MULTIPRODUCT BIOREFINERY FOR SYNTHESIS OF FUEL COMPONENTS AND CHEMICALS FROM LIGNOCELLULOSICS VIA LEVULINATE CONDENSATIONS

• US 20120283493A1
• Filed: 03/07/2012
• Published: 11/08/2012
• Est. Priority Date: 06/05/2009
• Status: Abandoned Application

• Current Assignee: Energy & Environmental Research Center (GE Aerospace)
• Original Assignee: Energy & Environmental Research Center (GE Aerospace)
• Inventors: Olson, Edwin S., Heide, Carsten
• Application Number:
  US13/413,881
• Publication Number:
  US 20120283493A1
• Time in Patent Office: Days
• US Class Current: 585/242
• CPC Class Codes: C10G 2300/1011 Biomass
• CPC Class Codes: C10G 2300/1014 of vegetal origin
• CPC Class Codes: C10G 2300/1096 Aromatics or polyaromatics
• CPC Class Codes: C10G 2400/02 Gasoline
• CPC Class Codes: C10G 2400/04 Diesel oil
• CPC Class Codes: C10G 2400/08 Jet fuel
• CPC Class Codes: C10G 2400/18 Solvents
• CPC Class Codes: C10G 3/42 Catalytic treatment
• CPC Class Codes: C10G 3/44 characterised by the catalyst used
• CPC Class Codes: C10G 3/50 in the presence of hydrogen, hydrogen donors or hydrogen generating compounds
• CPC Class Codes: C10L 1/04 essentially based on blends of hydrocarbons
• CPC Class Codes: C10L 1/08 for compression ignition
• CPC Class Codes: Y02P 30/20 using bio-feedstock

Abstract

An integrated method for production of fuels, fuel additives, or chemicals in a biorefinery by the conversion of cellulosic materials is disclosed herein. The method is based on converting a source of C6 sugar into a mixture of hydrotreated compounds. Embodiments of the method can be highly integrated, with reagents for particular steps being provided by other steps of the process.

Claims

1. A method for converting a source of C6 sugar into a mixture of hydrotreated compounds comprising:

thermocatalytically reacting a source of C6 sugar to produce a solution comprising at least one of levulinic acid and levulinic acid ester;

extracting at least one of the levulinic acid and the levulinic acid ester from the solution using a cyclic ether;

condensing at least a portion of at least one of the levulinic acid and the levulinic acid ester with at least one of C4-C11 aldehydes, C4-C11 ketones, C4-C11 esters, or C4-C11 ketoacids to produce a condensation product; and

hydrotreating at least a portion of the condensation product to provide a mixture of hydrotreated compounds.

2. The method of claim 1, wherein the source of C6 sugar comprises at least one of cellulosic material and starch material.

3. The method of claim 1, wherein the source of C6 sugar comprises wood, wood pulp, pulping sludge, particleboard, paper, grass, or an agricultural by-product.

4. The method of claim 1, wherein the source of C6 sugar comprises an agricultural by-product comprising at least one of straw, stalks, cobs, beets, beet pulp, seed hulls, bagasse, algae, corn starch, potato waste, sugar cane, and fruit waste.

5. The method of claim 1, wherein the thermocatalytic reaction is conducted with acid in at least one of water and alcohol.

6. The method of claim 1, wherein thermocatalytically reacting comprises depolymerizing the source of C6 sugar in a thermal unit to provide a soluble carbohydrate intermediate prior to reacting catalytically to produce at least one of the levulinic acid and the levulinic acid ester.

7. The method of claim 6, wherein the soluble carbohydrate intermediate comprises anhydrosugar.

8. The method of claim 7, wherein the thermocatalytic reaction of the anhydrosugar is catalyzed by a solid acid catalyst.

9. The method of claim 1, wherein the C4-C11 aldehyde is branched or aromatic.

10. The method of claim 9, wherein the C4-C11 aldehyde is selected from the group consisting of isobutyraldehyde, furfural, hydroxymethylfurfural, substituted benzaldehydes, and cyclic aliphatic aldehydes.

11. The method of claim 10, wherein the furfural is prepared from a source of C5 sugars.

12. The method of claim 1, wherein the C4-C11 ketone is selected from the group consisting of 1,2 diketones, 1,2 ketoesters, 1,4 ketoesters, 1,4 ketoacids, 2,3-butanedione, and 2,3-pentanedione.

13. The method of claim 1, wherein the condensing comprises condensing in the presence of a catalyst.

14. The method of claim 13, wherein the catalyst comprises a solid base catalyst.

15. The method of claim 13, wherein the catalyst comprises hydrotalcite or impregnated hydrotalcite.

16. The method of claim 13, wherein the catalyst is a solid acid catalyst

17. The method of claim 13, wherein the catalyst is a free radial initiator comprising manganese(III) acetate.

18. The method of claim 13, wherein the solid acid catalyst for the condensation comprises a transition metal or a heterogeneous catalyst comprising at least one of sulfated titania, sulfated zirconia, sulfated alumina, sulfonated activated carbon, sulfonated mesoporous carbon, sulfonated carbon composite, and sulfonated polymer.

19. The method of claim 1, further comprising separating the mixture of hydrotreated compounds to give at least one of a fuel or fuel blendstock.

20. The method of claim 1, wherein the hydrotreating of the condensation products comprises producing cyclic ethers.

21. The method of claim 20, further comprising hydrotreating the cyclic ethers to produce one of diesel, diesel blendstock, jet fuel, jet fuel blendstock, and any combination thereof.

22. The method of claim 21, further comprising coprocessing the cyclic ethers with at least one of free fatty acids, natural oils, tall oils, BTX (benzene, toluene, and xylenes), condensation products derived from BTX, and any combination thereof.

23. The method of claim 21, wherein the condensation product is separated to a mixture including materials having a chain length of about C10-C15, comprising n-alkanes, isoalkanes, cycloalkanes, and arylalkanes.

24. The method of claim 1, wherein at least a portion of an organic liquid is separated from an intermediate or final product of the method for use as solvent.

25. The method of claim 1, wherein the cyclic ether used to extract at least one of the levulinic acid and the levulinic acid ester is methyl tetrahydrofuran.

26. The method of claim 24, wherein the methyl tetrahydrofuran at least partially comprises methyl tetrahydrofuran separated from an intermediate or final product mixture of the method.

27. The method of claim 1, further comprising, partial evaporation of water prior to the extracting of at least one of levulinic acid and levulinic acid ester from the solution comprising at least one of levulinic acid and levulinic acid ester.

28. The method of claim 1, further comprising the hydrodeoxygenation of C5 oxygen containing carbon compounds to form gasoline.