Lower cellulase requirements for biomass cellulose hydrolysis and fermentation

• US 20060014260A1
• Filed: 05/09/2005
• Published: 01/19/2006
• Est. Priority Date: 05/07/2004
• Status: Abandoned Application

• Current Assignee: The Trustees of Dartmounth College (Dartmouth College)
• Original Assignee: The Trustees of Dartmounth College (Dartmouth College)
• Inventors: Lynd, Lee R., Shao, Xiongjun, Fan, Zhiliang
• Application Number:
  US11/124,941
• Publication Number:
  US 20060014260A1
• Time in Patent Office: Days
• US Class Current: 435/161
• CPC Class Codes: C12M 21/12 for producing fuels or solvents C12M21/04 takes precedence; liquid carbonaceous fuels C10L1/00, solid fuels C10L5/00
• CPC Class Codes: C12M 27/02 Stirrer or mobile mixing elements
• CPC Class Codes: C12M 45/02 by mechanical forces; Stirring; Trituration; Comminuting crushing, pulverizing, disintegrating in general B02C
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

A semi-continuous simultaneous saccharification and fermentation (SSF) process for the bioconversion of cellulose into ethanol and other organic chemicals is disclosed. The process provides for substantially higher substrate conversion at a given enzyme loading (or alternatively a lower enzyme loading used to achieve the same conversion) in a reactor operated according to a semi-continuous feeding protocol.

Claims

1. A method for producing ethanol from a cellulosic substrate, comprising the steps of:

(a) roviding within a reaction vessel, a reaction mixture in the form of a slurry comprising cellulosic substrate, an enzyme and a fermentation agent, wherein the reaction mixture is reacted under conditions sufficient to initiate and maintain a fermentation reaction;

(b) etermining, by experiment or theoretical calculations, an optimum feeding frequency; and

(c) roviding additional quantities of the cellulosic substrate and the enzyme into the reaction vessel at an interval(s) according to the optimized feeding frequency.

2. The method of claim 1, wherein the optimized feeding frequency is in a range of about 1 to 8.

3. The method of claim 1 further comprising the step of removing from the reaction vessel an ethanol-containing effluent.

4. The method of claim 1 wherein the cellulosic substrate comprises woody biomass, forage grasses, herbaceous energy crops, agricultural residue, waste paper sludge and municipal solid waste.

5. The method of claim 1 wherein the ethanol-containing effluent is removed from the top portion of the reaction vessel.

6. The method of claim 1 wherein the slurry is agitated by mechanical mixing.

7. The method of claim 1 wherein the fermentation agent is selected from fungi and bacteria.

8. The method of claim 1 wherein the enzyme is cellulase.

9. The method of claim 1 being carried out using a semi-continuously solids-fed bioreactor.

10. A method of operating a reactor system to provide semi-continuous solids-fed fermentation of paper sludge, comprising:

advancing a paper sludge under a semi-continuous controlled flow rate;

chopping the paper sludge as it advances to subdivide the paper sludge into comparatively smaller particles;

digesting the comparatively smaller particles in an agitator by the action of a hydrolyzing enzyme; and

controlling the flow rate and amount of hydrolyzing enzyme added to the agitator for use in the step of digesting to establish a semi-continuous state of flow through the reactor system over an extended period of time while also maintaining a predetermined conversion efficiency of the paper sludge by action of the hydrolyzing enzyme at an optimized loading concentration.

11. The method of claim 10, wherein the optimized loading concentration is in a range of about 5 to 15 fpu/g.

12. The method of claim 10 wherein the hydrolyzing enzyme is cellulase.

13. The method of claim 10 further comprising the step of adding a fermentation agent selected from fungi and bacteria.

14. The method of claim 13 further comprising the step of removing from the agitator an ethanol-containing effluent.

15. The method of claim 14 wherein the ethanol-containing effluent is removed from the top portion of the agitator.

16. A semi-continuous solids-fed bioreactor comprising:

a feed tube containing a plug of solid waste;

a screw driven by a timer-controlled motor, the screw acting to advance the plug of solid waste into a chopper; and

an agitator that receives solid waste particles from the chopper and enzymes, fermentation agents and liquid reagents from an inlet valve, the solid waste particles, enzymes, fermenation agents and liquid reagents forming a slurry in the agitator, wherein the agitator includes a mixer driven by a second motor and at least one conduit from which products may be removed.

17. The bioreactor of claim 16, further comprising an isolation valve connecting the feed tube and the chopper.

18. The bioreactor of claim 17, wherein the isolation valve comprises a ball valve.