IP Library Granted Patent US 11,118,197
Granted Patent B2
US 11,118,197 · App. 15/777,649 · Granted Sep 14, 2021

High gravity, fed-batch ionic liquid based process for deconstructing biomass

Inventors: Feng Xu (Albany, CA); Blake Simmons (San Francisco, CA); Seema Singh (Clarksburg, MD)
Assignee: National Technology & Engineering Solutions of Sandia, LLC
C12P7/10C12P19/02C12P19/14C13K1/02C13K13/002C12P2201/00C12P2203/00Y02E50/10
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Quick Facts
Patent No.
US 11,118,197
App. No.
15/777,649
Granted
Sep 14, 2021
Kind
B2
Abstract

In one aspect, the present invention provides methods for preparing a fermentation product. The methods include pre-treating a mixture of biomass and ionic liquid, wherein the ionic liquid comprises a choline cation and the biomass comprises polysaccharide and lignin. The methods further include forming hydrolysates from the introduction of glycoside hydrolase to the pre-treated mixture at conditions sufficient to produce a sugar composition mixture for fermentation steps. The present invention provides methods for loading biomass mixtures in a batch-fed process, wherein the biomass slurries can be loaded into water or a concentrated sugar composition for hydrolysate production. The methods can be performed in a one-pot process, wherein the ionic liquids are present in the mixtures throughout each step. Aspects of the invention provide compositions of sugar composition mixtures and fermentation product mixtures.

Claims (35)

1. A method for producing a fermentation product from biomass, wherein the biomass comprises polysaccharide and lignin, the method comprising:

(i) providing a pre-treatment mixture comprising the biomass at a concentration of at least about 5% w/w and less than about 50% w/w, an ionic liquid at a concentration of between about 5% w/w and about 25% w/w, and water, wherein the ionic liquid and biomass are present in the pre-treatment mixture at a mass ratio R m/i of from about 0.2 to about 5, and wherein the ionic liquid is selected from the group consisting of cholinium lysinate, cholinium aspartate, and a combination thereof;

(ii) maintaining the mixture under pre-treatment conditions sufficient to dissolve at least a portion of the polysaccharide present in the biomass, wherein the pre-treatment conditions comprise a temperature of at least about 100° C. and less than about 200° C. for a duration of at least about 0.5 h, thereby forming a pre-treated biomass slurry;

(iiia) combining a portion of the pre-treated biomass slurry with a glycoside hydrolase and a hydrolysate seed batch comprising a sugar and water, wherein the sugar is at a concentration of at least 70% w/w in the hydrolysate seed batch:

(iiib) maintaining the mixture formed in step (iiia) under conditions sufficient to hydrolyze at least a portion of the polysaccharide present in the pre-treated biomass slurry, thereby forming a mixture comprising hydrolyzed polysaccharide;

(iiic) adding to the mixture formed in step (iiib) an additional portion of the pretreated biomass slurry and maintaining the mixture under conditions sufficient to hydrolyze the polysaccharide present in the additional portion of the pre-treated biomass slurry;

(iiid) repeating step (iiic) 1 to 100 times; and

(iv) fermenting the mixture formed in step (iiid) with a fermentation microorganism under conditions suitable to produce the fermentation product,

wherein at least 70% of glucan and/or xylan present in the biomass is converted into the fermentation product.

2. The method of claim 1 , wherein the pre-treatment mixture comprises the biomass at a concentration of at least about 10% w/w and less than about 35% w/w.

3. The method of claim 1 , wherein the pre-treatment mixture comprises the biomass at a concentration of at least about 30% w/w and less than about 50% w/w.

4. The method of claim 1 , wherein the pre-treatment mixture comprises the ionic liquid or mixture of ionic liquids at a concentration of at least about 10% w/w and less than about 20% w/w.

5. The method of claim 1 , wherein the pre-treatment mixture comprises the biomass and the ionic liquid at a mass ratio R m/i of from about 0.5 to about 4.

