PROCESSING BIOMASS

• US 20160017444A1
• Filed: 10/09/2014
• Published: 01/21/2016
• Est. Priority Date: 02/19/2014
• Status: Abandoned Application

• Current Assignee: Xyleco, Inc.
• Original Assignee: Xyleco, Inc.
• Inventors: Medoff, Marshall, Masterman, Thomas Craig, Cooper, Christopher G.F.
• Application Number:
  US14/439,799
• Publication Number:
  US 20160017444A1
• Time in Patent Office: Days
• US Class Current: 1/1
• 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: C13K 1/02 obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: C13K 13/002 Xylose
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

Biomass feedstocks (e.g., plant biomass, animal biomass, and municipal waste biomass) are processed to produce useful products, such as fuels. For example, systems are described that can be useful in enhancing sugar yields from biomass.

Claims

1. A method for processing a biomass, the method comprising:

heating a slurry comprising a reduced recalcitrance lignocellulosic material to a temperature greater than about 120°

C. for a time sufficient to further reduce the recalcitrance of the material.

2. The method of claim 1, wherein the reduced recalcitrance lignocellulosic material has been irradiated with between about 1 and 100 Mrad of ionizing radiation (e.g., between about 10 and about 50 Mrad, between about 20 and about 40 Mrad).

3. The method of claim 1, wherein the slurry comprises at least about 10 wt % solids (e.g., at least about 20 wt %, at least 30 wt %, at least about 40%, at least about 50 wt %).

4. The method of claim 1, wherein the reduced recalcitrance lignocellulosic material is heated for a time sufficient to swell the material to at least about 5 vol. % higher than the volume of the reduced recalcitrance lignocellulosic material prior to heating (e.g., at least about 10 vol. %, at least about 20 vol %, at least about 30 vol. %, at least about 40 vol. %, at least about 50 vol. %).

5. The method of claim 1, wherein the reduced recalcitrance lignocellulosic material is heated for a time sufficient to reduce the crystallinity of the material by at least 10% (e.g., at least 20%, at least 30%, at least 40%, at least 50%).

6. The method of claim 1, wherein the reduced recalcitrance lignocellulosic material is initially at a temperature below about 50°

C. and reaches a temperature above about 120 DEG C. in less than about 20% of the total time the biomass material is held at the temperature above about 120°

C. (e.g., less than about 10%, less than about 5%, less than about 1%).

7. The method of claim 1, wherein the time to reach the temperature above about 120°

C. is less than about 6 min (e.g., less than about 3 min, less than about 1 min, less than about 30 seconds, less than about 10 seconds) and the time the material is held at the temperature above about 120°

C. is at least 10 min (e.g., at least about 20 min, at least about 30 min, at least about 1 hour, at least about 4 hours, at least about 8 hours, at least about 12 hours).

8. The method of claim 1, wherein heating the slurry includes heating by steam injection heating (e.g., externally modulated steam injection, internally modulated steam injection).

9. The method of claim 1, wherein heating includes heating the slurry in a tube reactor (e.g., configured as a heated screw conveyor).

10. The method of claim 1, wherein heating includes heating the slurry utilizing indirect heating (e.g., utilizing a heated screw conveyor, utilizing a heated pressure cooker).

11. The method of claim 1, wherein heating includes heating the slurry in a tube reactor while agitating the slurry.

12. The method of claim 11, wherein agitating comprises mixing with a mechanical mixer selected from the group consisting of an auger mixer, a jet mixer, a recirculating pump and combinations thereof.

13. The method of claim 1, wherein the material is cooled in flash tank after heating the material (e.g., to a temperature between about 90 and 110°

C.).

14. The method of claim 1, wherein the material is cooled utilizing a cooling fluid fed heat exchanger (e.g., to a temperature between about 20 and about 80°

C., between about 30 and about 70°

C.).

15. The method of claim 1, wherein after heating the reduced recalcitrance lignocellulosic material is saccharified (e.g., utilizing an enzyme).

16. The method of claim 1, wherein after heating the reduced recalcitrance lignocellulosic material is contacted with an enzyme or organism.

