METHOD FOR PRODUCING ETHANOL BY FERMENTATION FROM LIGNOCELLULOSIC BIOMASS

• US 20110111474A1
• Filed: 02/10/2009
• Published: 05/12/2011
• Est. Priority Date: 03/12/2008
• Status: Active Grant

• Current Assignee: Klingele Golfkarton C.V.
• Original Assignee: Zylum Beteiligungsgesellschaft Mbh & Co. Patente Ii KG (Deutsche Bank Group)
• Inventors: Karstens, Ties
• Granted Patent: US 8,883,469 B2
• Time in Patent Office: Days
• US Class Current: 435/165
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: D21C 3/20 with organic solvents or in solvent environment
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

The description relates to a method of producing bioethanol by separating lignin from a crushed lignocellulose biomass and obtaining cellulose and, if required, hemicellulose and additionally processing the cellulose or the mixture of cellulose and hemicellulose to form sugars and subsequently form bioethanol. The method is characterised in that crushed lignocelluloses biomass is treated with an alkanolamine for extracting the lignin therein, the lignin solution is separated, the residue containing cellulose/hemicellulose is converted to sugars without drying, and the sugars are fermented to obtain bioethanol. The raw cellulose (cellulose/hemicellulose), owing to its high reactivity, can easily be converted into sugar, which can be fermented to form bioethanol.

Claims

1. A method of producing bioethanol by separating lignin from a crushed lignocelluloses biomass and obtaining cellulose and, if required, hemicelluloses and further processing of the cellulose or mixture of cellulose and hemicellulose to obtain sugars and subsequently obtain bioethanol, characterised in that crushed lignocelluloses biomass is treated with an alkanolamine for extracting the lignin therein, the lignin solution is separated, the residue containing cellulose/hemicellulose is converted to sugars without drying, and the sugars are fermented to obtain bioethanol.

2. A method according to claim 1, characterised in that the lignocellulose biomass is in the form of straw, grass, bagasse, poplar and/or bamboo.

3. A method according to claim 1, characterised in that during extraction of the lignin an additional solvent for lignin is used, particularly one which swells the cellulose and hemicellulose.

4. A method according to any of claim 1, characterised in that before extraction of the lignin, the lignocellulose biomass is treated with ammonia gas or with liquid ammonia solution.

5. A method according to any of claim 1, characterised in that extraction is continued for at least 10 minutes, in particular at least half an hour at a temperature of about 80°

C. to 150°

C., particularly about 100°

C. to 140°

C.

6. A method according to any of claim 1, characterised in that the alkanolamine is heated before extraction, particularly to a temperature of at least about 80°

C.

7. A method according to claim 1, characterised in that the alkanolamine is monoethanolamine.

8. A method according to claim 1, characterised in that after extraction of the lignin, the lignin solution adhering to the residue is removed by an additional solvent.

9. A method according to claim 8, characterised in that the lignin solution adhering to the residue is removed by washing or washing in countercurrent with the additional solvent, after which the additional solvent is separated from lignin and the extraction agent alkanolamine by distillation and recovered for additional use.

10. A method according to claim 1, characterised in that the lignin solution adhering to the residue is removed by squeezing out or centrifuging.

11. A method according to claim 1, characterised in that the lignin dissolved in the alkanolamine is precipitated by adding a non-solvent and separated by solid/liquid separation processes.

12. A method according to claim 11, characterised in that the precipitated lignin is separated from alkanol by filtering or centrifuging.

13. A method according to claim 12, characterised in that the lignin dissolved in alkanolamine is separated in a thin-film evaporator or by a membrane process.

14. A method according to claim 1, characterised in that the moist intermediate product containing the cellulose and, if required, hemicellulose is converted to sugar by treatment with a cellulase,

15. A method according to claim 1, characterised in that the sugar obtained from cellulose and, if required, hemicelluloses is fermented to form bioalcohol by adding and fermenting with yeast.