Biomass pretreatment

• US 8,030,030 B2
• Filed: 03/13/2008
• Issued: 10/04/2011
• Est. Priority Date: 03/14/2007
• Status: Active Grant

• Current Assignee: Suganit Systems, Inc., University of Toledo
• Original Assignee: Suganit Systems, Inc., University of Toledo
• Inventors: Anderson, Jared, Rao, Kripa, Kumar, Guneet, Paripati, Praveen, Varanasi, Sasidhar, Schall, Constance Ann, Dadi, Anantharam Prasad
• Primary Examiner(s): Saucier; Sandra
• Assistant Examiner(s): HANLEY, SUSAN MARIE
• Application Number:
  US12/075,762
• Publication Number:
  US 20080227162A1
• Time in Patent Office: 1,300 Days
• Field of Search: 435/72, 435/41, 435/200, 435/209
• US Class Current: 435/72
• CPC Class Codes: C12P 19/02 Monosaccharides 2-ketogulonic acid C12P7/60
• 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 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: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

A method for lignocellulose conversion to sugar with improvements in yield and rate of sugar production has been developed by using ionic liquid pretreatment. This new pretreatment strategy substantially improves the efficiency (in terms of yield and reaction rates) of saccharification of lignocellulosic biomass. Cellulose and hemicellulose, when hydrolyzed into their sugars, can be converted into ethanol fuel through well established fermentation technologies. These sugars also form the feedstocks for production of variety of chemicals and polymers. The complex structure of biomass requires proper pretreatment to enable efficient saccharification of cellulose and hemicellulose components to their constituent sugars. Current pretreatment approaches suffer from slow reaction rates of cellulose hydrolysis (by using the enzyme cellulase) and low yields.

Claims

1. A method for treating a lignocellulosic biomass comprising the steps of:

incubating a lignocellulosic biomass comprising lignin, cellulose, and hemicellulose in an ionic liquid (IL) for a sufficient time and temperature to swell the cellulose and hemicellulose by without dissolution of the biomass in the IL;

washing the IL-incubated biomass comprising lignin, cellulose and hemicellulose with a liquid non-solvent for cellulose that is miscible with water and the IL; and

contacting said swelled washed biomass comprising lignin, cellulose and hemicellulose with an aqueous buffer comprising enzymes capable of hydrolyzing both cellulose and hemicellulose to produce polysaccharides, and converting said polysaccharides to hexose and pentose sugars.

2. A method according to claim 1 wherein said contacting step forms a post-saccharification solid residue comprising lignin.

3. A method according to claim 2 wherein the lignin can be converted to fuels, chemicals, or polymers.

4. A method according to claim 1 comprising the further step of converting the hexose and pentose sugars to fuels, chemicals, or polymers.

5. A method according to claim 3 wherein between 75% to 97% of the cellulose is converted to glucose after 24 hours.

6. A method according to claim 1 wherein the time and temperature during the step of IL-incubation of the biomass is optimized to sufficiently swell matrices of the biomass to enhance the penetration of hydrolyzing enzymes and water during the hydrolysis step.

7. A method according to claim 1 wherein the incubating step comprises incubating the biomass for a time ranging from 5 minutes to 8 hours at a temperature ranging from 50°

C. to 200°

C.

8. A method according to claim 1 wherein the ionic liquid is molten during incubation.

9. A method according to claim 1 wherein the IL is capable of disrupting hydrogen-bonding in the structure of the cellulose or the hemicellulose wherein the IL comprises a cation selected from imidazolium, pyrrolidinium, pyridinium, phosphonium, or ammonium.

10. A method according to claim 1 wherein the IL is represented by the structure:

11. A method according to claim 1 wherein the IL is represented by the structure:

12. A method according to claim 10 or 11 wherein the halide is a chloride, fluoride, bromide or iodide.

13. A method according to claim 1 wherein the IL is 1-n-butyl-3-methylimidazolium chloride, 1-allyl-3-methyl imidazolium chloride, 3-methyl-N-butylpyridinium chloride, 1-ethyl-3-methyl imidazolium acetate, or 1-ethyl-3-methyl imidazolium propionate.

14. A method according to claim 1 wherein the liquid non-solvent for cellulose that is used for washing is water, an alcohol, acetonitrile or a solvent which dissolves the IL and thereby extracts the IL from the biomass.

15. A method according to claim 14 wherein the alcohol is ethanol, methanol, butanol, or propanol, and wherein the IL is recovered from the liquid non-solvent.

16. A method according to claim 15, comprising the further step of reusing the recovered IL for treating more biomass.

17. A method according to claim 15, comprising recovering the IL from the liquid non-solvent by a method selected from one or more of activated charcoal treatment, distillation, membrane separation, electro-chemical separation techniques, sold-phase extraction and liquid-liquid extraction.

18. A method according to claim 1, wherein the biomass is corn stover or poplar, and wherein the time required for complete enzymatic hydrolysis is within 16 to 36 hours.

19. A method according to claim 1, wherein the ionic liquid has a water content not exceeding 10%.

20. A method according to claim 1 wherein the incubation temperature is achieved by heating with agitation or microwave irradiation with intermittent agitation.

21. A method according to claim 1 wherein the ionic liquid is a mixture of composition described by Equation 1:

22. A method according to claim 21, comprising a five component mixture of the following ILs:

1-butyl-3-methyl imidazolium chloride ([BMIM⁺][Cl⁻

])+1-butyl-3-methyl imidazolium hexafluorophosphate ([BMIM⁺][PF₆₋

])+1-ethyl-3-methyl imidazolium chloride ([EMIM⁺][Cl⁻

])+1-ethyl-3-methyl imidazolium hexafluorophosphate ([EMIM⁺][PF₆₋

])+1-ethyl-3-methyl imidazolium tetrafluoroborate ([EMIM⁺][BF₄⁻

]).

23. A method according to claim 1, comprising the further step of recovering the IL following the washing step.

24. A method according to claim 23, wherein 99% or more of the IL is recovered.

28. A method according to claim 1 or claim 27 wherein the aqueous buffer comprising enzymes comprises an enzyme mixture of cellulases, endo-glucanases, exo-glucanases, and 1-β

-glucosidases.

29. A method according to claim 28, comprising the further step of recovering the enzymes from the hydrolyzed biomass.

30. A method according to claim 28, wherein said enzyme mixture further comprises xylanases or arabinases.

25. A method for disruption of the structure of a lignocellulosic biomass which comprises lignin, cellulose and hemicellulose and treating the disrupted biomass, comprising the steps of:

incubating the biomass in an ionic liquid (IL) for a sufficient time and temperature to swell the cellulose and hemicellulose without dissolution of the biomass in the IL;

washing the swelled IL-incubated lignocellulosic biomass with a liquid non-solvent for cellulose that is miscible with water and the IL; and

treating the incubated and washed lignocellulosic biomass with chemical or biochemical reagents to effect the conversion of the swollen biomass to useful chemicals.

26. A method according to claim 25 wherein the biochemical reagent used to convert the washed biomass is an added enzyme.

27. A method according to claim 25 wherein the treating step comprises adding a buffer comprising enzymes capable of hydrolyzing both cellulose and hemicellulose to the incubated and washed biomass to hydrolyze the cellulose and hemicellulose to sugar.