Process for the production of carbohydrate cleavage products from a lingnocellulosic material

• US 9,970,038 B2
• Filed: 04/30/2010
• Issued: 05/15/2018
• Est. Priority Date: 08/06/2009
• Status: Active Grant

• Current Assignee: Annikki Gmbh
• Original Assignee: Annikki Gmbh
• Inventors: Fackler, Karin, Messner, Kurt, Krongtaew, Chularat, Ertl, Ortwin
• Primary Examiner(s): Holland, Paul J
• Application Number:
  US13/388,725
• Publication Number:
  US 20130078677A1
• Time in Patent Office: 2,937 Days
• Field of Search: None
• 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 5/023 Methane
• CPC Class Codes: C12P 7/02 containing a hydroxy group
• CPC Class Codes: C12P 7/14 Multiple stages of fermentation; Multiple types of microorganisms or re-use of microorganisms
• CPC Class Codes: C12P 7/18 polyhydric
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

A process for the production of carbohydrate cleavage products, characterized by a combination of the measures that a lignocellulosic material is treated with an aqueous solution containing an alcohol, in particular a C_1-4-alcohol or a phenol, and having a pH-value of between 11.0 and 14.0 in order to cleave lignocellulose and separate cleavage products from the material, whereby a material enriched with cellulose and hemicellulose is obtained, and the obtained material enriched with cellulose and hemicellulose is treated with at least one carbohydrate-cleaving enzyme in order to obtain the carbohydrate cleavage products.

Claims

1. A process for the production of xylitol, the process comprising:

treating a lignocellulosic material with an aqueous solution containing an alcohol and having a pH-value of between 11.0 and 14.0, in order to cleave lignocellulose and separate cleavage products from said lignocellulosic material, whereby a material enriched with cellulose and hemicellulose is obtained, and

treating said obtained material enriched with cellulose and hemicellulose with a xylanase in order to obtain a xylose solution and solid;

converting said xylose solution to xylitol by enzymatic conversion without fermentation, wherein NAD(P)H as a cofactor, a cosubstrate for the regeneration of said cofactor, and an alcohol dehydrogenase are added to said xylose.

2. The process of claim 1, wherein said aqueous solution has a pH-value of between 11.0 and 13.0.

3. The process of claim 1, wherein said lignocellulosic material are straw, bagasse, energy grasses and/or spelts.

4. The process of claim 1, wherein said lignocellulosic material is present in said aqueous solution in a stock density of 5-40% by weight.

5. The process of claim 1, wherein said material enriched with cellulose and hemicellulose is converted with a xylanase and a liquid phase obtained is enzymatically converted into xylitol, and a remaining solid:

is reacted further with cellulase in order to obtain different fermentation products;

or

is subjected to a thermal or thermochemical conversion;

or

is subjected to a microbial conversion by bacteria, yeasts, or fungi;

or

is subjected to a further delignification step for the purpose of obtaining a cellulose fiber material.

6. The process of claim 1, wherein said material enriched with cellulose and hemicellulose is converted with a xylanase and a liquid phase obtained is enzymatically converted into xylitol using a xylose reductase, and a remaining solid:

is reacted further with cellulase in order to obtain different fermentation products;

or

is subjected to a thermal or thermochemical conversion;

or

is subjected to a microbial conversion by bacteria, yeasts, or fungi;

or

is subjected to a further delignification step for the purpose of obtaining a cellulose fiber material.

7. The process of claim 5, wherein said remaining solid is fermented in a biogas plant and is processed further into biogas.

8. The process of claim 1, wherein said alcohol includes a C_1-4-alcohol or a phenol.

9. The process of claim 8, wherein said lignocellulosic material are straw, bagasse, energy grasses and/or spelts.

10. The process of claim 9, wherein said lignocellulosic material is present in said aqueous solution in a stock density of 5-40% by weight.

11. The process of claim 6, wherein said remaining solid is fermented in a biogas plant and is processed further into biogas.

12. The process of claim 1, wherein said cleavage occurs at a temperature below 100°

C.

13. The process of claim 1, wherein glucose, xylose and lignin components of said lignocellulosic material are obtained in separated material flows.

14. The process of claim 1, wherein said enzymatic conversion from xylose to xylitol is performed directly in a mixture of said xylose solution and said solid.

15. The process of claim 1, wherein after treating said lignocellulosic material with said aqueous solution containing said alcohol, a solution containing lignin is separated and a decomposed solid remaining after said separation is treated with a xylanase, and a liquid phase is separated from said decomposed solid.

16. The process of claim 1, wherein treatment with said xylanase is conducted at 30-90°

C.

17. The process of claim 1, wherein said alcohol is at a concentration from 30% to 70% by volume in said aqueous solution so as to be sufficient to reduce solubility of hemicellulose and retain said hemicellulose in said lignocellulosic material so as to reduce loss of hemicellulose from said lignocellulosic material.

18. The process of claim 1, wherein said treating of said lignocellulosic material is performed without hydrogen peroxide.

19. The process of claim 1, wherein said cosubstrate for regeneration of said cofactor is selected from the group consisting of ethanol and isopropanol.