Methods to convert lignin to phenolic and carboxylate compounds
View Patent ↗A method of converting lignin to phenolic compounds and dicarboxylates in high yield is described. The method involves the use of peroxy acids to react with lignin at a moderated treatment conditions. The peroxy acids can be used along or in combination of other catalysts that have the capability to lower the molecular weight of lignin. A phenolic compounds yield is achieved (>60%) and these phenolic compounds represents high value precursors for various applications include but not limited to antioxidants, health improvement agents, anticorrosive agents, liquid fuel components and performance enhancing agents, resin and adhesives. Dicarboxylic acids can be used for polymer applications or hydrodeoxygenation to hydrocarbon fuel.
1. A process comprising:
oxidatively depolymerizing a lignin with a peroxy acid at a temperature of not less than about 5° C. to not greater than about 160° C. to yield a mixture of dicarboxylic acid compounds and a mixture of phenolic compounds, wherein the mixture of dicarboxylic acid compounds is in at least about 10% total weight yield, wherein the total weight yield is calculated from the lignin on a contained lignin basis.
2. The process of claim 1 , wherein the mixture of phenolic compounds is in at least about 28% the total weight yield.
3. The process of claim 1 , further comprising:
substantially separating one or more dicarboxylic acid compounds or combination thereof from the mixture of phenolic compounds;
reducing at least one of the dicarboxylic acid compounds to a saturated dicarboxylic acid; and
recovering the one or more dicarboxylic acids or combination thereof in at least about 10% the total weight yield.
4. The process of claim 1 , further comprising:
substantially separating one or more dicarboxylic acid compounds or combination thereof from the mixture of phenolic compounds;
esterifying at least one of the dicarboxylic acid compounds to a dicarboxylate ester; and
recovering one or more dicarboxylate esters or combination thereof in at least about 10% the total weight yield.
5. The process of claim 1 , wherein the mixture of phenolic compounds is in at least about 60% the total weight yield.
6. The process of claim 1 , wherein the mixture of dicarboxylic acid compounds is at least about 25% the total weight yield.
7. The process of claim 1 , wherein the lignin is an alkaline lignin.
8. The process of claim 1 , wherein the oxidatively depolymerizing the lignin with the peroxy acid comprises oxidatively depolymerizing at the temperature of not less than about 40° C. to not greater than about 120° C.
9. The process of claim 1 , wherein the oxidatively depolymerizing the lignin with the peroxy acid comprises oxidatively depolymerizing for at least 3 hours.
10. The process of claim 1 , wherein the peroxy acid comprises peracetic acid, performic acid, or combinations thereof.
11. The process of claim 1 , wherein the peroxy acid is a peroxyaryloic acid.
12. The process of claim 1 , wherein the peroxy acid is a peroxybenzoic acid.
13. The process of claim 1 , wherein the peroxy acid is selected from the group consisting of metachloro-peroxybenzoic acid, peroxymonosulfuric acid, and peroxysulfonic acid.
14. The process of claim 1 , wherein the peroxy acid is generated in-situ from an organic acid and hydrogen peroxide.
15. The process of claim 1 , wherein the mixture of phenolic compounds comprises vanillin, vanillic acid, and gallic acid.
16. The process of claim 4 , wherein recovering the one or more dicarboxylate esters comprises recovering a dicarboxylate ester fraction comprising a dialkyl muconate, a dialkyl succinate, a dialkyl maleate, or a combination thereof.