CHLORINE DIOXIDE TREATMENT OF BIOMASS FEEDSTOCK

• US 20120040413A1
• Filed: 08/11/2010
• Published: 02/16/2012
• Est. Priority Date: 08/11/2010
• Status: Active Grant

• Current Assignee: Chevron USA Incorporated (Chevron Corp.), Georgia Tech Research Corporation (University System of Georgia)
• Original Assignee: Chevron USA Incorporated (Chevron Corp.), Georgia Tech Research Corporation (University System of Georgia)
• Inventors: Miller, Stephen J., Sannigrahi, Poulomi, Rasgauskas, Arthur J.
• Granted Patent: US 8,497,097 B2
• Time in Patent Office: Days
• US Class Current: 435/105
• 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 2203/00 Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

The instant invention pertains to the use of chlorine dioxide in new processes for treating lignocellulosic feedstocks, as well as, new compositions suitable for, for example, bioalcohol production. Advantageously, the processes and compositions of the present invention may be used in more environmentally friendly, cost-efficient production of fuels and, if desired, may be coupled with other biomass processing facilities such as Kraft pulp bleaching mills.

Claims

1. A process for treating a lignocellulosic feedstock wherein the process comprises:

(a) contacting the feedstock with a solution comprising chlorine dioxide, ethanol, and water to form a mixture;

(b) heating the mixture at a temperature and time sufficient to produce a composition mixture comprising (1) a first solid portion comprising cellulose which is suitable for enzymatic hydrolysis, (2) a second solid portion comprising lignin or a derivative thereof, and (3) a solution comprising hemicellulose.

2. The process of claim 1 wherein the lignocellulosic feedstock has a holocellulose content of greater than about 50 weight percent of the total feedstock as measured by NREL/TP 510-42618.

3. The process of claim 1 which further comprises enzymatically hydrolyzing at least part of the first solid portion to form a composition comprising glucose.

4. The process of claim 3 which further comprises fermenting the composition comprising glucose.

5. The process of claim 1 wherein the amount of chlorine dioxide employed in step (a) is from about 0.5% to about 8% by weight based on the total dry weight of feedstock employed.

6. The process of claim 1 wherein the feedstock is contacted with the solution comprising chlorine dioxide, ethanol, and water at a temperature of from about 50°

C. to about 90°

C. for a time of at least about 1 hour.

7. The process of claim 1 wherein the feedstock is contacted with the solution comprising chlorine dioxide, ethanol, and water at a temperature of from about 60°

C. to about 80°

C. for a time of at least about 2 hours.

8. The process of claim 1 wherein the mixture in step (b) is heated at a temperature of at least about 180°

C. for at least about 5 minutes.

9. The process of claim 1 wherein the mixture in step (b) is heated at a temperature of at least about 180°

C. for at least about 30 minutes.

10. The process of claim 1 which further comprises separating the second solid portion comprising lignin or a derivative thereof from the solid first portion.

11. The process of claim 1 wherein the portions are separated by precipitating the second solid portion comprising lignin or a derivative thereof and recovering the lignin by filtration.

12. The process of claim 1 wherein the amount of ethanol is from about 40 to about 80 weight percent based on the total amount of ethanol and water.

13. The process of claim 1 wherein the ratio of feedstock to solution comprising chlorine dioxide, ethanol, and water is from about 1:

3 to about 1;

10.

14. The process of claim 1 wherein the conditions under which the feedstock is contacted with a solution comprising chlorine dioxide, ethanol, and water are sufficient to reduce the pH at least 1 unit prior to step (b).

15. The process of claim 1 wherein the lignocellulosic feedstock has an average particle size of less than about 25 mm in its smallest dimension.

16. The process of claim 1 wherein the lignocellulosic feedstock has an average particle size of less than about 10 mm in its smallest dimension.

17. A composition comprising a lignocellulosic feedstock and a solution comprising chlorine dioxide, ethanol, and water wherein the composition is characterized by (1) a ratio of feedstock to solution comprising chlorine dioxide and water of from about 1:

3 to about 1;

10; and

(2) an amount of chlorine dioxide of from about 0.5% to about 5% by weight based on the total dry weight of dry feedstock.

18. The composition of claim 17 wherein the ethanol comprises from about 50 to about 70 percent by weight based on the total amount of ethanol and water.

19. The composition of claim 17 wherein the composition is characterized by (1) a ratio of feedstock to solution comprising chlorine dioxide and water of from about 1:

3 to about 1;

10; and

(2) an amount of chlorine dioxide of from about 0.8% to about 1.5% by weight based on the total dry weight of dry feedstock.

20. A process for treating a lignocellulosic feedstock wherein the process comprises:

(a) contacting the feedstock with a solution comprising chlorine dioxide, ethanol, and water to form a mixture, wherein the ratio of feedstock to solution comprising chlorine dioxide, ethanol, and water is from about 1;

3 to about 1;

10, wherein the amount of ethanol is from about 40 to about 80 weight percent based on the total amount of ethanol and water, and wherein the amount of chlorine dioxide is from about 0.5% to about 8% by weight based on the total dry weight of feedstock;

(b) heating the mixture at a temperature of at least about 180°

C. for at least about 5 minutes to produce a composition mixture comprising (1) a first solid portion comprising cellulose which is suitable for enzymatic hydrolysis, (2) a second solid portion comprising lignin or a derivative thereof, and (3) a solution comprising hemicellulose;

(c) separating the second solid portion comprising lignin or a derivative thereof from the solid first portion;

(d) enzymatically hydrolyzing at least part of the solid first portion to form a composition comprising glucose; and

(e) fermenting the composition comprising glucose.