Pretreatment of lignocellulosic biomass with sulfur dioxide and/or sulfurous acid

• US 10,655,149 B2
• Filed: 09/16/2016
• Issued: 05/19/2020
• Est. Priority Date: 02/10/2016
• Status: Active Grant

• Current Assignee: Iogen Corporation
• Original Assignee: Iogen Corporation
• Inventors: Dechman, John, Foody, Brian
• Primary Examiner(s): Underdahl, Thane
• Application Number:
  US16/076,457
• Publication Number:
  US 20190194697A1
• Time in Patent Office: 1,341 Days
• Field of Search: None
• CPC Class Codes: C10L 1/02 essentially based on components consisting of carbon, hydrogen, and oxygen only
• 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 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: C12Y 302/01004 Cellulase (3.2.1.4), i.e. endo-1,4-beta-glucanase
• 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

A process for hydrolyzing lignocellulosic biomass includes feeding lignocellulosic biomass into a pretreatment reactor, wherein the pretreatment reactor has a headspace charged with sulfur dioxide previously used in the pretreatment of lignocellulosic biomass. In addition, acid comprising sulfur dioxide and/or sulfurous acid is fed into the pretreatment reactor (e.g., with the lignocellulosic biomass, separate from the lignocellulosic biomass, or a combination thereof) and the lignocellulosic biomass is heated. As the pretreated lignocellulosic biomass is discharged from the pretreatment reactor, at least a portion of the sulfur dioxide used in the pretreatment is retained in the headspace.

Claims

1. A process for hydrolyzing lignocellulosic biomass comprising:

a) feeding lignocellulosic biomass and acid into a pretreatment reactor, said acid comprising at least one of sulfur dioxide and sulfurous acid;

b) heating said lignocellulosic biomass in the pretreatment reactor for a time and at a temperature sufficient to provide a slurry comprising pretreated lignocellulosic biomass, said slurry adjacent a headspace comprising sulfur dioxide;

c) removing said slurry from the pretreatment reactor;

d) preventing at least a portion of the sulfur dioxide in the headspace from exiting the pretreatment reactor as the slurry is removed;

e) hydrolyzing cellulose in the removed slurry in the presence of cellulase to produce glucose; and

f) contacting additional lignocellulosic biomass with the sulfur dioxide prevented from exiting the pretreatment reactor in step d) under conditions selected to pretreat the additional lignocellulosic biomass.

2. The process according to claim 1, wherein an amount of acid fed into the pretreatment reactor in step a) is determined in dependence upon an amount of sulfur dioxide retained in the headspace.

3. The process according to claim 1, comprising monitoring a partial pressure of sulfur dioxide in the headspace.

4. The process according to claim 3, wherein adding acid in step a) comprises injecting sulfur dioxide into the pretreatment reactor at a rate selected in dependence upon the monitored partial pressure.

5. The process according to claim 1, wherein the pretreatment reactor is a batch pretreatment reactor, wherein the sulfur dioxide is retained within a vapour reservoir chamber, and wherein step d) comprises:

closing a valve to the vapour reservoir chamber to trap a portion of the sulfur dioxide therein; and

discharging the slurry from the pretreatment reactor with the valve closed.

6. The process according to claim 1, wherein the pretreatment reactor is a continuous mode pretreatment reactor, and wherein step d) comprises maintaining a liquid seal between the headspace and a discharge of the pretreatment reactor, said liquid seal comprising the slurry.

7. The process according to claim 1, wherein the amount of acid fed into the pretreatment reactor in step a) is selected to provide an equivalent sulfur dioxide loading that is at least 1% weight sulfur dioxide on weight of dry lignocellulosic biomass.

8. The process according to claim 1, wherein feeding lignocellulosic biomass and acid into a pretreatment reactor comprises feeding acid impregnated lignocellulosic biomass into the pretreatment reactor.

9. The process according to claim 1, wherein the time is between about 1 minute and about 30 minutes.

10. The process according to claim 1, wherein the temperature is between about 170°

C. and about 240°

C.

11. The process according to claim 1, wherein a volume of the headspace is greater than about 20% of a volume of the pretreatment reactor.

12. The process according to claim 1, wherein a volume of the headspace is greater than about 50% of a volume of the pretreatment reactor.

13. The process according to claim 1, wherein a volume of the headspace is greater than about 70% of a volume of the pretreatment reactor.

14. The process according to claim 1, wherein the lignocellulosic biomass has a consistency at an inlet of the pretreatment reactor that is greater than about 15 wt %.

15. The process according to claim 1, wherein heating said lignocellulosic biomass in step b) comprises injecting steam into the pretreatment reactor.

16. The process according to claim 15, wherein feeding acid into the pretreatment reactor in step a) comprises injecting sulfur dioxide into the pretreatment reactor.

17. The process according to claim 16, wherein the sulfur dioxide is injected with the steam.

18. A process for pretreating lignocellulosic biomass comprising:

a) feeding acid and lignocellulosic biomass into a pretreatment reactor, said acid comprising at least one of sulfur dioxide and sulfurous acid, said acid added to the pretreatment reactor with the lignocellulosic biomass, separate from the lignocellulosic biomass, or a combination thereof;

b) adding heat to the pretreatment reactor such that said lignocellulosic biomass and acid are heated for a time and at a temperature sufficient to provide a slurry comprising pretreated lignocellulosic biomass, said slurry disposed within the pretreatment reactor adjacent a headspace, said headspace comprising sulfur dioxide;

c) removing the slurry from the pretreatment reactor;

d) reserving at least a portion of the sulfur dioxide in the headspace within at least one of the pretreatment reactor and a reservoir connected to the pretreatment reactor as the slurry is removed from the pretreatment reactor; and

e) pretreating additional lignocellulosic biomass in the presence of the reserved sulfur dioxide.

19. The process according to claim 18, wherein the pretreatment reactor is a batch pretreatment reactor, and wherein step d) comprises sealing sulfur dioxide within the reservoir as the slurry is being removed.

20. The process according to claim 18, wherein the pretreatment reactor is a continuous pretreatment reactor, and wherein step d) comprises maintaining a liquid seal between the headspace and a slurry discharge valve.

21. A process for hydrolyzing lignocellulosic biomass comprising:

a) feeding lignocellulosic biomass and acid into a pretreatment reactor, said acid comprising at least one of sulfur dioxide and sulfurous acid;

b) heating said lignocellulosic biomass in the pretreatment reactor for a time and at a temperature sufficient to provide a slurry comprising pretreated lignocellulosic biomass, said slurry adjacent a headspace comprising sulfur dioxide;

c) removing at least a portion of said slurry from the pretreatment reactor;

d) preventing at least a portion of the sulfur dioxide in the headspace from exiting the pretreatment reactor as the at least a portion of the slurry is removed such that a concentration of sulfur dioxide in at least a region of the headspace of the pretreatment reactor is substantially maintained while the slurry is removed;

e) hydrolyzing cellulose in the removed slurry in the presence of cellulase to produce glucose; and

f) selecting an amount of make-up sulfur dioxide to be added to the pretreatment reactor in dependence upon an amount of sulfur dioxide prevented from exiting the pretreatment reactor.