System for treatment of biomass to facilitate the production of ethanol

• US 9,068,206 B1
• Filed: 03/03/2010
• Issued: 06/30/2015
• Est. Priority Date: 03/03/2009
• Status: Active Grant

• Current Assignee: Poet Research Inc.
• Original Assignee: Poet Research Inc.
• Inventors: Kwiatkowski, Jason Richard, McDonald, William F., Carlson, David Charles
• Primary Examiner(s): Savage, Matthew O
• Application Number:
  US12/716,989
• Time in Patent Office: 1,945 Days
• Field of Search: 210/198.2, 210/266, 210/692, 210/656, 210/180, 210/182, 210/190, 210/251, 210/253, 210/259, 210/269, 210/340, 210/664, 210/669, 210/683, 435/93, 435/163, 435/165, 435/289.1, 127/9, 127/46.2, 494/36
• US Class Current: 1/1
• CPC Class Codes: C12P 17/10 Nitrogen as only ring hetero atom
• CPC Class Codes: C13K 1/04 Purifying
• CPC Class Codes: C13K 13/002 Xylose
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

Systems for treating biomass for the production of ethanol are disclosed. The systems are configured to treat a liquid component separated from biomass to yield sugars available to be fermented into a fermentation product. The systems comprise a filter configured to remove particulate matter to provide a filtered component and an apparatus configured to remove inhibitors from the filtered liquid component provide a treated liquid component comprising sugars available for fermentation. Methods for treating for treating biomass useful in the production of a fermentation product are also disclosed. The methods include the steps of filtering a liquid component to remove particulate matter thereby yielding a filtered liquid component, and treating the filtered liquid component to remove inhibitors thereby yielding a treated liquid component comprising sugars available to be fermented into a fermentation product.

Claims

1. A system for the production of ethanol from pre-treated biomass comprising:

a source of pre-treated biomass;

a centrifuge in fluid communication with the source of pre-treated biomass, wherein the centrifuge is configured to separate the pre-treated biomass into a liquid component and a solid component, wherein the liquid component comprises sugars;

a filter comprising a pore size of between 25 microns and 100 microns, wherein the filter is in fluid communication with the centrifuge to receive the liquid component to provide a filtered liquid component;

an apparatus configured to remove one or more inhibitors from the filtered liquid component, thereby yielding a first treated liquid component, wherein the apparatus is in fluid communication with the filter to receive the filtered liquid component;

an evaporation system in fluid communication with the apparatus to receive the first treated liquid component to remove water from the first treated liquid component and produce a second treated liquid component; and

a fermentation system in fluid communication with the evaporation system to receive the second treated liquid component, wherein the fermentation system comprises an ethanologen to ferment the sugars into ethanol;

wherein the apparatus comprises an ion exchange system comprising a resin bed;

wherein the resin bed comprises a resin capable of binding said inhibitors;

wherein the biomass comprises lignocellulosic material;

wherein the lignocellulosic material comprises at least one of corn cobs, corn plant husks, corn plant leaves and corn plant stalks.

2. The system of claim 1 wherein the inhibitors comprise furfural.

3. The system of claim 1 wherein the inhibitors comprise hydroxymethylfurfural.

4. The system of claim 1 wherein the liquid component comprises furfural in a concentration of at least 700 PPM.

5. The system of claim 1 wherein the resin does not retain sugars.

6. The system of claim 1 wherein the resin does not retain xylose.

7. The system of claim 1 wherein the first treated liquid component comprises furfural at a concentration of no more than 700 PPM.

8. The system of claim 1 wherein the first treated liquid component comprises hydroxymethylfurfural at a concentration of no more than 100 PPM.

9. The system of claim 1 wherein the resin comprises an ion exchange chromatography type resin.

10. The system of claim 1, wherein the ion exchange system is in fluid communication with a source of a caustic solution and the filtered liquid component, and wherein the ion exchange system is configured to regenerate the resin bed by washing the resin bed with caustic solution from the source of caustic solution.

11. The system of claim 10, wherein the ion exchange system comprises:

a first column comprising a resin bed; and

a second column comprising a resin bed,

wherein the first column and the second column are each in fluid communication with the source of a caustic solution and the filtered liquid component, and wherein the first column and the second column are each configured to regenerate the resin bed by washing the resin bed with caustic solution from the source of caustic solution.

12. The system of claim 11, wherein the first column and the second column are configured in a parallel flow arrangement.