Process comprising sulfur dioxide and/or sulfurous acid pretreatment and enzymatic hydrolysis

• US 9,574,212 B2
• Filed: 06/30/2016
• Issued: 02/21/2017
• Est. Priority Date: 03/16/2015
• Status: Active Grant

• Current Assignee: Iogen Corporation
• Original Assignee: Iogen Corporation
• Inventors: Foody, Brian, Tolan, Jeffrey S., MacDonald, Daniel, Foody, Patrick J.
• Primary Examiner(s): Ware, Debbie K
• Application Number:
  US15/199,638
• Publication Number:
  US 20160312249A1
• Time in Patent Office: 236 Days
• US Class Current: 1/1
• CPC Class Codes: B01D 2251/60 Inorganic bases or salts
• CPC Class Codes: B01D 2252/10 Inorganic absorbents chemical reactants B01D2251/00
• CPC Class Codes: B01D 2252/102 Ammonia
• CPC Class Codes: B01D 2257/302 Sulfur oxides
• CPC Class Codes: B01D 53/002 by condensation
• CPC Class Codes: B01D 53/1481 Removing sulfur dioxide or sulfur trioxide
• CPC Class Codes: B01D 53/501 by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
• CPC Class Codes: C12M 45/03 by control of the humidity or content of liquids; Drying
• CPC Class Codes: C12M 45/09 by enzymatic treatment
• CPC Class Codes: C12M 45/20 Heating; Cooling heating or cooling apparatus for laboratory uses B01L7/00
• 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 ethanol C12P7/10
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: C12P 7/14 Multiple stages of fermentation; Multiple types of microorganisms or re-use of microorganisms
• CPC Class Codes: C12Y 302/01004 Cellulase (3.2.1.4), i.e. endo-1,4-beta-glucanase
• CPC Class Codes: D21C 1/02 with water or steam
• CPC Class Codes: D21C 1/04 with acid reacting compounds
• CPC Class Codes: D21C 3/06 sulfur dioxide; sulfurous acid; bisulfites sulfites
• CPC Class Codes: Y02E 50/10 : Biofuels, e.g. bio-diesel

Abstract

The disclosure provides a process for producing a fermentation product from a lignocellulosic feedstock. The process describes soaking a lignocellulosic feedstock in an aqueous solution to produce a soaked feedstock. The soaked feedstock is at least partially dewatered and the at least partially dewatered feedstock is subjected to pretreating in the presence of sulfur dioxide, sulfurous acid or a combination thereof to produce a pretreated feedstock composition. The pretreated feedstock composition is fed to an enzymatic hydrolysis in which the concentration of dissolved solids fed to the enzymatic hydrolysis is at least 50% (w/w) of the concentration of dissolved solids in the pretreated feedstock composition. The cellulose in the pretreated feedstock composition is hydrolyzed with cellulase enzymes in the presence of the dissolved solids to produce glucose. The glucose is fermented to produce the fermentation product.

Claims

1. A process for producing a fermentation product from a lignocellulosic feedstock comprising:

(i) soaking the lignocellulosic feedstock in a liquid comprising water to produce a soaked feedstock;

(ii) at least partially dewatering the soaked feedstock to produce an at least partially dewatered feedstock;

(iii) feeding the at least partially dewatered feedstock to a heating device;

(iv) adding steam and acid to the heating device, said steam heating the at least partially dewatered feedstock to a first temperature to provide a heated feedstock, said acid comprising at least one of sulfur dioxide and sulfurous acid;

(v) pretreating the heated feedstock in the presence of the acid in a pretreatment reactor to produce a pretreated feedstock, said pretreatment reactor disposed downstream of said heating device;

(vi) hydrolyzing cellulose in the pretreated feedstock with cellulase enzymes to produce glucose, wherein the concentration of dissolved solids in the pretreated feedstock fed to the hydrolysis is at least about 50% of the concentration of dissolved solids in the pretreated feedstock produced in step (v); and

(vii) fermenting the glucose to produce the fermentation product.

2. The process of claim 1, wherein the liquid comprises at least one of sulfur dioxide and sulfurous acid.

3. The process of claim 1, wherein the fermentation product is ethanol.

4. The process of claim 1, wherein the step of at least partially dewatering is conducted with a screw press.

5. The process of claim 1, comprising adding an inorganic alkali to the lignocellulosic feedstock subsequent to the pretreating and prior to the hydrolyzing to increase the pH of the pretreated feedstock, wherein the inorganic alkali comprises at least one of calcium hydroxide, ammonia, calcium carbonate, or potassium carbonate.

6. The process of claim 1, wherein the lignocellulosic feedstock comprises at least one of an agricultural residue, a biomass or energy crop, bagasse, sugar cane tops, or sugar cane leaves.

