Cellulose-solvent-based lignocellulose fractionation with modest reaction conditions and reagent cycling
View Patent ↗Embodiments of the present invention overcome the well-known recalcitrance of lignocellulosic biomass in an economically viable manner. A process and system are provided for the efficient fractionation of lignocellulosic biomass into cellulose, hemicellulose sugars, lignin, and acetic acid. The cellulose thus obtained is highly amorphous and can be readily converted into glucose using known methods. Fermentable hemicellulose sugars, low-molecular-weight lignin, and purified acetic acid are also major products of the process and system. The modest process conditions and low solvent/solid ratios of some embodiments of the invention imply relatively low capital and processing costs.
1. A process for fractionating lignocellulosic biomass, the process comprising:
(i) providing lignocellulosic biomass with an amount of hemicellulose present in the biomass in its native form;
(ii) providing a first solvent and combining with the lignocellulosic biomass, wherein the first solvent dissolves at least some of the cellulose present in the lignocellulosic biomass;
(iii) providing a second solvent and combining with the material from step (ii), wherein at least some of the cellulose that is dissolved by the first solvent in step (ii) precipitates out of the liquid phase;
(iv) providing a third solvent and combining with the material from step (iii), and then separating a black liquor and substantially solid phase; and
(v) providing a fourth solvent and combining with the substantially solid phase from step (iv), and then separating the solid phase comprising cellulose, and a light liquor comprising hemicellulose, and no xylose or xylose as a minor constituent.
2. The process of claim 1 , wherein the first solvent in step (ii) comprises one or more chemicals selected from the group consisting of hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, polyphosphoric acid, acetic acid, sulfur dioxide, zinc chloride, sodium hydroxide, potassium hydroxide, ammonia, lithium chloride/N,N-dimethylacetamide, 1-butyl-3-methylimidazolium hexafluorophosphate, dimethylsulfoxide/tetrabutylammonium fluoride trihydrate, N-methylmorpholine-N-oxide, cadmium monoxide/ethylenediamine, and water.
3. The process of claim 1 , wherein the second solvent in step (iii) comprises one or more chemicals selected from the group consisting of methanol, ethanol, 1-propanol, 2-propanol, acetone, propanal, 1-butanol, 2-butanol, butanal, butanone (methyl ethyl ketone), t-butanol, and water.
4. The process of claim 1 , wherein the third solvent in step (iv) comprises one or more chemicals selected from the group consisting of methanol, ethanol, 1-propanol, 2-propanol, acetone, propanal, 1-butanol, 2-butanol, butanal, butanone (methyl ethyl ketone), t-butanol, and water.
5. The process of claim 1 , wherein the fourth solvent from step (v) comprises one or more materials selected from the group consisting of liquid water, steam, recycle water, process condensate, fermentation-broth condensate, and carbon dioxide.
6. The process of claim 1 , further comprising subjecting the black liquor, obtained in step (iv), to step (vi), a vapor/liquid separation operation selected from the group consisting of distillation, single-stage evaporation, multiple-effect evaporation, thermocompression, and venturi scrubbing.
7. The process of claim 1 , wherein steps (ii)-(v) are each conducted in batches.
8. The process of claim 3 , wherein the second solvent in step (iii) comprises acetone.
9. A process for fractionating lignocellulosic biomass, the process comprising:
(i) providing chemically unmodified lignocellulosic biomass;
(ii) providing polyphosphoric acid and combining with the lignocellulosic biomass, wherein the polyphosphoric acid dissolves at least 90% of the cellulose present in the lignocellulosic biomass;
(iii) providing acetone or ethanol and combining with the material from step (ii), wherein at least 90% of the cellulose that is dissolved by the polyphosphoric acid in step (ii) precipitates out of the liquid phase;
(iv) providing acetone or ethanol and combining with the material from step (iii), and then separating a substantially solid phase and black liquor; and
(v) providing water and combining with the substantially solid phase from step (iv), and then separating a solid phase, which comprises the cellulose, and light liquor comprising hemicellulose with a high degree of polymerization as a major constituent.
10. The process of claim 9 , further comprising separating the black liquor and recovering polyphosphoric acid.
11. The process of claim 10 , wherein recovering polyphosphoric acid comprises burning a process stream and recycling P 2 O 5 and steam back to step (ii).
12. The process of claim 9 , further comprising recovering acetone from the black liquor, the light liquor, or both.
13. A process for fractionating lignocellulosic biomass comprising:
(i) providing lignocellulosic biomass without prior removal of hemicellulose;
(ii) removing lignin by dissolving cellulose and hemicellulose, then dissolving lignin into a liquid phase and precipitating cellulose and hemicellulose into a solid phase, and separating;
(iii) removing hemicellulose from the solid phase by dissolving hemicellulose into a liquid phase, and separating, wherein hemicellulose is separated from the biomass solely by dissolving, precipitating, and re-dissolving hemicellulose at reactor temperatures ranging between about 20° C. and 80° C., whereby less furfural is produced than compared with a method for removing hemicellulose from the biomass in which hemicellulose is hydrolyzed at reactor temperatures above 80° C.