Deep eutectic solvents, uses thereof, and method for preparing a lignin prepolymer based on the deep eutectic solvents
US-2023357537-A1 · Nov 9, 2023 · US
US2023331759A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023331759-A1 |
| Application number | US-202217722997-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 18, 2022 |
| Priority date | Apr 18, 2022 |
| Publication date | Oct 19, 2023 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A method for the recovery of lignin includes dissolving black liquor in solvent to form a mixture having a pH greater than or equal to about 12 to less than or equal to about 14. The pH of the mixture is then adjusted to greater than or equal to about 3 to less than or equal to about 7. The mixture is liquefacted, which includes increasing a temperature of the mixture to a target temperature, maintaining the target temperature for a period of time, and cooling the mixture to room temperature. Following liquefaction, the mixture is filtered to separate soluble and insoluble fractions of the mixture. The soluble fraction includes a lignin product having a polydispersity greater than or equal to about 1.78 to less than or equal to about 2.56.
Opening claim text (preview).
What is claimed is: 1 . A method for recovery of lignin, the method comprising: dissolving black liquor in solvent to form a mixture, wherein a pH of the mixture is greater than or equal to about 12 to less than or equal to about 14; adjusting the pH of the mixture to greater than or equal to about 3 to less than or equal to about 7; liquefacting the mixture, wherein liquefacting comprises: increasing a temperature of the mixture to a target temperature; maintaining the target temperature for a period of time; and cooling the mixture to room temperature; and filtering the mixture following liquefacting the mixture to separate soluble and insoluble fractions of the mixture, wherein the soluble fraction comprises a lignin product. 2 . The method according to claim 1 , wherein the solvent comprises methanol. 3 . The method according to claim 1 , wherein a mass ratio of the black liquor to the solvent in the mixture is greater than or equal to about 1:10 to less than or equal to about 1:5. 4 . The method according to claim 1 , wherein the step of adjusting the pH of the mixture is done using at least one of an organic acid and an inorganic acid. 5 . The method according to claim 1 , wherein the target temperature comprises a temperature greater than or equal to about 100° C. to less than or equal to about 200° C. 6 . The method according to claim 1 , wherein the period of time during the step of maintaining the target temperature is greater than or equal to about 1 minute to less than or equal to about 15 minutes. 7 . The method according to claim 1 , wherein a polydispersity of the lignin product is greater than or equal to about 1.78 to less than or equal to about 2.56. 8 . The method according to claim 1 , wherein the solvent is recycled after the step of filtering the mixture. 9 . A foam part for a vehicle comprising the lignin product recovered from the method according to claim 1 . 10 . A method for recovery of lignin, the method comprising: dissolving black liquor in solvent to form a mixture; adjusting a pH of the mixture to greater than or equal to about 3 to less than or equal to about 7; liquefacting the mixture, wherein liquefacting comprises: increasing a temperature of the mixture to a target temperature; maintaining the target temperature for a period of time; and cooling the mixture to room temperature; and filtering the mixture following liquefacting the mixture to separate soluble and insoluble fractions of the mixture, wherein the soluble fraction comprises a lignin product, wherein a polydispersity of the lignin product is greater than or equal to about 1.78 to less than or equal to about 2.56. 11 . The method according to claim 10 , wherein the solvent comprises methanol. 12 . The method according to claim 10 , wherein a mass ratio of the black liquor to the solvent in the mixture is greater than or equal to about 1:10 to less than or equal to about 1:5. 13 . The method according to claim 10 , wherein the step of adjusting of the pH of the mixture is done using at least one of an organic acid and an inorganic acid. 14 . The method according to claim 10 , wherein the target temperature comprises a temperature greater than or equal to about 100° C. to less than or equal to about 200° C. 15 . The method according to claim 10 , wherein the period of time during the step of maintaining the target temperature is greater than or equal to about 1 minute to less than or equal to about 15 minutes. 16 . A method for recovery of lignin, the method comprising: dissolving black liquor in methanol to form a mixture; adjusting a pH of the mixture to greater than or equal to about 3 to less than or equal to about 7 using at least one of an organic acid and an inorganic acid; liquefacting the mixture, wherein liquefacting comprises: increasing a temperature of the mixture to a target temperature; maintaining the target temperature for a period of time; and cooling the mixture to room temperature; and filtering the mixture following liquefacting the mixture to separate soluble and insoluble fractions of the mixture, wherein the soluble fraction comprises a lignin product. 17 . The method according to claim 16 , wherein a mass ratio of the black liquor to methanol in the mixture is greater than or equal to about 1:10 to less than or equal to about 1:5. 18 . The method according to claim 16 , wherein the target temperature comprises a temperature greater than or equal to about 100° C. to less than or equal to about 200° C. 19 . The method according to claim 16 , wherein the period of time during the step of maintaining the target temperature is greater than or equal to about 1 minute to less than or equal to about 15 minutes. 20 . The method according to claim 16 , wherein a polydispersity of the lignin product is greater than or equal to about 1.78 to less than or equal to about 2.56.
Low-molecular-weight derivatives of lignin (high-molecular-weight derivatives of lignin {C08H6/00}) · CPC title
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
Related publications grouped by family.
Answers are generated from the same data shown on this page.