7. The process of claim 1, wherein the first temperature is between 170°

C. and 230°

C., and wherein the pretreating is conducted at about the first temperature.

8. The process of claim 1, wherein the pretreating is conducted at a pH less than 2.5.

9. The process of claim 1, wherein the pretreatment reactor has a residence time between 30 seconds and 30 minutes.

10. The process of claim 9, wherein the heating device has a residence time that is less than 1 minute.

11. The process of claim 1, wherein the heating device has a residence time that is about a time required to heat the at least partially dewatered feedstock in the heating device to a temperature that the pretreating is conducted at.

12. The process of claim 1, wherein the heating device has a residence time selected to minimize hydrolysis of hemicellulose in the at least partially dewatered feedstock within the heating device.

13. The process of claim 1, wherein the concentration of dissolved solids in the pretreated feedstock (w/w) fed to enzymatic hydrolysis is at least 55% of the concentration of dissolved solids (w/w) in the pretreated feedstock produced in step (vi).

14. The process of claim 1, wherein between the steps of soaking and hydrolyzing, the undissolved solids content of the lignocellulosic feedstock is between 15 wt % and 40 wt %.

15. The process of claim 1, wherein there is no solids-liquid separation between the steps of pretreating and hydrolyzing.

16. The process of claim 1, wherein the cellulose in the pretreated feedstock is substantially unwashed.

17. The process of claim 1, wherein the cellulose in the pretreated feedstock is substantially undiluted prior to hydrolyzing.

18. The process of claim 1, wherein the sulfur dioxide, sulfurous acid, or a combination thereof, are added to the lignocellulosic feedstock to provide an equivalent sulfur dioxide loading greater than about 10 wt %.

19. A process for producing a fermentation product from a lignocellulosic feedstock comprising:

(i) feeding the lignocellulosic feedstock to at least one soaking tank, wherein the lignocellulosic feedstock is soaked in a liquid comprising water to produce a soaked feedstock;

(ii) feeding the soaked feedstock to a dewatering device, wherein the soaked feedstock is at least partially dewatered to produce an at least partially dewatered feedstock having a consistency between 15 wt % and 40 wt %;

(iii) feeding the at least partially dewatered feedstock to a heating device, wherein the at least partially dewatered feedstock is fluffed-up as it is conveyed therethrough, and wherein steam and acid are added to the at least partially dewatered feedstock to produce an acidified feedstock having a pH between 0.5 and 2.5, said acid comprising at least one of sulfur dioxide and sulfurous acid, a residence time of the heating device less than 1 minute;

(iv) feeding the acidified feedstock to at least one pretreatment reactor disposed downstream of the heating device, wherein the acidified feedstock resides for a time between 30 seconds and 30 minutes at a temperature between 170°

C. and 230°

C. to produce a pretreated feedstock;

(v) feeding the pretreated feedstock to at least one hydrolysis tank, wherein cellulose in the pretreated feedstock is hydrolyzed with cellulase to produce glucose, a concentration of dissolved solids in the pretreated feedstock fed to the hydrolysis at least about 50% of a concentration of dissolved solids in the pretreated feedstock produced in step (iv); and

(vi) feeding a stream comprising the glucose to at least one fermentation tank, wherein the glucose is fermented to produce the fermentation product.

20. A system for producing a fermentation product from a lignocellulosic feedstock comprising:

at least one tank for soaking the lignocellulosic feedstock in at least one of water and an aqueous solution;

a dewatering device disposed downstream of the at least one tank for at least partially dewatering the soaked feedstock to produce an at least partially dewatered feedstock;

a heating device disposed downstream of the dewatering device for fluffing up the at least partially dewatered feedstock, said heating device having at least one inlet for introducing steam and an acid to the at least partially dewatered feedstock, said acid comprising at least one of sulfur dioxide and sulfurous acid;

at least one pretreatment reactor disposed downstream of the heating device, said at least one pretreatment reactor including at least one outlet for discharging a pretreated feedstock;

at least one hydrolysis tank disposed downstream of said at least one outlet for hydrolyzing cellulose in the pretreated feedstock with cellulase enzymes to produce glucose;

at least one system disposed between the at least one outlet and the at least one hydrolysis tank, said at least one system including at least one of a cooling system, a pH adjustment system, a solid liquid separator, a washing system, and a dilution system, said at least one system feeding the pretreated feedstock to the at least one hydrolysis tank such that a concentration of dissolved solids in the pretreated feedstock fed to the hydrolysis is at least about 50% of the concentration of dissolved solids in the pretreated feedstock produced by the at least one pretreatment reactor; and

at least one fermentation tank disposed downstream of the at least one pretreatment reactor for fermenting the glucose to produce the fermentation product.