Renewable aromatics from lignocellulosic lignin
US-2015322214-A1 · Nov 12, 2015 · US
US10208076B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10208076-B2 |
| Application number | US-201514757851-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 23, 2015 |
| Priority date | Dec 7, 2012 |
| Publication date | Feb 19, 2019 |
| Grant date | Feb 19, 2019 |
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The present invention provides novel and improved processes for treating a lignocellulosic biomass or technical lignin using ionic liquids to obtain lignin breakdown products and polysaccharide biomass components. Recycling of ionic liquids can be included in the methods of the invention.
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What is claimed is: 1. A composition containing monomeric guaiacol, 4-ethyl guaiacol, 4-vinyl guaiacol, eugenol, syringol, 4-(1-propenyl) guaiacol, vanillin, allyl syringol, and guaiacylacetone, wherein the composition is formed by: i) solubilizing a technical lignin in a solution comprising a water-miscible ionic liquid (IL) to generate a solubilized material; ii) precipitating a fraction of the solubilized material with a polar solvent to generate a precipitated fraction and a supernatant; iii) extracting the lignin compounds from the supernatant by contacting the supernatant with an extractant; and iv) separating the lignin compounds from the extractant; wherein the extractant is a non-polar solvent. 2. The composition of claim 1 , wherein the ionic liquid is [C2mim][OAc]. 3. The composition of claim 1 , wherein the extractant is selected from the group consisting of benzene, pentane, and hexane. 4. The composition of claim 1 , wherein the solubilizing is performed at a temperature between about 100° C. and about 180° C. 5. The composition of claim 1 , wherein the polar solvent comprises water. 6. The composition of claim 1 , wherein the technical lignin comprises kraft lignin, a lignosulfate, alkali lignin, low sulfonate alkali lignin, or a combination thereof. 7. A method comprising: i) contacting a technical lignin with an ionic liquid for at least about 3 hours to generate a solubilized material; ii) precipitating a fraction of the solubilized material with a polar solvent to generate a precipitated fraction and a supernatant; iii) extracting monomeric lignin compounds from the supernatant with an extractant; and iv) separating the lignin compounds from the extractant; wherein the monomeric lignin compounds are selected from the group consisting of guaiacol, 4-ethyl guaiacol, 4-vinyl guaiacol, eugenol, syringol, 4-(1-propenyl) guaiacol, vanillin, allyl syringol, guaiacylacetone, and combinations thereof, and wherein the extractant is a non-polar solvent. 8. The method of claim 7 , wherein the ionic liquid is [C2mim][OAc]. 9. The method of claim 7 , wherein the contacting is performed at a temperature between about 100° C. and about 180° C. 10. The method of claim 7 , wherein the polar solvent comprises water. 11. The method of claim 7 , wherein the technical lignin comprises kraft lignin, a lignosulfate, alkali lignin, low sulfonate alkali lignin, or a combination thereof.
Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for (volatile compounds obtained by decomposition of spent liquors in order to regenerate them D21C11/125; compounds obtained by fractionating the liquors in order to regenerate them D21C11/0042) · CPC title
with organic solvents {or in solvent environment} · CPC title
Low-molecular-weight derivatives of lignin (high-molecular-weight derivatives of lignin {C08H6/00}) · CPC title
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