Process for treating biomass

• US 9,938,662 B2
• Filed: 07/16/2015
• Issued: 04/10/2018
• Est. Priority Date: 04/27/2012
• Status: Active Grant

• Current Assignee: The Michigan Biotechnology Institute
• Original Assignee: The Michigan Biotechnology Institute
• Inventors: Campbell, Timothy J., Teymouri, Farzaneh
• Primary Examiner(s): Brunsman, David M
• Application Number:
  US14/800,859
• Publication Number:
  US 20150315744A1
• Time in Patent Office: 999 Days
• CPC Class Codes: C08B 1/003 Preparation of cellulose solutions, i.e. dopes, with different possible solvents, e.g. ionic liquids solutions used in the manufacture of monocomponent artificial filaments or cellulose or derivatives thereof D01F2/02
• CPC Class Codes: C12P 19/02 Monosaccharides 2-ketogulonic acid C12P7/60
• 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 2201/00 Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
• CPC Class Codes: D21C 1/02 with water or steam
• CPC Class Codes: D21C 1/04 with acid reacting compounds
• CPC Class Codes: D21C 1/06 with alkaline reacting compounds
• CPC Class Codes: D21C 5/005 Treatment of cellulose-containing material with microorganisms or enzymes
• 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

This invention is directed to a process for treating biomass. The biomass is treated with a biomass swelling agent within the vessel to swell or rupture at least a portion of the biomass. A portion of the swelling agent is removed from a first end of the vessel following the treatment. Then steam is introduced into a second end of the vessel different from the first end to further remove swelling agent from the vessel in such a manner that the swelling agent exits the vessel at a relatively low water content.

Claims

1. A process comprising:

contacting biomass with a biomass swelling agent within a vessel under conditions sufficient to swell or rupture at least a portion of the biomass, thereby providing a treated biomass;

removing at least a portion of the swelling agent from the vessel, while leaving at least a majority of the treated biomass within the vessel;

introducing steam into the vessel; and

contacting the treated biomass left within the vessel with the steam to further remove swelling agent from the vessel.

2. The process of claim 1, wherein the biomass is contained within the vessel at a bed porosity of at least 85 vol %.

3. The process of claim 1, wherein the swelling agent is ammonia.

4. The process of claim 1, wherein swelling agent is added to the vessel to provide a weight ratio of swelling agent to biomass in a contacting zone of the vessel of at least 0.1:

1.

5. The process of claim 1, wherein the contact of the steam and the treated biomass in the vessel is carried out to provide an Archimedes number of at least 4.

6. The process of claim 1, wherein the swelling agent that is removed from the vessel by contact with the steam is recovered directly from the treatment vessel during the steam contacting step, and the directly recovered swelling agent has a water content of not greater than 15 wt %, based on total content of swelling agent recovered during the steam contacting step.

7. The process of claim 6, wherein the swelling agent that is removed from the vessel is removed as a vapor.

8. The process of claim 1, wherein the biomass is contained within a contact zone of the vessel, with the contact zone having a length to diameter ratio of greater than four.

9. The process of claim 1, wherein the steam is supplied to the vessel as saturated or superheated steam.

10. The process of claim 1, wherein the biomass is treated with the swelling agent to increase enzyme digestibility by at least 10% relative to that initially supplied to the vessel.

11. The process of claim 1, wherein during the contact of the steam and the treated biomass in the vessel, the vessel is at a bed angle of not greater than 25 degrees from vertical.

12. The process of claim 1, wherein the swelling agent comprises a water-soluble amine having the structure NRR₁ R₂ where R, R₁ and R₂ are the same or different and are selected from the group consisting of H and hydrocarbons containing 1-20 carbons, optionally substituted with oxygen, nitrogen, sulfur or phosphorous, and optionally where two or more of the R groups are attached to form a cyclic group.

13. The process of claim 12, wherein the water-soluble amine is selected from the group consisting of ammonia, methylamine, dimethylamine, ethylamine, tripropylamine, morpholine, and mixtures thereof.

14. The process of claim 1, wherein the swelling agent comprises water-soluble ammonium ions having the structure ⁺NRR₁ R₂R₃ where R, R₁ R₂, and R₃ are the same or different and are selected from the group consisting of H and hydrocarbons containing 1-20 carbons, optionally substituted with oxygen, nitrogen, sulfur or phosphorous, and optionally where two or more of the R groups are attached to form a cyclic group.

15. The process of claim 1, wherein the swelling agent comprises a hydroxide, carbonate, or bicarbonate of lithium, sodium, potassium, magnesium, or calcium.

16. The process of claim 1, wherein the swelling agent comprises a water soluble mono- or poly-carboxylic acid.

17. The process of claim 1, wherein the swelling agent comprises an inorganic acid.

18. The process of claim 1, wherein the vessel includes a plurality of containers within the vessel and positioned vertically relative to each other, each container comprising a perforated end plate and containing a portion of the biomass therein.

19. The process of claim 18, wherein the biomass in each container is compressed therein.

20. The process of claim 18, wherein the biomass is contained within the vessel at a bed porosity of at least 85 vol %.

21. The process of claim 1, further comprising:

recycling the swelling agent removed from the vessel to a second vessel containing biomass therein; and

contacting the biomass in the second vessel with the recycled swelling agent to swell or rupture at least a portion of the biomass.

22. The process of claim 21, wherein recycling the swelling agent comprises feeding the removed swelling agent to the second vessel with no processing to remove water when the removed swelling agent has a moisture content at or below a desired moisture content.

23. The process of claim 22, wherein the desired moisture content is 15 wt. %.

24. The process of claim 1, wherein removing at least a portion of the swelling agent from the vessel comprises, prior to introducing steam into the vessel, reducing pressure in the vessel to a value less than 50% of the pressure in the vessel during contacting the biomass with the swelling agent.