6. The method of claim 1 , wherein step (ii) is performed for about 1-3 hours.

7. The method of claim 1 , wherein the glycoside hydrolase in step (iiia) is:

i) a cellulase, hemicellulase, pectinase, xylanase, galactanase, mannanase, or β-glucosidase;

ii) one or more, or all, enzymes selected from the group consisting of cellulase, hemicellulase, pectinase, xylanase, galactanase, mannanase, and β-glucosidase; or

iii) a mixture comprising one or more, or all, enzymes selected from the group consisting of cellulase, hemicellulase, pectinase, xylanase, galactanase, mannanase, and β-glucosidase.

8. The method of claim 1 , wherein step (iii) comprises a temperature of between about 25° C. and about 60° C. and a pH of from about 4 to about 6.

9. The method of claim 1 , wherein the fermentation product is selected from the group consisting of methanol, ethanol, isopropanol, butanol, isopentenol and bisabolene.

10. The method of claim 1 , wherein any combination of the steps of (i)-(iv) are performed in the same reaction chamber.

11. The method of claim 1 , wherein step (iii) and/or step (iv) comprises more than 50%, 90%, 95% or 99% of the ionic liquid in the mixtures of steps (i)-(ii).

12. A method of producing a polysaccharide hydrolysate from biomass, wherein the biomass comprises polysaccharide and lignin, the method comprising:

(i) providing a slurry comprising pre-treated biomass at a concentration of at least about 5% w/w and less than about 50% w/w, an ionic liquid or mixture of ionic liquids at a concentration of between about 5% w/w and about 25% w/w, and water, wherein the ionic liquid and biomass are present in the pre-treated slurry at a mass ratio R m/i of from about 0.2 to about 5, and wherein the ionic liquid is selected from the group consisting of cholinium lysinate, cholinium aspartate, and a combination thereof;

(ii) combining a portion of the pre-treated biomass slurry with a glycoside hydrolase and a hydrolysate seed batch comprising a sugar and water, wherein the sugar is at a concentration of at least 70% w/w in the hydrolysate seed batch;

(iii) maintaining the mixture formed in step (ii) under conditions sufficient to hydrolyze the polysaccharide present in the portion of the pre-treated biomass slurry, thereby forming a mixture comprising a hydrolyzed polysaccharide;

(iv) adding to the mixture formed in step (iii) an additional portion of the pre-treated biomass slurry of step (i), and maintaining the mixture under conditions sufficient to hydrolyze the polysaccharide present in the additional portion of the pre-treated biomass slurry; and

(v) repeating the step of (iv) 1 to 100 times,

wherein at least 70% of glucan and/or xylan present in the biomass is converted into a monosaccharide.

13. The method of claim 1 , wherein the conditions sufficient to hydrolyze at least a portion of the polysaccharide present in the pre-treated biomass slurry of step (iii) are maintained for at least 2 days.

14. The method of claim 12 , wherein the portion of the pretreated biomass slurry of step (ii) is introduced at a rate of from at least 2 grams per day to about 20 grams per day per 30 milliliters of the mixture comprising the glycoside hydrolase and hydrolysate seed batch.

15. The method of claim 12 , wherein the additional portion of the pre-treated biomass slurry of step (iv) is added at a rate of from at least 2 grams per day to about 20 grams per day per 30 milliliters of the mixture formed in step (iii).

16. The method of claim 15 , wherein the addition of the portion of the pre-treated biomass slurry of step (iv) is repeated for at least 4 days.

17. The method of claim 12 , wherein the mixture of step (iii) is maintained under conditions sufficient to hydrolyze the polysaccharide for at least 1 day, or at least 2 days.

18. The method of claim 12 , wherein the mixture of step (iv) is maintained under conditions sufficient to hydrolyze the polysaccharide for at least 1 day, or at least 2 days.

Assignments (2)
CONFIRMATORY LICENSE Recorded May 1, 2020
From: UNIVERSITY OF CALIF-LAWRENC BERKELEY LAB
To: UNITED STATES DEPARTMENT OF ENERGY
Reel/Frame 052545/0763 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 21, 2018
From: XU, FENG; SIMMONS, BLAKE; SINGH, SEEMA
To: NATIONAL TECHNOLOGY & ENGINEERING SOLUTIONS OF SANDIA, LLC
Reel/Frame 046938/0370 →
Continuity (2)
Provisional Application 62257647 · Nov 19, 2015
Related Publication 20180346938A1 · Dec 6, 2018
Cited By (1)
US 12,305,213