Method for mixed biomass hydrolysis

• US 9,200,337 B2
• Filed: 04/22/2014
• Issued: 12/01/2015
• Est. Priority Date: 04/22/2014
• Status: Active Grant

• Current Assignee: Renmatix, Inc.
• Original Assignee: Renmatix, Inc.
• Inventors: Colakyan, Manuk, Jara-Moreno, Rory Hernan
• Primary Examiner(s): Mayes, Melvin C
• Assistant Examiner(s): CALL, DOUGLAS BRYANT
• Application Number:
  US14/258,362
• Publication Number:
  US 20150299816A1
• Time in Patent Office: 588 Days
• Field of Search: None
• US Class Current: 1/1
• CPC Class Codes: C13K 13/002 Xylose

Abstract

Methods and systems are disclosed for the hydrolysis of mixed biomass. The methods include forming a mixture of at least two modified biomass feedstocks to achieve various benefits, such as maximizing sugar yields and minimizing the formation of degradation products.

Claims

1. A hydrolysis method comprising:

(1) providing at least two modified biomass feedstocks comprising;

(a) from greater than 0 wt % to less than 100 wt % of a first modified biomass feedstock exhibiting a maximum hydrolysis yield at time X, when subjected to a first condition; and

(b) from greater than 0 wt % to less than 100 wt % of a second modified biomass feedstock exhibiting a maximum hydrolysis yield at time Y, when subjected to the first condition;

wherein;

the second modified biomass feedstock is different from the first modified biomass feedstock;

time X is less than or equal to time Y;

and time X and time Y differ by less than or equal to about 100% of time X; and

(2) subjecting a mixture of the first modified biomass feedstock and the second modified biomass feedstock to the first condition to achieve a maximum hydrolysis yield at time Z, wherein time Z is less than time Y;

wherein;

the hydrolysis method is performed at a pH of at least 1.3; and

all weight percent values are on a dry basis and are based on the total weight of the at least two modified biomass feedstocks.

2. The method of claim 1, wherein the second modified biomass feedstock is different from the first modified biomass feedstock by a difference selected from the group consisting of compositional proportions, biomass type, biomass species, hemicellulose structure, geographical harvesting location, harvesting season, and any combination thereof.

3. The method of claim 2, wherein the difference is biomass type, and the biomass type of the first and second modified biomass feedstocks is independently selected from the group consisting of a softwood biomass, a hardwood biomass, a tropical wood biomass, an annual fiber biomass, a non-woody biomass, municipal solid waste, and any combination thereof.

4. The method of claim 1, wherein the hydrolysis method is performed at a pH of at least about 2.

5. The method of claim 1, wherein

(a) the first modified biomass feedstock is prepared by a first treatment;

and

(b) the second modified biomass feedstock is prepared by a second treatment;

wherein the first and second treatments independently are selected from the group consisting of size reduction, steam explosion, ammonia explosion, enzymatic treatment, acid treatment, base treatment, hydrothermal treatment, biological treatment, catalytic treatment, non-catalytic treatment, and any combination thereof; and

wherein the first treatment is the same or different than the second treatment.

6. The method of claim 5, wherein at least one of the first and the second treatments is size reduction, and wherein the average equivalent spherical diameter of at least one of the first and second modified biomass feedstocks is less than about 50 mm.

7. The method of claim 5, wherein both the first treatment and the second treatment are size reduction, the second modified biomass feedstock has a particle size of less than about 50 mm, and the average equivalent spherical diameter of the second modified biomass feedstock is smaller than the average equivalent spherical diameter of the first modified biomass feedstock.

8. The method of claim 5, wherein the first and the second treatment are size reduction, and wherein the second modified biomass feedstock has an average equivalent spherical diameter of less than about 80% of an average equivalent spherical diameter of the first modified biomass feedstock.

9. The method of claim 1, wherein the first modified biomass feedstock and the second modified biomass feedstock are in the mixture in a weight ratio of from about 1:

25 to about 25;

1.

10. The method of claim 1, wherein the first condition is hot water extraction, acidic hot water extraction, sub-critical fluid extraction, near-critical fluid extraction, supercritical fluid extraction, enzymatic treatment, or any combination.

11. The method of claim 10, wherein the first condition is hot water extraction.

12. The method of claim 11, wherein the hot water extraction is performed at a temperature of about 120°

C. to about 260°

C.

13. The method of claim 11, wherein the hot water extraction employs hot water, and the hot water extraction is performed at a pressure sufficient to maintain all of the hot water in liquid form.

14. The method of claim 1, wherein time Z is less than about 90% of time Y.

15. The method of claim 1, wherein the maximum hydrolysis yield at time Z achieved in the subjecting the mixture to the first condition is higher than an average of the maximum hydrolysis yields at times X and Y.

16. The method of claim 15, wherein the maximum hydrolysis yield at time Z achieved in the subjecting the mixture to the first condition is at least about 5% higher than the average of the maximum hydrolysis yields at times X and Y.

17. The method of claim 1, wherein time Z is less than an average of time X and time Y.

18. The method of claim 1, wherein a first degradation yield of a degradation product at time Z achieved in the subjecting the mixture to the first condition is lower than at least one of (1) a second degradation yield of the degradation product of the first modified biomass feedstock at time X, when subjected to the first condition, and (2) a third degradation yield of the degradation product of the second modified biomass feedstock at time Y, when subjected to the first condition.

19. The method of claim 18, wherein the degradation product is furfural.

20. The method of claim 1, further comprising:

preparing the first modified biomass feedstock with a first treatment; and

preparing the second modified biomass feedstock with a second treatment;

wherein the first and second treatments independently are selected from the group consisting of size reduction, steam explosion, ammonia explosion, enzymatic treatment, acid treatment, base treatment, hydrothermal treatment, biological treatment, catalytic treatment, non-catalytic treatment, and any combination thereof; and

wherein the first treatment is the same or different than the second treatment.