Methods for pretreating biomass

• US 8,968,515 B2
• Filed: 12/22/2010
• Issued: 03/03/2015
• Est. Priority Date: 05/01/2006
• 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: Balan, Venkatesh, Dale, Bruce E., Chundawat, Shishir, Sousa, Leonardo
• Primary Examiner(s): Kim, Taeyoon
• Assistant Examiner(s): Patury, Srikanth
• Application Number:
  US12/976,344
• Publication Number:
  US 20110192559A1
• Time in Patent Office: 1,532 Days
• Field of Search: 422/148, 435/100, 435/102, 435/105, 435/165, 435/277, 127/37
• US Class Current: 162/29
• CPC Class Codes: C08B 1/003 Preparation of cellulose solutions, i.e. dopes, with different possible solvents, e.g. ionic liquids solutions used in the manufacture of monocomponent artificial filaments or cellulose or derivatives thereof D01F2/02
• 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: Y02P 30/20 using bio-feedstock

Abstract

A method of alkaline pretreatment of biomass, in particular, pretreating biomass with gaseous ammonia.

Claims

1. A method for treating biomass comprising:

adding gaseous ammonia at an elevated temperature to a reaction vessel containing biomass, wherein the reaction vessel is operated under a pressure of about 100 psi to about 1000 psi;

allowing the gaseous ammonia to condense on the biomass and react with water present in the biomass, to produce a pretreated biomass, wherein the reaction vessel pressure is released over a period of greater than two minutes; and

removing residual ammonia present in the reaction vessel.

2. The method of claim 1 wherein the biomass has a temperature which increases substantially instantaneously due to an exothermic reaction between the water and gaseous ammonia react.

3. The method of claim 2 wherein the biomass temperature is between about 50°

C. and about 200°

C.

4. The method of claim 1 wherein the gaseous ammonia is delivered to the reaction vessel under pressure.

5. The method of claim 1 wherein the biomass is comprised of about 5% to about 233% water on a dry weight basis.

6. The method of claim 1 wherein the biomass is comprised of about 5% to about 60% water on a dry weight basis.

7. The method of claim 1 wherein the gaseous ammonia reacts with the water in the biomass for about 1 minute to about 120 minutes.

8. The method of claim 7 wherein the gaseous ammonia reacts with the water in the biomass for about 1 minute to about 20 minutes.

9. The method of claim 1 wherein the method is a continuous method or a semi-batch method.

10. The method of claim 1 further comprising delivering a carrier to the reaction vessel.

11. The method of claim 10 wherein the carrier is combined with the gaseous ammonia.

12. The method of claim 10 wherein the carrier is steam.

13. The method of claim 10 wherein the carrier is an oxidative carrier or an inert gas.

14. The method of claim 13 wherein the oxidative carrier is air and the inert gas is nitrogen.

15. The method of claim 1 wherein the reaction vessel is selected from a fluidized bed reactor, a fixed bed reactor and a semi-fluidized bed reactor.

16. The method of claim 1 wherein at least a portion of the water present in the biomass is added water.

17. The method of claim 1 wherein a biomass to ammonia ratio is from about 1:

0.2 to about 1;

2.

18. The method of claim 1 wherein the residual ammonia present in reaction vessel is removed with steam.

19. The method of claim 18 wherein the biomass to ammonia ratio is from about 1:

0.2 to about 1;

1.

20. The method of claim 1 wherein a biomass to ammonia ratio is from about 1:

0.01 to about 1;

5.

21. The method of claim 1 wherein the reaction vessel pressure is from about 200 psi to about 500 psi.

22. The method of claim 1 wherein the reaction vessel pressure is released over a period of greater than two minutes prior to the removing step.

23. The method of claim 22 further comprising recovering the gaseous ammonia provided to the reaction vessel and recycling at least a portion of said gaseous ammonia and at least a portion of the residual ammonia.

24. The method of claim 23 wherein at least 50% of said gaseous ammonia is recovered and recycled.

25. The method of-claim 23 wherein from about 50% to about 99.5% of said gaseous ammonia is recovered and recycled.

26. The method of claim 23 wherein the biomass is treated with a mixture of recycled gaseous ammonia and steam.

27. The method of claim 1 wherein the biomass has a moisture content of less than about 15% dry weight basis.

28. The method of claim 1 further comprising impregnating the biomass with ammonia prior to the allowing step.

29. The method of claim 28 wherein a biomass to ammonia ratio is from about 1:

0.01 to about 1;

0.3.

30. The method of claim 28 wherein the biomass is fed to the reaction vessel continuously.