claim 7, wherein said plant cell wall components further include hemicellulose, arabinan, and combinations and degradation products thereof.

9. The method of claim 1, wherein glucan and xylan are retained with the pretreated biomass.

10. The method of claim 1, wherein the extracting step is performed simultaneously with the anhydrous liquid ammonia pretreatment.

11. The method of claim 1, wherein the extracting step is performed after the anhydrous liquid ammonia pretreatment.

12. The method of claim 1, further comprising digesting the pretreated biomass with a combination of enzymes.

13. The method of claim 12, wherein the combination of enzymes comprises at least one exocellulase, at least one endocellulase and/or beta-glucosidase.

14. The method of claim 13, wherein the combination of enzymes comprises Cel7A (Cellobiohydrolase I), Cel6A (Cellobiohydrolase II) and Cel7B (EG I), each of which are from Trichoderma (T.) reesei.

15. The method of claim 14, wherein the combination of enzymes further comprises Cel5A_tr, from T. reesei, Cel5A_ac from Acidothermus cellulolyticum, or a combination thereof.

16. The method of claim 15, wherein the combination of enzymes further comprises cellulase Cel12A, Cel61A, or Cel61B, each of which are from T. reesei or a combination thereof.

17. The method of claim 1, further comprising an enzymatic hydrolysis step to hydrolyze the pretreated biomass product, wherein said enzymatic hydrolysis step proceeds at a rate that is at least 1.5 times faster than a hydrolysis step performed using plant biomass that has not been pretreated with the liquid ammonia.

18. The method of claim 1, further comprising recycling the liquid ammonia in a batch mode, a semi-batch mode or continuously.

19. The method of claim 1, further comprising reusing the liquid ammonia to pretreat another batch of lignocellulosic biomass.

20. The method of claim 2, further comprising recycling the solvent in a batch mode, a semi-batch mode or continuously.

21. The method of claim 2, further comprising reusing the solvent to pretreat another batch of lignocellulosic biomass.

22. The method of claim 1, wherein the product is a biofuel.

23. The method of claim 1, wherein the extracted product is converted to a bioproduct comprising a resin, a polymer, a biofuel, a biochemical, heat and/or electricity.

24. The method of claim 1, wherein the liquid ammonia is combined with acetone.

25. The method of claim 24, wherein the liquid ammonia to acetone volume:

volume ratio ranges from 10;

90 to 99;

1.

27. The method of claim 1 wherein the pretreated biomass product comprises a cellulose-rich solids fraction and a liquid fraction.

28. The method of claim 27 wherein the plant biomass also contains hemicellulose and the cellulose rich solids fraction in the pretreated biomass product is separated from the hemicellulose and the lignin.

26. A method for producing a digested product from lignocellulosic biomass comprising:

completely converting native cellulose I_β

to cellulose III_I by pretreating the lignocellulosic biomass with anhydrous liquid ammonia or liquid ammonia comprising a solution of at least 80% ammonia at a temperature from about 50°

C. to about 140°

C. and at atmospheric pressure or higher to generate a pretreated biomass, wherein the lignocellulosic biomass has a moisture content less than 20% and a weight ratio of liquid ammonia to lignocellulosic biomass is 3;

1 to 8;

1, wherein the pretreated lignocellulosic biomass contains lignin and/or hemicellulose; and

digesting the pretreated biomass with a combination of enzymes to produce fermentable sugars, wherein the combination of enzymes comprises at least one exocellulase, at least one endocellulase and/or beta-glucosidase.