METHOD FOR THE PRODUCTION OF GLUCOSE FROM LIGNOCELLULOSIC FEEDSTOCKS

• US 20100184151A1
• Filed: 01/13/2010
• Published: 07/22/2010
• Est. Priority Date: 01/14/2009
• Status: Active Grant

• Current Assignee: Iogen Energy Corporation (Iogen Corporation)
• Original Assignee: Iogen Energy Corporation (Iogen Corporation)
• Inventors: Tolan, Jeffrey S., Foody, Brian
• Granted Patent: US 8,298,796 B2
• Time in Patent Office: Days
• 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

Abstract

A method for producing glucose from a lignocellulosic feedstock is provided. The method comprises pretreating the lignocellulosic feedstock with acid to produce a pretreated feedstock composition. A calcium-containing stream is provided that comprises calcium that is obtained from the lignocellulosic feedstock and a calcium carbonate-containing stream is obtained by precipitation of the calcium from the calcium-containing stream. The pH of the pretreated feedstock is adjusted with (a) the calcium carbonate-containing stream; (b) a calcium hydroxide-containing stream that is derived from said calcium carbonate-containing stream by subjecting said calcium carbonate-containing stream to calcination; or (c) a combination of the calcium carbonate-containing stream and the calcium hydroxide-containing stream. The pH adjustment results in a neutralized pretreated lignocellulosic feedstock having a pH between about 3 and about 9 and enzymatic hydrolysis of the neutralized, pretreated lignocellulosic feedstock is then conducted with cellulase enzymes to produce the glucose.

Claims

1. A method for processing a lignocellulosic feedstock to produce glucose, said method comprising the steps of:

(i) pretreating the lignocellulosic feedstock with acid to produce a composition comprising pretreated feedstock;

(ii) providing a calcium-containing stream that comprises calcium that is obtained from the lignocellulosic feedstock;

(iii) producing a calcium carbonate-containing stream that is obtained by precipitation of said calcium from the calcium-containing stream;

(iv) adjusting the pH of a stream comprising said pretreated feedstock with

(a) the calcium carbonate-containing stream;

(b) a calcium hydroxide-containing stream that is derived from said calcium carbonate-containing stream by subjecting said calcium carbonate-containing stream to calcination;

or

(c) a combination of the calcium carbonate-containing stream and the calcium hydroxide-containing stream,

wherein said adjusting of the pH of said stream comprising the pretreated feedstock produces a neutralized, pretreated lignocellulosic feedstock having a pH between about 3 and about 9 and wherein the pH of the neutralized, pretreated lignocellulosic feedstock thus produced is greater than the pH of the composition comprising pretreated feedstock produced in step (i); and

(v) carrying out enzymatic hydrolysis of said neutralized, pretreated lignocellulosic feedstock with cellulase enzymes to produce the glucose.

2. The method according to claim 1, wherein the calcium-containing stream contains magnesium that is obtained from the feedstock and wherein magnesium carbonate is produced together with calcium carbonate by precipitation of said magnesium.

3. The method according to claim 1, wherein the acid used to pretreat said lignocellulosic feedstock is sulfuric acid.

4. The method according to claim 1, wherein the enzymatic hydrolysis is carried out in the presence of a microorganism that converts glucose to at least one fermentation product.

5. The method according to claim 1, wherein the precipitation of calcium comprises the addition of carbon dioxide, alkali, carbonate or bicarbonate salts, or a combination thereof, to the calcium-containing stream.

6. The method according to claim 1, wherein the precipitation of calcium comprises the addition of carbon dioxide and an alkali selected from the group consisting of ammonia, ammonium hydroxide, sodium hydroxide, potassium hydroxide, and a combination thereof, to the calcium-containing stream.

7. The method according to claim 5, wherein the carbonate or bicarbonate salts are selected from the group consisting of ammonium carbonate, sodium carbonate, potassium carbonate, ammonium bicarbonate, sodium bicarbonate, potassium bicarbonate and a combination thereof.

8. The method according to claim 1, wherein the precipitation of calcium is carried out at a pH of about 3 to about 11, a temperature of about 20°

C. to about 95°

C., and a time of about 5 min to about 48 hr.

9. The method according to claim 1, wherein the calcium-containing stream, from which said calcium is precipitated, is selected from the group consisting of:

(a′

) a sugar stream containing glucose, xylose, or a combination thereof;

(b′

) a still bottoms stream resulting from fermenting the glucose produced in step (v) to produce a fermentation broth comprising a fermentation product, distilling the fermentation broth to obtain a stream containing a concentrated fermentation product and the still bottoms stream;

(c′

) a stream resulting from combining the sugar stream and the still bottoms stream; and

(d′

) a stream derived from any one of the sugar stream, the still bottoms stream and the stream resulting from combining the sugar stream and the still bottoms stream.

10. The method according to claim 9, wherein the sugar stream is obtained from the composition comprising pretreated feedstock subsequent to the step of pretreating and prior to the step of enzymatically hydrolyzing.

11. The method according to claim 1, wherein the pretreating is conducted at a pH of about 0.4 to about 3.0.

12. The method according to claim 1, wherein the pretreating is conducted to hydrolyze at least a portion of hemicellulose present in said feedstock and increase accessibility of cellulose in said feedstock to being hydrolyzed with said cellulase enzymes.

13. The method according to claim 1, wherein the pretreating is conducted at a temperature of between about 160°

C. to about 280°

C.

14. The method according to claim 1, wherein the cellulase enzymes comprise cellobiohydrolases (CBHs), endoglucanases (EGs) and β

-glucosidase.

15. The method according to claim 1, wherein the lignocellulosic feedstock is selected from the group consisting of corn stover, soybean stover, corn cobs, rice straw, rice hulls, corn fiber, wheat straw, barley straw, canola straw, oat straw, oat hulls and combinations thereof.

16. The method according to claim 9, wherein the calcium-containing stream from which said calcium is precipitated is the still bottoms stream, or a stream derived therefrom.

17. The method according to claim 9, wherein the calcium-containing stream from which said calcium is precipitated is the stream resulting from combining the sugar stream and the still bottoms stream, or a stream derived therefrom.

18. The method according to claim 9, wherein the calcium-containing stream from which said calcium is precipitated is the sugar stream, or a stream derived therefrom.

19. The method according to claim 16, wherein, after the calcium is precipitated, a sugar-containing stream is obtained with a reduced concentration of calcium, which sugar-containing stream is fermented to produce an alcohol, a sugar alcohol, an organic acid, or a combination thereof.

20. The method according to claim 1, wherein the neutralized, pretreated lignocellulosic feedstock has a pH between about 4 and about 6.