Processes and apparatus for lignin separation in biorefineries

Patent metadata

Field	Value
Publication number	US-9322072-B2
Application number	US-201314066534-A
Country	US
Kind code	B2
Filing date	Oct 29, 2013
Priority date	Dec 11, 2012
Publication date	Apr 26, 2016
Grant date	Apr 26, 2016

Abstract

The present invention generally provides methods of improving lignin separation during biomass fractionation with an acid to release sugars and a solvent for lignin (such as ethanol). In some embodiments, a digestor is employed to fractionating a feedstock in the presence of a solvent for lignin, sulfur dioxide, and water, to produce a liquor containing hemicellulose, cellulose-rich solids, and lignin. A solid additive is added to the digestor, wherein the solid additive combines with at least a portion of the lignin. Then a mixture of lignin and the solid additive is separated from the liquor, prior to hemicellulose recovery. Optionally, a solid additive may also be introduced to a hydrolysis reactor for converting hemicellulose oligomers to monomers, to improve separation of acid-catalyzed lignin. In some embodiments, the solid additive is gypsum or a gypsum/lignin mixture.

First claim

What is claimed is:

1. A process for fractionating lignocellulosic biomass, said process comprising:
(a) providing a feedstock comprising lignocellulosic biomass;
(b) in a digestor, fractionating said feedstock under effective fractionation conditions in the presence of a solvent for lignin, an acid or acid precursor, and water, to produce a liquor containing hemicellulose, cellulose-rich solids, and lignin;
(c) substantially removing said cellulose-rich solids from said liquor;
(d) after step (c), introducing a solid additive to said liquor, wherein said solid additive is introduced directly and not generated in situ, and wherein said solid additive combines with at least a portion of said lignin; and
(e) after step (d), separating a mixture comprising said lignin and said solid additive from said liquor,
wherein step (d) is carried out prior to or simultaneously with removal of said solvent for lignin from said liquor, and
wherein said solid additive is selected from the group consisting of metal sulfates, metal sulfate hydrates, metal sulfate derivatives, ammonium sulfate, ammonium sulfate derivatives, native lignin, acid-condensed lignin, sulfonated lignin, lignin derivatives, and combinations thereof.

2. The process of claim 1 , wherein said acid or acid precursor is selected from the group consisting of sulfur dioxide, sulfurous acid, sulfur trioxide, sulfuric acid, lignosulfonic acid, and combinations thereof.

3. The process of claim 1 , wherein said solid additive is selected from the group consisting of anhydrite, calcium sulfate hemihydrate, gypsum, and combinations thereof.

4. The process of claim 1 , wherein said solid additive consists essentially of gypsum.

5. The process of claim 4 , wherein said acid or acid precursor is selected from the group consisting of sulfur dioxide, sulfurous acid, sulfur trioxide, sulfuric acid, lignosulfonic acid, and combinations thereof, and wherein said gypsum is recycled gypsum that is generated from downstream neutralization of said acid or acid precursor following step (e).

6. The process of claim 1 , wherein said solid additive consists essentially of gypsum and a lignin species selected from the group consisting of native lignin, acid-condensed lignin, sulfonated lignin, lignin derivatives, and combinations thereof.

7. The process of claim 6 , wherein said acid or acid precursor is selected from the group consisting of sulfur dioxide, sulfurous acid, sulfur trioxide, sulfuric acid, lignosulfonic acid, and combinations thereof, and wherein said gypsum is recycled gypsum that is generated from downstream neutralization of said acid or acid precursor following step (e) and said lignin is recycled lignin that is removed following step (e).

8. The process of claim 1 , wherein step (d) is carried out prior to or simultaneously with removal of said acid or acid precursor from said liquor.

9. The process of claim 1 , wherein step (d) is carried out following removal of said acid or acid precursor from said liquor.

10. The process of claim 1 , said process further comprising recovering at least a portion of said solid additive from said mixture obtained in step (e), as recovered solid additive, and then recycling at least a portion of said recovered solid additive back to step (d) whereby said recovered solid additive is introduced to said liquor.

