Concurrent saccharification and fermentation of fibrous biomass

• US 8,058,041 B2
• Filed: 07/03/2008
• Issued: 11/15/2011
• Est. Priority Date: 07/04/2007
• Status: Active Grant

• Current Assignee: Suzano Canada Inc. (Suzano S.A.)
• Original Assignee: Lignol Innovations Ltd (Suzano S.A.)
• Inventors: Pye, Edward Kendall, Berlin, Alex, O'Connor, Donald
• Primary Examiner(s): Lilling; Herbert J
• Application Number:
  US12/167,880
• Publication Number:
  US 20090011484A1
• Time in Patent Office: 1,230 Days
• Field of Search: 435/165, 435/289.1
• US Class Current: 435/165
• CPC Class Codes: C12M 21/12 for producing fuels or solvents C12M21/04 takes precedence; liquid carbonaceous fuels C10L1/00, solid fuels C10L5/00
• CPC Class Codes: C12M 45/04 Phase separators; Separation of non fermentable material; Fractionation
• CPC Class Codes: C12M 45/06 by chemical means or hydrolysis
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

A process for simultaneous saccharification and fermentation of a cellulosic solids fraction extracted from a lignocellulosic feedstock. The viscosity of the cellulosic solids fraction is reduced by intermixing with a liquid carbohydrate stream. A suitable liquid carbohydrate stream is a de-lignified liquids fraction that was previously separated from the solids fraction during processing of the lignocellulosic feedstock. Alternatively, the viscosity of the solids fraction may be reduced by commingling with a liquid carbohydrate stream comprising one or more monosaccharides. The reduced-viscosity cellulosic solids fraction is then commingled with a fermentative microbial inoculant and a cellulosic biomass-degrading enzyme composition. The commingled mixture is maintained in a pressurized reaction vessel under elevated temperatures to enable simultaneous enzymatic hydrolysis of the cellulosic solids to monosaccharides and fermentation of the monosaccharides to produce an ethanolic beer. The ethanolic beer is distillable for recovery of fuel-grade ethanol and a stillage that may be further processed.

Claims

1. A process for simultaneous saccharification and fermentation of a cellulosic solids fraction extracted from a lignocellulosic feedstock, the process comprising the steps of:

separating an extracted lignocellulosic feed stock into a cellulosic solids fraction and a liquids fraction;

processing said liquids fraction to remove extracted lignins therefrom thereby producing a de-lignified liquids fraction;

reducing the viscosity of the separated cellulosic solids fraction by intermixing said cellulosic solids fraction with a portion of said de-lignified liquids fraction;

intermixing the reduced-viscosity cellulosic solids fraction with (a) an effective amount of a fermentative microbial culture, and (b) an effective amount of a cellulosic biomass-degrading enzyme;

commingling said microbial culture, said biomass-degrading enzyme and said reduced-viscosity cellulosic solids fraction to provide a reaction mixture comprising ethanol; and

separating ethanol from said reaction mixture.

2. A process according to claim 1, wherein said de-lignified liquids fraction is intermixed with a liquid carbohydrate stream.

3. A process according to claim 1, wherein said liquid carbohydrate stream contains one of glucose, galactose, mannose, xylose or mixtures thereof.

4. A process according to claim 1, wherein said de-lignified liquids fraction is additionally processed to remove at least one of acetic acid, furfural and 5-hydoxymethyl-2-furfural prior to intermixing with the cellulosic solids fraction.

5. A process according to claim 1, wherein said lignocellulosic feedstock is selected from the group consisting angiosperm biomass, gymnosperm biomass, field crop biomass, vegetative and/or fruit pulps, wood and wood processing scraps and waste materials, recyclable paper and cardboard goods.

6. A process according to claim 1, wherein the fermentative microbial culture is a strain selected from the group consisting of yeast species, fungal species, and bacterial species.

7. A process according to claim 6, wherein the fermentative microbial culture is a strain selected from the group consisting of naturally occurring strains and genetically modified strains.

8. A process according to claim 7, wherein the fermentative microbial culture is a strain selected from the group consisting of Saccharomyces spp.

9. A process according to claim 8, wherein the fermentative microbial culture is Saccharomyces cerevisiae strain Y-1528.

10. A process according to claim 7, wherein the fermentative microbial culture is a fungal strain selected from the group consisting of Trichoderma spp. and Aspergillus spp.

11. A process according to claim 7, wherein the fermentative microbial culture is a bacterial strain selected from the group consisting of Zymomonas spp., Corynebacterim spp., Clostridium spp. and Escherichia coli.

12. A process according to claim 1, wherein the cellulosic biomass-degrading enzyme is selected from the group consisting of cellulases, β

-glucosidases, hemicellulases, β

-xylosidases, and mixtures thereof.

13. A process according to claim 1, wherein the process is a batch process.

14. A process according to claim 1, wherein the process is a continuous process.

15. A process according to claim 1, wherein the process is a semi-continuous process.

16. A process for simultaneous saccharification and fermentation of a cellulosic solids fraction extracted and separated from a lignocellulosic feedstock, the process comprising the steps of:

reducing the viscosity of the separated cellulosic solids fraction by intermixing said cellulosic solids fraction with a liquid stream comprising at least one monosaccharide carbohydrate;

intermixing the reduced-viscosity cellulosic solids fraction with (a) an effective amount of a fermentative microbial culture, and (b) an effective amount of a cellulosic biomass-degrading enzyme;

commingling said microbial culture, said biomass-degrading enzyme and said reduced-viscosity cellulosic solids fraction to provide a reaction mixture comprising ethanol; and

separating ethanol from said reaction mixture.

17. A process according to claim 16, wherein the liquid stream comprises a monosaccharide selected from the group consisting of glucose, mannose, galactose, xylose, and mixtures thereof.

18. A process according to claim 16, wherein said lignocellulosic feedstock is selected from the group consisting angiosperm biomass, gymnosperm biomass, field crop biomass, vegetative and/or fruit pulps, wood and wood processing scraps and waste materials, recyclable paper and cardboard goods.

19. A process according to claim 16, wherein the fermentative microbial culture is a strain selected from the group consisting of yeast species, fungal species, and bacterial species.

20. A process according to claim 19, wherein the fermentative microbial culture is a strain selected from the group consisting of naturally occurring strains and genetically modified strains.

21. A process according to claim 20, wherein the fermentative microbial culture is a strain selected from the group consisting of Saccharomyces spp.

22. A process according to claim 21, wherein the fermentative microbial culture is Saccharomyces cerevisiae strain Y1528.

23. A process according to claim 20, wherein the fermentative microbial culture is a fungal strain selected from the group consisting of Trichoderma spp. and Aspergillus spp.

24. A process according to claim 20, wherein the fermentative microbial culture is a bacterial strain selected from the group consisting of Zymomonas spp., Corynebacterim spp., Clostridium spp. and Escherichia coli.

25. A process according to claim 16, wherein the cellulosic biomass-degrading enzyme is selected from the group consisting of cellulases, β

-glucosidases, hemicellulases, β

-xylosidases, and mixtures thereof.

26. A process according to claim 16, wherein the process is a batch process.

27. A process according to claim 16, wherein the process is a continuous process.

28. A process according to claim 16, wherein the process is a semi-continuous process.