Sulfur dioxide and/or sulfurous acid pretreatment

• US 10,662,455 B2
• Filed: 09/16/2016
• Issued: 05/26/2020
• Est. Priority Date: 12/18/2015
• Status: Active Grant

• Current Assignee: Iogen Corporation
• Original Assignee: Iogen Corporation
• Inventors: Tolan, Jeffrey S., MacDonald, Daniel G., Martens, Kristin, Leduc, Natacha, Foody, Brian
• Primary Examiner(s): Ware, Deborah K
• Application Number:
  US16/061,254
• Publication Number:
  US 20180363017A1
• Time in Patent Office: 1,348 Days
• CPC Class Codes: B01D 3/06 Flash distillation
• CPC Class Codes: C12M 45/06 by chemical means or hydrolysis
• CPC Class Codes: C12M 45/09 by enzymatic treatment
• 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 7/10 substrate containing cellulosic material
• CPC Class Codes: C13K 1/02 obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: C13K 13/002 Xylose
• CPC Class Codes: D21C 1/04 with acid reacting compounds
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

A process for producing alcohol from lignocellulosic biomass includes adding at least one of sulfur dioxide and sulfurous acid to the lignocellulosic biomass to provide an effective sulfur dioxide dosage and/or effective sulfur dioxide slurry concentration, each of which is calculated using the ratio of the volume of the slurry in the pretreatment reactor to the total volume of the pretreatment reactor, within a predetermined range.

Claims

1. A method for pretreating and hydrolyzing lignocellulosic biomass comprising:

a) adding acid to the lignocellulosic biomass to produce acidified lignocellulosic biomass, said acid comprising at least one of sulfur dioxide and sulfurous acid;

b) pretreating the acidified lignocellulosic biomass in at least one pretreatment reactor to provide a pretreated slurry having a pH less than 1.5, said pretreated slurry comprising cellulose, said acidified lignocellulosic biomass having a consistency between 14.5 wt % and 51 wt %, said at least one pretreatment reactor comprising a first pretreatment reactor, said pretreating conducted at a temperature greater than 170°

C. and under pretreating conditions wherein a product of sulfur dioxide dosage and V_s/V_r is greater than 0.8 wt %, where V_s/V_r is a ratio of slurry volume to reactor volume and where sulfur dioxide dosage is a ratio of grams of sulfur dioxide present in the first pretreatment reactor to grams of dry lignocellulosic biomass present in the first pretreatment reactor expressed as a weight percentage; and

c) hydrolyzing the cellulose from the pretreated slurry with an enzyme to produce glucose.

2. The method according to claim 1, comprising reducing a pressure on the pretreated slurry to produce a flash stream and a cooled pretreated slurry.

3. The method according to claim 2, comprising recovering the acid from at least one of the flash stream and a stream derived from the flash stream.

4. The method according to claim 3, comprising recycling the recovered acid back into the at least one pretreatment reactor.

5. The method according to claim 1, wherein said acid is added to the lignocellulosic biomass in an amount sufficient to provide a sulfur dioxide dosage of at least 6 wt %.

6. The method according to claim 1, wherein said acid is added to the lignocellulosic biomass in an amount sufficient to provide a sulfur dioxide dosage of at least 15 wt %.

7. The method according to claim 1, wherein said acid is added to the lignocellulosic biomass in an amount sufficient to provide a sulfur dioxide dosage of at least 20 wt %.

8. The method according to claim 1, wherein step a) includes adding sulfur dioxide to the lignocellulosic biomass upstream of the first pretreatment reactor, to the first pretreatment reactor, or a combination thereof.

9. The method according to claim 1, wherein the enzyme comprises cellulase at a dosage of less than about 12 milligrams protein per gram of cellulose.

10. The method according to claim 1, wherein adding acid to the lignocellulosic biomass comprises adding an amount of sulfur dioxide sufficient to provide a pretreated slurry having a pH less than 1.25.

11. The method according to claim 3, wherein recovering the acid comprises collecting gaseous sulfur dioxide from the flash stream.