11. The process of claim 1 , said process further comprising recovering said hemicellulose.

12. The process of claim 1 , said process further comprising hydrolyzing said cellulose-rich solids to produce glucose.

13. A process for fractionating lignocellulosic biomass, said process comprising:
(a) providing a feedstock comprising lignocellulosic biomass;
(b) in a digestor, fractionating said feedstock under effective fractionation conditions in the presence of a solvent for lignin, an acid or acid precursor, and water, to produce a liquor containing hemicellulose, cellulose-rich solids, and lignin;
(c) substantially removing said cellulose-rich solids from said liquor;
(d) after step (c), in a hydrolysis reactor, hydrolyzing said hemicellulose contained in said liquor, in the presence of a hydrolysis catalyst, to produce fermentable hemicellulosic sugars;
(e) after step (d), introducing a solid additive to said hydrolysis reactor, wherein said solid additive is introduced directly and not generated in situ, and wherein said solid additive combines with at least a portion of said lignin;
(f) after step (e), separating a mixture comprising said lignin and said solid additive from said fermentable hemicellulosic sugars; and
(g) recovering said fermentable hemicellulosic sugars,
wherein said solid additive is selected from the group consisting of metal sulfates, metal sulfate hydrates, metal sulfate derivatives, ammonium sulfate, ammonium sulfate derivatives, native lignin, acid-condensed lignin, sulfonated lignin, lignin derivatives, and combinations thereof.

14. The process of claim 13 , wherein said acid or acid precursor is selected from the group consisting of sulfur dioxide, sulfurous acid, sulfur trioxide, sulfuric acid, lignosulfonic acid, and combinations thereof.

15. The process of claim 13 , wherein said solid additive is selected from the group consisting of anhydrite, calcium sulfate hemihydrate, gypsum, and combinations thereof.

16. The process of claim 13 , wherein said solid additive consists essentially of gypsum.

17. The process of claim 16 , wherein said acid or acid precursor is selected from the group consisting of sulfur dioxide, sulfurous acid, sulfur trioxide, sulfuric acid, lignosulfonic acid, and combinations thereof, and wherein said gypsum is recycled gypsum that is generated from downstream neutralization of said acid or acid precursor following step (g).

18. The process of claim 13 , wherein said solid additive consists essentially of gypsum and lignin.

19. The process of claim 18 , wherein said acid or acid precursor is selected from the group consisting of sulfur dioxide, sulfurous acid, sulfur trioxide, sulfuric acid, lignosulfonic acid, and combinations thereof, and wherein said gypsum is recycled gypsum that is generated from downstream neutralization of said acid or acid precursor following step (g) and said lignin is recycled lignin that is removed following step (g).

20. The process of claim 13 , wherein step (d) is carried out prior to or simultaneously with removal of said solvent for lignin from said liquor.

21. The process of claim 13 , wherein step (d) is carried out following removal of said solvent for lignin from said liquor.

22. The process of claim 13 , wherein step (d) is carried out prior to or simultaneously with removal of said acid or acid precursor from said liquor.

23. The process of claim 13 , wherein step (d) is carried out following removal of said acid or acid precursor from said liquor.

24. The process of claim 13 , said process further comprising introducing a second solid additive to said digestor.

25. The process of claim 24 , wherein said second solid additive introduced to said digestor is the same as said solid additive introduced to said hydrolysis reactor.

26. The process of claim 13 , said process further comprising recovering at least a portion of said solid additive from said mixture obtained in step (f), as recovered solid additive, and recycling at least a portion of said recovered solid additive back to step (e) whereby said recovered so

Assignees

• Api Ip Holdings Llc

Inventors

• Retsina Theodora
• Pylkkanen Vesa
• Nelson Kimberly
• Szczepanik Mark

Classifications

• C08H8/00

  Macromolecular compounds derived from lignocellulosic materials {(pretreatment thereof B27N)} · CPC title

• C07G1/00 Primary

  Low-molecular-weight derivatives of lignin (high-molecular-weight derivatives of lignin {C08H6/00}) · CPC title

• C13K1/02

  obtained by saccharification of cellulosic materials (manufacture of fodder A23K10/32) · CPC title

• C13K1/00 Primary

  Glucose (separation from invert sugar C13K3/00); Glucose-containing syrups · CPC title

• C13K13/00

  Sugars not otherwise provided for in this class · CPC title