Methods of biomass pretreatment

• US 5,865,898 A
• Filed: 07/27/1993
• Issued: 02/02/1999
• Est. Priority Date: 08/06/1992
• Status: Expired due to Term

• Current Assignee: Texas A&M University System
• Original Assignee: Texas A&M University System
• Inventors: Holtzapple, Mark T., Davison, Richard R.
• Primary Examiner(s): Mullis, Jeffrey C.
• Application Number:
  US08/096,972
• Time in Patent Office: 2,016 Days
• Field of Search: 536/56, 536/124, 162/29, 162/90, 162/190, 530/500, 426/312, 426/635, 426/636, 127/37, 423/165
• US Class Current: 127/37
• CPC Class Codes: A23K 10/32 from hydrolysates of wood or straw
• CPC Class Codes: C01F 11/18 Carbonates
• 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

The invention is directed to methods for the pretreatment of a lignocellulose-containing biomass. Pretreatment comprises the addition of calcium hydroxide and water to the biomass to form a mixture, and subjecting the mixture to relatively high temperatures for a period of time sufficient to render the biomass amenable to digestion. The pretreated biomass is digested to produce useful products such as feedstocks, fuels, and compounds including fatty acids, sugars, ketones and alcohols. Alternatively, the pretreatment process includes the addition of an oxidizing agent, selected from the group consisting of oxygen and oxygen-containing gasses, to the mixture under pressure. The invention is also directed to a method for the recovery of calcium from the pretreated biomass.

Claims

1. A method for pretreating a lignocellulose-containing biomass comprising the steps of adding calcium oxide or hydroxide and water and an oxidizing agent to the biomass to form a mixture;

and pretreating the biomass for oxidizing lignin without degrading the lignocellulose by maintaining the mixture at greater than ambient temperature, but less than 100°

C. for a period of less than about 36 hours, so that the pretreated biomass contains a weight of glucose that is susceptible to hydrolysis that is greater than about 75% by weight of the total glucose present in the biomass before pretreatment.

2. The method of claim 1 wherein the lignocellulose-containing biomass contains greater than 20% lignin.

3. The method of claim 1 wherein the oxidizing agent is added to the mixture at a pressure of between about 20 to about 500 psig.

4. The method of claim 1 wherein the oxidizing agent is added to the mixture at a pressure of about 100 psig.

5. The method of claim 1 wherein the mixture contains between about 6 to about 19 grams of water per gram of dry biomass.

6. The method of claim 1 wherein the mixture contains about 16 grams of water per gram of dry biomass.

7. The method of claim 1 wherein the mixture contains between about 2 to about 30 grams of calcium oxide or hydroxide per 100 grams of dry biomass.

8. The method of claim 1 wherein the mixture contains about 30 grams of calcium hydroxide per 100 grams of dry biomass.

9. The method of claim 1 wherein the lignocellulose-containing biomass is selected from the group consisting of grass, wood, bagasse, straw, paper, plant material, and combinations thereof.

10. The method of claim 1 wherein the mixture is maintained elevated between about 40°

C. to about 150°

C.

11. The method of claim 1 wherein the mixture is maintained elevated between about 100°

C. and about 140°

C.

12. The method of claim 1 wherein the mixture is maintained elevated about 120°

C.

13. The method of claim 1 wherein the period of time is between about 1 and about 36 hours.

14. The method of claim 1 wherein the period of time is about 3 hours.

15. The method of claim 1 wherein the elevated temperature is about 120°

C., the period of time is about 3 hours, and the oxidizing agent pressure is about 100 psig.

16. The method of claim 1 wherein the weight of glucose that is susceptible to hydrolysis is greater than about 90% by weight of the total glucose present in the biomass before pretreatment.

17. The method of claim 1 wherein the glucose rendered susceptible to hydrolysis comprises cellulose and hemicellulose.

18. The method of claim 1 wherein pretreatment does not degrade said biomass.

19. The method of claim 1 wherein the mixture is dry mixed before pretreatment.

20. The method of claim 1 wherein the mixture is continuously mixed during pretreatment.

23. The method of claim 16 wherein the weight of glucose that is susceptible to hydrolysis is greater than about 90% by weight of the total glucose present in the biomass before pretreatment.

21. A method for pretreating a lignocellulose-containing biomass comprising the steps of adding calcium oxide or hydroxide and water and an oxidizing agent, selected from the group consisting of oxygen and oxygen-containing gasses, to the biomass to form a mixture;

pretreating the biomass for oxidizing lignin without degrading the lignocellulose by maintaining the mixture at greater than ambient temperature, but less than 100°

C. for a period of less than about 36 hours, so that the pretreated biomass contains a weight of glucose that is susceptible to hydrolysis that is greater than about 75% by weight of the total glucose present in the biomass before pretreatment; and

hydrolyzing the pretreated biomass.

22. The method of claim 21 wherein the pretreated biomass is hydrolyzed by acid hydrolysis, enzymatic action, fermentation or a combination thereof.

24. The method of claim 21 wherein the glucose rendered susceptible to hydrolysis comprises cellulose and hemicellulose.

25. The method of claim 21 wherein pretreatment does not degrade said biomass.

26. A method for recovering calcium from a biomass pretreatment process comprising:

a) pretreating the biomass for oxidizing lignin without degrading the lignocellulose by adding calcium oxide or hydroxide and water and an oxidizing agent to the biomass to form a mixture and maintaining the mixture at greater than ambient temperature, but less than 100°

C. for a period of less than about 36 hours, so that the pretreated biomass contains a weight of glucose that is susceptible to hydrolysis that is greater than about 75% by weight of the total glucose present in the biomass before pretreatment;

b) carbonating the pretreated mixture or a liquid portion thereof to precipitate calcium carbonate or bicarbonate; and

c) recovering the precipitated calcium carbonate or bicarbonate.

27. The method of claim 26 wherein the pH of the carbonated mixture is between about 8.5 and about 10.5.

28. The method of claim 26 wherein the pH of the carbonated mixture is between about 9.0 and about 10.

29. The method of claim 26 further comprising heating the carbonated mixture to form carbon dioxide and calcium oxide, and recovering the calcium oxide.

30. The method of claim 26 wherein the precipitated calcium carbonate or bicarbonate is recovered by filtration, hydroclone separation, sedimentation, centrifugation or a combination thereof.

31. The method of claim 26 wherein the mixture is dry mixed before pretreatment.

32. The method of claim 26 wherein the mixture is continuously mixed during pretreatment.

33. A method for recovering calcium from a biomass pretreatment process comprising:

a) pretreating the biomass for oxidizing lignin without degrading the lignocellulose by adding calcium oxide or hydroxide and water and an oxidizing agent, selected from the group consisting of oxygen and oxygen-containing gasses, to the biomass to form a mixture and maintaining the mixture at greater than ambient temperature, but less than 100°

C. for a period of less than about 36 hours, so that the pretreated biomass contains a weight of glucose that is susceptible to hydrolysis that is greater than about 75% by weight of the total glucose present in the biomass before pretreatment;

b) adding a carbonating agent to the pretreated mixture or a liquid portion thereof to form calcium carbonate or bicarbonate;

c) heating the calcium carbonate or bicarbonate to form calcium oxide;

and recovering the calcium oxide.

34. The method of claim 33 wherein the carbonating agent is carbon dioxide gas.

35. The method of claim 33 wherein heating is performed by burning the remaining lignin of the digested biomass.

36. The method of claim 33 further comprising the step of digesting the carbonated mixture.

37. The method of claim 36 wherein digestion is performed by acid hydrolysis, enzymatic action, fermentation or a combination thereof.