12. The method according to claim 1, wherein V_s/V_r is less than 0.60.

13. The method according to claim 1, wherein V_s/V_r is between 0.10 and 0.40.

14. The method according to claim 1, wherein the effective sulfur dioxide slurry concentration in the first pretreatment reactor is between 0.25 wt % and 1.5 wt %, said effective sulfur dioxide slurry concentration calculated from the product of the sulfur dioxide slurry concentration and V_s/V_r, said sulfur dioxide slurry concentration calculated from the ratio of grams of sulfur dioxide present to grams of moisture present expressed as a weight percentage.

15. The method according to claim 1, wherein the product of sulfur dioxide dosage and V_s/V_r is greater than 1 wt %.

16. The method according to claim 1, wherein the product of sulfur dioxide dosage and V_s/V_r is greater than 2 wt %.

17. The method according to claim 1, wherein the lignocellulosic biomass comprises a non-woody lignocellulosic biomass.

18. The method according to claim 1, wherein a residence time of the acidified lignocellulosic biomass in the first pretreatment reactor is between 30 seconds and 8 minutes, and wherein the first pretreatment reactor is held at a temperature between 180°

C. and 240°

C. for the residence time.

19. The method according to claim 1, wherein said pretreating comprises conducting a sulfur dioxide catalyzed steam explosion pretreatment.

20. A method for pretreating and hydrolyzing lignocellulosic biomass comprising:

a) adding acid to the lignocellulosic biomass to produce acidified lignocellulosic biomass, said acid comprising at least one of sulfur dioxide and sulfurous acid;

b) pretreating the acidified lignocellulosic biomass in at least one pretreatment reactor to provide a pretreated slurry, said pretreated slurry comprising cellulose and having a pH that is less than 1.55, said acidified lignocellulosic biomass having a consistency that is greater than 14.5 wt % and less than 50.5 wt %, said at least one pretreatment reactor comprising a first pretreatment reactor having a reactor volume V_r and a slurry volume V_s; and

c) hydrolyzing the cellulose with an enzyme to produce glucose,

wherein adding the acid to the lignocellulosic biomass comprises adding an amount of the acid that provides an effective sulfur dioxide dosage that is greater than 1 wt % and an effective sulfur dioxide slurry concentration that is between 0.25 wt % and 1.5 wt %, said effective sulfur dioxide slurry concentration calculated from the product of the sulfur dioxide slurry concentration in the first pretreatment reactor and V_s/V_r, said sulfur dioxide slurry concentration calculated from the ratio of grams of sulfur dioxide present to grams of moisture present expressed as a weight percentage, said effective sulfur dioxide dosage calculated from the product of sulfur dioxide dosage in the first pretreatment reactor and V_s/V_r,

and wherein said pretreating is conducted at a temperature greater than 170°

C.

21. The method according to claim 20, wherein the effective sulfur dioxide dosage is greater than 1.5 wt %.

22. The method according to claim 20, wherein the effective sulfur dioxide dosage is greater than 2 wt %.

23. A method for pretreating and hydrolyzing lignocellulosic biomass comprising:

a) adding acid to the lignocellulosic biomass to produce acidified lignocellulosic biomass, said acid comprising at least one of sulfur dioxide and sulfurous acid;

b) pretreating the acidified lignocellulosic biomass in at least one pretreatment reactor to provide a pretreated slurry having a pH less than 1.5, said pretreated slurry comprising cellulose, said acidified lignocellulosic biomass having a consistency between 14.5 wt % and 40.5 wt %, said at least one pretreatment reactor comprising a first pretreatment reactor, said pretreating conducted at a temperature greater than 170°

C. and under pretreating conditions wherein a product of sulfur dioxide loading and V_s/V_r is greater than 0.8 wt %, where V_s/V_r is a ratio of slurry volume to reactor volume and where sulfur dioxide loading is a ratio of grams of sulfur dioxide fed to the first pretreatment reactor to grams of dry lignocellulosic biomass fed to the first pretreatment reactor expressed as a weight percentage; and

c) hydrolyzing the cellulose from the pretreated slurry with an enzyme to produce glucose,

wherein said acid is added to the lignocellulosic biomass in an amount sufficient to provide a sulfur dioxide loading of at least 20 wt %.