Process for enzymatic hydrolysis of lignocellulosic material and fermentation of sugars

Patent metadata

Field	Value
Publication number	US-10144939-B2
Application number	US-201515307046-A
Country	US
Kind code	B2
Filing date	Apr 29, 2015
Priority date	Apr 30, 2014
Publication date	Dec 4, 2018
Grant date	Dec 4, 2018

Abstract

The invention relates to a process for the preparation of a fermentation product from lignocellulosic material, comprising the following steps:
a) optionally, pre-treatment of the lignocellulosic material, b) optionally, washing of the optionally pretreated lignocellulosic material, c) enzymatic hydrolysis of the optionally washed and/or optionally pretreated lignocellulosic material using an enzyme composition comprising at least two cellulases and whereby the enzyme composition at least comprises LPMO, and optionally purifying the hydrolyzed lignocellulosic material, d) fermentation of the hydrolyzed lignocellulosic material to produce a fermentation product, and e) optionally, recovery of a fermentation product, wherein oxygen is consumed in amounts corresponding to between 20 and 5000 mmol molecular oxygen per kg glucan present in the lignocellulosic material, the oxygen is added after the pretreatment and before and/or during the enzymatic hydrolysis of the lignocellulosic material, preferably in an amount corresponding to at least 30 mmol molecular oxygen per kg glucan present in the lignocellulosic material, more preferably in an amount corresponding to at least 40 mmol molecular oxygen per kg glucan present in the lignocellulosic material, and most preferably in an amount corresponding to at least 50 mmol molecular oxygen per kg glucan present in the lignocellulosic material is consumed.

First claim

The invention claimed is:

1. A process for preparation of a sugar product from lignocellulosic material, comprising:
enzymatic hydrolysis of the lignocellulosic material using an enzyme composition comprising at least two cellulases and whereby the enzyme composition at least comprises lytic polysaccharide monooxygenase (LPMO),

wherein oxygen is consumed in amounts corresponding to between 20 and 5000 mmol molecular oxygen per kg glucan present in the lignocellulosic material, the oxygen is added during the enzymatic hydrolysis of the lignocellulosic material, oxygen is added to lignocellulosic material so that the dissolved oxygen concentration in the liquid phase is more than 0.02 mol/m 3 when measured at about 62° C. and normal atmospheric pressure.

2. A process for preparation of a fermentation product from lignocellulosic material, comprising:
enzymatic hydrolysis of the lignocellulosic material using an enzyme composition comprising at least two cellulases and whereby the enzyme composition at least comprises lytic polysaccharide monooxygenase (LPMO), and optionally purifying the hydrolysed lignocellulosic material, and
fermentation of the hydrolysed lignocellulosic material to produce a fermentation product,

wherein oxygen is consumed in amounts corresponding to between 20 and 5000 mmol molecular oxygen per kg glucan present in the lignocellulosic material, the oxygen is added after the pretreatment and before and/or during the enzymatic hydrolysis of the lignocellulosic material and wherein the dissolved oxygen concentration in the liquid phase is more than 0.02 mol/m 3 when measured at about 62° C. and normal atmospheric pressure.

3. The process according to claim 2 , wherein the fermentation is conducted with a microorganism that is able to ferment at least one C5 sugar.

4. The process according to claim 3 , wherein the microorganism is of the species Saccharomyces cerevisiae , in which genetic modifications have been made.

5. The process according to claim 1 , wherein the oxygen is added in the form of bubbles.

6. The process according to claim 1 , wherein the reactor for the enzymatic hydrolysis has a volume of 1 m 3 or more.

7. The process according to claim 1 , wherein the enzymatic hydrolysis time is 5 to 150 hours.

8. The process according to claim 1 , wherein the enzyme composition used retains activity for 30 hours or more.

9. The process according to claim 1 , wherein the hydrolysis is conducted at a temperature of 45° C. or more.

10. The process according to claim 1 , wherein the enzyme composition is obtained from a fungus, or the enzyme composition comprises a fungal enzyme.

11. The process according to claim 1 , wherein the dry matter content in the enzymatic hydrolysis is 10 wt % or more.

12. The process according to claim 1 , in which the enzymatic hydrolysis takes place in a batch, fed batch and/or continuous culture reactor.

13. The process according to claim 1 , wherein the enzyme composition is in the form of a whole fermentation broth of a fungus.

14. The process according to claim 1 , in which oxygen is introduced as an oxygen-containing gas, optionally air.

15. The process according to claim 1 , wherein oxygen is consumed in amounts corresponding to between 28 and 3400 mmol molecular oxygen per kg glucan present in the lignocellulosic material.

16. The process according to claim 1 , wherein the hydrolysis is conducted at a temperature of 50° C. or more.

17. The process according to claim 1 , wherein the hydrolysis is conducted at a temperature of 55° C. or more.

18. The process according to claim 1 , wherein the enzyme composition is obtained from a fungus of the genus Rasamsonia or the enzyme composition comprises a Rasamsonia enzyme.

19. The process according to claim 1 , wherein the dry matter content in the enzymatic hydrolysis is 14 wt % or more.

20. The process according to claim 1 , wherein the dry matter content in the enzymatic hydrolysis is 14 to 33 wt %.

21. The process of claim 1 , further comprising pre-treatment of the ligno-cellulosic material, prior to the enzymatic hydrolysis.

22. The process of claim 1 , further comprising washing of the ligno-cellulosic material, prior to the enzymatic hydrolysis.

23. The process of claim 1 , further comprising recovery of a glucose-containing composition from the enzymatic hydrolysis.

24. The process of claim 1 , further comprising, prior to the enzymatic hydrolysis, pre-treatment of the ligno-cellulosic material and washing of the pre-treated ligno-cellulosic material.

25. The process of claim 1 , further comprising pre-treatment of the ligno-cellulosic material prior to the enzymatic hydrolysis and recovery of a glucose-containing composition from the enzymatic hydrolysis.

26. The process of claim 1 , further comprising pre-treatment of the ligno-cellulosic material and washing of the pre-treated ligno-cellulosic material, prior to the enzymatic hydrolysis, and recovery of a glucose-containing composition from the enzymatic hydrolysis.

27. The process of claim 2 , further comprising pre-treatment of the ligno-cellulosic material, prior to the enzymatic hydrolysis.

28. The process of claim 2 , further comprising washing of the ligno-cellulosic material, prior to the enzymatic hydrolysis.

29. The process of claim 2 , further comprising recovery of a fermentation product from the enzymatic hydrolysis.

30. The process of claim 2 , further comprising, prior to the enzymatic hydrolysis, pre-treatment of the ligno-cellulosic material and washing of the pre-treated ligno-cellulosic material.

31. The process of claim 2 , further comprising pre-treatment of the ligno-cellulosic material prior to the enzymatic hydrolysis and recovery of a fermentation product from the enzymatic hydrolysis.

32. The process of claim 2 , further comprising pre-treatment of the ligno-cellulosic material and washing of the pre-treated ligno-cellulosic material, prior to the enzymatic hydrolysis, and recovery of a fermentation product from the enzymatic hydrolysis.

Assignees

• Dsm Ip Assets Bv

Inventors

• Noordam Bertus
• Berkhout Michael Petrus Jozef

Classifications

• C13K13/00

  Sugars not otherwise provided for in this class · CPC title

• C12P19/14

  produced by the action of a carbohydrase {(EC 3.2.x)}, e.g. by alpha-amylase {, e.g. by cellulase, hemicellulase} · CPC title

• C12P2203/00

  Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source · CPC title

• C12P7/16

  Butanols · CPC title

• C12P2201/00

  Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis · CPC title