IP Library Granted Patent US 8,022,260
Granted Patent B2
US 8,022,260 · App. 12/299,316 · Granted Sep 20, 2011

Process for the conversion of biomass to liquid fuels and specialty chemicals

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Quick Facts
Patent No.
US 8,022,260
App. No.
12/299,316
Granted
Sep 20, 2011
Kind
B2
Abstract

The present invention relates to the conversion of solid biomass to liquid fuels and specialty chemicals. The process utilizes an activating step to make the biomass more susceptible to conversion, that is the biomass is broken down such that the components of the biomass are dissociated. Subsequently, the activated biomass undergoes a reaction to convert it to a bio-oil.

Claims (28)

1. A process for converting biomass to a bio-oil comprising the steps of:

a) adding one or more additives that act to subject the biomass to a pH swing of at least 4 pH units to activate the biomass in order to produce an activated biomass that is more susceptible to conversion;

b) optionally adding a solvent to said activated biomass;

c) partially converting the activated biomass to form a first bio-oil and leave an unconverted biomass; and

d) subjecting the unconverted biomass from step c) to a conversion process to produce a second bio-oil.

2. The process of claim 1 wherein the biomass in step a) is in particulate form, and at least two additives are added in step a) wherein at least a potion of the at least two additives react to form a crystalline phase distributed within the biomass particle.

3. The process of claim 2 wherein the biomass comprises at least one compound selected from the group consisting of cellulose and lignin.

4. The process of claim 3 wherein the cellulose comprises crystalline cellulose.

5. The process of claim 1 comprising, after step c) and before step d), the additional step of separating unconverted biomass from the first bio-oil.

6. The process of claim 5 wherein the unconverted biomass in step d) comprises crystalline cellulose.

7. The process of claim 6 wherein one or more additives are added to the unconverted biomass from step c) wherein such additives activate the biomass to make it more susceptible to conversion prior to step d).

8. A process for converting biomass to a bio-oil comprising the steps of:

a) adding an inorganic material, and optionally a solvent, to the biomass to form a mixture wherein said inorganic material is selected from the group consisting of cationic clays, anionic clays, natural clays, hydrotalcite materials, layered materials, minerals, metal oxides, hydroxides of metals of the alkaline and alkaline earth groups, and mixtures thereof and wherein the inorganic material is in a particulate form;

b) treating said mixture in a mechanical device to cause a homogeneous and intimate mixing of its components;

c) partially converting the biomass in said mixture during the treating of step b) to produce a first bio-oil and leave an unconverted biomass; and

d) subjecting the unconverted biomass from step c) to a conversion process to produce a second bio-oil.

9. The process of claim 8 wherein the mechanical devise is an extruder which extrudes the mixture to produce an extrudate and during the extrusion additional additives are added and heat and/or steam is added to the extruding mixture and further comprising drying, steaming and/or calcining the extrudate from the extrusion prior to step d).

10. The process of claim 8 wherein the conversion process of step d) is selected from the group consisting of a hydrothermal process, a pyrolysis process, and a flash pyrolysis process, a gasification process, a thermal cracking process, a catalytic cracking process, a hydrocracking process, an acid hydrolysis process, an enzymatic process, and aqueous reforming process and combinations thereof.

11. The process of claim 8 wherein the process further comprises the additional steps of (i) converting the second bio-oil to a liquid fuel, suitable for use in an internal combustion engine and (ii) converting the first bio-oil obtained in step c) to a liquid fuel, suitable for use in an internal combustion engine and wherein the additional steps (i) and (ii) comprise conversion in a unit selected from an FCC unit, a Hydrocracking unit, a Hydrotreating unit, a Thermal Cracking unit, and combinations thereof.

12. The process of claim 8 wherein the first bio-oil and the second bio-oil are blended with fossil fuels prior to processing in a refinery.

13. The process of claim 8 wherein the first bio-oil is subsequently converted to a transportation fuel by aqueous phase reforming.

14. The process of claim 8 wherein, prior to step d), the unconverted biomass from step c) is submitted to intimate mixing with an additive, optionally in the presence of a solvent.

15. The process of claim 8 wherein prior to step a) one or more additives are added to the biomass wherein such additives activate the biomass so that it is more susceptible to conversion.

16. The process of claim 15 wherein the one or more additives act to subject the biomass to a pH swing of at least 4 pH units.

17. The process of claim 16 wherein the biomass is in particulate form prior to step a). and the one or more additives are at least two additives wherein at least a potion of the at least two additives react to form a crystalline phase distributed within the biomass particle.

18. The process of claim 8 comprising, after step c) and before step d), the additional step of separating the unconverted biomass from the first bio-oil.

19. The process of claim 18 wherein the biomass comprises lignin, hemi-cellulose and crystalline cellulose and wherein in step c) at least part of the hemi-cellulose is converted to the first bio-oil such that the unconverted biomass comprises mainly lignin and crystalline cellulose.

20. The process of claim 19 wherein prior to step d) one or more additives are added to the unconverted biomass from step c) such that the unconverted biomass is activated to make it more susceptible to conversion prior to step d).

Assignments (13)
CHANGE OF NAME Recorded Aug 18, 2020
From: INAERIS TECHNOLOGIES, LLC
To: MARD, INC.
Reel/Frame 054213/0032 →
CHANGE OF NAME Recorded Apr 7, 2016
From: KIOR, LLC
To: INAERIS TECHNOLOGIES, LLC
Reel/Frame 038380/0344 →
NUNC PRO TUNC ASSIGNMENT Recorded Sep 29, 2015
From: KIOR, INC.
To: KIOR, LLC
Reel/Frame 036717/0262 →
LICENSE Recorded Apr 13, 2015
From: BIOECON B.V.
To: BIOECON INTERNATIONAL HOLDING N.V.
Reel/Frame 035391/0973 →
LICENSE Recorded Dec 4, 2014
From: KIOR INC.
To: BIOECON B.V.
Reel/Frame 034365/0882 →
LICENSE Recorded Nov 11, 2014
From: BIOECON B.V.
To: KIOR INC.
Reel/Frame 034141/0823 →
SECURITY INTEREST Recorded Jul 22, 2014
From: KIOR, INC.
To: KFT TRUST, VINOD KHOSLA, TRUSTEE, AS FIRST LIEN AGENT
Reel/Frame 033390/0423 →
SECURITY INTEREST Recorded Apr 8, 2014
From: KIOR, INC.
To: KFT TRUST, C/O KHOSLA VENTURES
Reel/Frame 032630/0441 →
SECURITY AGREEMENT Recorded Oct 23, 2013
From: KIOR, INC.
To: KHOSLA VENTURES III, LP
Reel/Frame 031483/0771 →
SECURITY INTEREST Recorded Feb 1, 2012
From: KIOR, INC.
To: 1538731 ALBERTA LTD., AS AGENT
Reel/Frame 027689/0151 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 29, 2009
From: BIOECON INTERNATIONAL HOLDING N.V.
To: BIOECON B.V.
Reel/Frame 023019/0102 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 29, 2009
From: BIOECON B.V.
To: KIOR, INC.
Reel/Frame 023019/0662 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 3, 2008
From: O'CONNOR, PAUL, MR.; STAMIRES, DENNIS, MR.; DAAMEN, SJOERD, MR.
To: BIOECON INTERNATIONAL HOLDING N.V.
Reel/Frame 021774/0220 →