Hydroxide catalysts for lignin depolymerization
US-9790249-B2 · Oct 17, 2017 · US
US11123711B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11123711-B2 |
| Application number | US-201816234950-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 28, 2018 |
| Priority date | Dec 28, 2017 |
| Publication date | Sep 21, 2021 |
| Grant date | Sep 21, 2021 |
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The invention herein concerns a catalyst of gold particles on a layered double hydroxide (LDH) that assists in oxidation of alcohols in lignins. In some embodiments, the LDH comprises lithium and aluminum metals. Also considered are methods of using the catalyst to oxidize lignins and methods of preparing the catalyst.
Opening claim text (preview).
We claim: 1. A system for alcohol oxidation reaction on lignins comprising a lignin-containing biomass in contact with a catalyst for lignin depolymerization including gold nanoparticles dispersed and supported_on a layered double hydroxide (LDH), wherein the gold nanoparticles are of less than 10 nm in diameter and the catalyst is under molecular oxygen. 2. The system of claim 1 , wherein the system further comprises an oxygen source for the reaction. 3. The system of claim 2 , wherein the oxygen source is air, gaseous oxygen, or hydrogen peroxide. 4. A method for oxidizing alcohols in lignin comprising contacting a lignin-containing biomass substrate with a catalyst under molecular oxygen in a reactor vessel, wherein said catalyst includes gold nanoparticles dispersed and supported_on a layered double hydroxide (LDH), wherein the gold nanoparticles are of less than 10 nm in diameter. 5. The method of claim 4 , wherein the lignin-biomass comprises an extracted lignin-containing product from a lignocellulosic biomass. 6. The method of claim 4 , wherein the lignin containing biomass comprises a lignocellulosic biomass. 7. The method of claim 4 , wherein the reactor vessel is at a temperature of between 20 and 250° C. 8. The method of claim 4 , further comprising a hydrolysis step with an acid or a base after oxidation of the lignin-biomass. 9. The method of claim 4 , wherein in the reactor vessel receives an oxygen source. 10. The method of claim 4 , wherein the reactor vessel has an O 2 partial pressure of between 0.1 and 100 atm. 11. The method of claim 4 , further comprising a solvent in the reactor vessel. 12. The method of claim 11 , wherein the solvent is selected from the group of N,N-dimethyl formamide (DMF), dimethyl acetamide (DMAC), 1,2-dimethoxyethane, 2-ethyoxyethanol, 2-methoxyethanol, diglyme, polyols, ionic liquids, diphenyl ether, water, γ-valerolactone, alcohols, pyridine, 1,4-dioxane, tetrahydrofuran, dimethyl sulfoxide (DMSO), and mixtures thereof. 13. The method of claim 4 , wherein the catalyst is in contact with the substrate for a period of between 1 minute and 72 hours.
Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title
having a two-dimensional [2D] layered crystalline structure, e.g. layered double hydroxide [LDH] · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
Nanoparticles · CPC title
Metal or metal oxide crystallite size · CPC title
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