Method for grafting polyphenols
US-2020032002-A1 · Jan 30, 2020 · US
US11066524B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11066524-B2 |
| Application number | US-201716338819-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 3, 2017 |
| Priority date | Oct 4, 2016 |
| Publication date | Jul 20, 2021 |
| Grant date | Jul 20, 2021 |
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The invention relates to a process for producing at least one alkoxylated polyphenol comprising the following successive steps:(a) reacting at least one polyphenol, at least one alkoxylating agent, at least one catalyst, in the presence of at least one alkoxylated polyphenol as a solvent, the polyphenol/polyphenol alkoxylated weight ratio as a solvent being less than 2, preferably less than or equal to 1.5, more preferably less than or equal to 1, even more preferably less than or equal to 0.5; and(b) removing the residual alkoxylating agent.
Opening claim text (preview).
The invention claimed is: 1. A process for producing at least one alkoxylated polyphenol comprising the following successive steps: (a) reacting at least one polyphenol, at least one alkoxylating agent and at least one catalyst in the presence of at least one alkoxylated polyphenol as a solvent, wherein the (polyphenol)/(alkoxylated polyphenol as a solvent) weight ratio ranges from 0.05 to 0.5 and the (polyphenol)/(alkoxylating agent) weight ratio ranges from 0.15 to 0.7; and (b) removing residual alkoxylating agent. 2. The process according to claim 1 , wherein the polyphenol is selected from natural tannins, lignins and polyphenols other than tannins and lignins. 3. The process according to claim 2 , wherein the polyphenol is a lignin. 4. The process according to claim 1 , wherein the alkoxylating agent has the following formula (I): wherein R 1 denotes a hydrogen atom or an alkyl radical in C 1 -C 6 . 5. The process according claim 1 , wherein the alkoxylating agent is selected from ethylene oxide, propylene oxide, butylene oxide, and mixtures thereof. 6. The process according to claim 1 , wherein the catalyst is selected from alkali metal hydroxides, sodium or potassium alkoxides, and tertiary amines selected from trialkylamines and tetramethylguanidine. 7. The process according to claim 1 , wherein the temperature in step (a) ranges from 70° C. to 200° C. 8. The process according to claim 1 , wherein the pressure during step (a) ranges from 0.1 to 1.8 MPa. 9. The process according to claim 1 , wherein it is carried out batchwise, semi-continuously or continuously. 10. The process according to claim 1 , comprising a step (c) of recovering the alkoxylated polyphenol obtained after step (b). 11. The process according to claim 1 , wherein the alkoxylated polyphenol produced by the process is identical to the alkoxylated polyphenol used as the solvent. 12. The process according to claim 1 , wherein the alkoxylated polyphenol produced by the process is different from the alkoxylated polyphenol used as the solvent.
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