17. The method of claim 1, wherein the lignocellulosic material is selected from the group consisting of wood, particle board, forestry wastes (e.g., sawdust, aspen wood, wood chips), grasses, (e.g., switchgrass, miscanthus, cord grass, reed canary grass), grain residues, (e.g., rice hulls, oat hulls, wheat chaff, barley hulls), agricultural waste (e.g., silage, canola straw, wheat straw, barley straw, oat straw, rice straw, jute, hemp, flax, bamboo, sisal, abaca, corn cobs, corn stover, soybean stover, corn fiber, alfalfa, hay, coconut hair), sugar processing residues (e.g., bagasse, beet pulp, agave bagasse), algae, seaweed, manure, sewage, and mixtures of any of these.

18. The method of claim 1, wherein after heating the reduced recalcitrance lignocellulosic material is fermented and then heated a second time to a temperature greater than about 120°

C.

19. The method of claim 1, wherein the reduced recalcitrance lignocellulosic material is heated at a rate of between about 340 DEG C.·

Kg/min and about 10,000,000 DEG C.·

Kg/min (e.g., between about 100,000 and about 500,000 DEG C.·

Kg/min).

20. The method of claim 1, wherein the reduced recalcitrance lignocellulosic material has an average particle size between about 0.25 mm and about 3 mm (e.g., between about 0.5 mm and about 2 mm) prior to being heated.

21. A method for processing a biomass material, the method comprising:

heating a reduced recalcitrance lignocellulosic material to a temperature greater than about 120°

C. using steam and forming a slurry by combining the steam and the reduced recalcitrance lignocellulosic material wherein the steam condenses and wets the reduced recalcitrance lignocellulosic material by condensation onto the reduced recalcitrance lignocellulosic material (e.g., an interior or exterior surface of the reduced recalcitrance lignocellulosic material).

22. The method of claim 21, wherein the reduced recalcitrance lignocellulosic material is heated at a rate of between about 340 DEG C.·

Kg/min and about 10,000,000 DEG C.·

Kg/min (e.g., between about 100,000 and about 500,000 DEG C.·

Kg/min).

23. The method of claim 21, wherein the slurry is held at the temperature greater than about 120°

C. for at least 1 min (e.g., at least 5 min, at least 10 min (e.g., at least 20 min, at least 30 min, at least 1 hour, at least 4 hours, at least 8 hours, at least 12 hours).

24. The method of claim 21, wherein the slurry includes at least about 10 wt % solids (e.g., at least about 20 wt %, at least 30 wt %, at least 40%, at least 50 wt %).

25. The method of claim 21, further comprising cooling the slurry to a temperature between about 20 and about 80°

C. (e.g., between about 30 and about 70°

C.).

26. The method of claim 21, wherein the steam and reduced recalcitrance lignocellulosic material are combined utilizing a Jet Cooker.

27. The method of claim 21, wherein the slurry is collected in a tube reactor that is agitated internally utilizing a mechanical agitator selected from the group consisting of an auger mixer, a jet mixer, a recirculating pump, and combinations thereof.

28. The method of claim 21, further comprising contacting the reduced recalcitrance lignocellulosic material with an organism or enzyme.

29. The method of claim 21, wherein the reduced recalcitrance lignocellulosic materiall is made by irradiating a cellulosic or lignocellulosic material with between about 10 and 50 Mrad of ionizing radiation (e.g., about 20 and about 40 Mrad).

30. A method for processing a biomass, the method comprising:

producing a sugar solution by enzymatically saccharifying a cellulosic or lignocellulosic material,

wherein the recalcitrance of the cellulosic or lignocellulosic material has been reduced by steam heating the material to a target temperature and irradiating the cellulosic or lignocellulosic material.

31. The method of claim 30, wherein the cellulosic or lignocellulosic material is held at the target temperature for between about 1 and about 240 min.

32. The method of claim 30, wherein the cellulosic or lignocellulosic material has been irradiated with an electron beam and receives a dose of irradiation between about 10 and about 50 Mrad.

33. The method of claim 30, wherein the target temperature is between about 120 and 160°

C.

34. The method of claim 30, wherein the material has been irradiated with between about 20 and about 40 Mrad, the final temperature is between about 140 and about 180°

C. and the temperature is held at the final temperature for between about 1 min and about 60 min.

35. The method of claim 30, wherein the sugar solution is fermented.