Nano-catalytic-solvo-thermal technology platform bio-refineries

• US 8,546,561 B2
• Filed: 07/16/2009
• Issued: 10/01/2013
• Est. Priority Date: 07/16/2008
• Status: Active Grant

• Current Assignee: Renmatix, Inc.
• Original Assignee: Renmatix, Inc.
• Inventors: Kilambi, Srinivas
• Primary Examiner(s): LEWIS, PATRICK T
• Application Number:
  US12/504,611
• Publication Number:
  US 20100069626A1
• Time in Patent Office: 1,538 Days
• Field of Search: None
• US Class Current: 536/128
• CPC Class Codes: C08H 8/00 Macromolecular compounds derived from lignocellulosic materials pretreatment thereof B27N
• CPC Class Codes: Y02P 20/54 using solvents, e.g. supercritical solvents or ionic liquids

Abstract

Methods of making glucose and/or furfural from biomass require one or more supercritical fluids that may be used to process biomass, cellulose from the biomass, and/or xylose from the biomass. Examples of supercritical fluids for use in processing biomass include ethanol, water, and carbon dioxide at a temperature and pressure above the critical points for ethanol and carbon dioxide but at a temperature and/or pressure below that of the critical point for water. A supercritical fluid containing carbon dioxide and water may be used to convert cellulose to glucose or convert xylose to furfural. The fluid has a temperature and pressure above the critical point of carbon dioxide, but at least one of the temperature and pressure is below the critical point for water.

Claims

1. A method of making at least one of furfural and glucose, the method comprising:

a. processing a biomass using a first fluid to form lignin, cellulose, and xylose;

b. processing at least one of the cellulose and xylose using a second fluid to form glucose and furfural respectively;

c. wherein at least one of the processing steps above is performed with a reactive fluid comprising carbon dioxide and water, the reactive fluid having a temperature and pressure above a critical point for carbon dioxide, and at least one of the temperature and the pressure of the reactive fluid being below the critical temperature and pressure, respectively, of water.

2. A method according to claim 1 wherein the reactive fluid further comprises C₁-C₅ alcohol, the temperature and pressure of the reactive fluid are above a critical point for said C₁-C₅ alcohol, and the reactive fluid is the first fluid used to process the biomass to form the lignin, cellulose, and xylose.

3. A method according to claim 1 wherein the second fluid comprises said reactive fluid of claim 1, and said second fluid does not contain alcohol.

4. A method according to claim 3 wherein the second fluid consists essentially of said carbon dioxide and said water.

5. A method according to claim 1 wherein said temperature and pressure of the first fluid and the second fluid when present are in the near-critical range for water.

6. A method according to claim 2 wherein the alcohol of the first fluid comprises ethanol.

7. A method according to claim 6 wherein the alcohol consists essentially of ethanol.

8. A method according to claim 2 further comprising separating an aqueous alcoholic solution of the lignin and the xylose from the first fluid by reducing at least one of the temperature and the pressure of the first fluid to evolve the carbon dioxide.

9. A method according to claim 8 further comprising precipitating the lignin by removing the alcohol from the alcoholic solution and filtering the lignin from the remaining solution containing the xylose.

10. A method according to claim 9 further comprising contacting the xylose-containing solution with carbon dioxide to form a second fluid, maintaining said second fluid at a temperature and pressure above the critical point of carbon dioxide and below a critical temperature, a critical pressure, or both of water sufficient to dehydrate said xylose to form furfural.

11. A method according to claim 1 wherein the cellulose is precipitated and separated from the first fluid.

12. A method according to claim 11 wherein the precipitation occurs by reducing the pressure of the first fluid sufficiently rapidly to prevent crystallization of the cellulose, providing an amorphous cellulose.

13. A method according to claim 11 or claim 12 and further comprising contacting the separated cellulose with supercritical water for a sufficient period of time to solubilize the cellulose and form a cellulose solution but not so long to hydrolyze more than ten percent by weight of the cellulose.

14. A method according to claim 13 wherein the period of time is about a second or less.

15. A method according to claim 14 wherein the period of time is about half a second or less.

16. A method according to claim 13 and further comprising quenching the cellulose solution with carbon dioxide to form a reaction mixture having a temperature and pressure above a critical point for carbon dioxide and wherein at least one of said temperature and said pressure are below a critical temperature and pressure respectively for water, and hydrolyzing said cellulose in said reaction mixture to form said glucose.

17. A method according to claim 11 or claim 12 comprising contacting said cellulose with a fluid comprising carbon dioxide and water, the third fluid having a temperature and pressure above a critical point for carbon dioxide, and at least one of the temperature and the pressure of said fluid being below the critical temperature and pressure, respectively, of water.

18. A method according to claim 17 wherein the third fluid has a temperature between about 280 and 290°

C.

19. A method according to claim 18 wherein said contacting occurs for a period of time between about 15 and 20 seconds.

20. A method according to claim 1 or claim 2 wherein

a. the second fluid comprises said carbon dioxide and water of step (c) and said processing of step (b) comprises processing the cellulose using said second fluid;

and

b. the xylose is processed using a third fluid comprising carbon dioxide and water, the third fluid having a temperature and pressure above a critical point for carbon dioxide, and at least one of the temperature and the pressure of the third fluid being below the critical temperature and pressure, respectively, of water.

21. A method according to claim 1, wherein the first fluid is quenched quickly subsequent to forming said lignin, cellulose, and xylose.