Method and a system for producing glycolic acid and/or glycolate
A method and a system for producing glycolic acid and/or glycolate from sustainable resources. A method for catalytic production of glycolic acid and/or glycolate including the step of: oxidation of a starting material including between 0.1-100 wt/wt % glycolaldehyde at a temperature of between −10° C. and 100° C. with an oxidant in the presence of a metal-based catalyst including a catalytically active metal, which is selected from the group of palladium and platinum; or mixtures thereof.
1. A method for catalytic production of glycolic acid comprising the steps of: obtaining a C 1 -C 3 oxygenate mixture, wherein the C 1 -C 3 oxygenate mixture originates from thermal fragmentation of at least one carbohydrate, wherein the C 1 -C 3 oxygenate mixture comprises 10 wt % to 95 wt % of glycolaldehyde, 0.1 wt % to 60 wt % of formaldehyde, and 0.1 wt % to 80 wt % pyruvaldehyde and oxidizing the C 1 -C 3 oxygenate mixture at a temperature of between −10° C. and 100° C. with an oxidant in the presence of a metal-based catalyst comprising a catalytically active metal, which is selected from the group consisting of palladium, platinum, and mixtures thereof.
2. The method according to claim 1 , wherein the C 1 -C 3 oxygenate mixture further comprises at least one of the following: acetol in an amount of 0.1-80 wt/wt %, and/or glyoxal in an amount of 0.1-80 wt/wt %.
3. The method according to claim 1 , wherein the C 1 -C 3 oxygenate mixture further comprises a solvent selected from the group consisting of water, methanol, ethanol, and mixtures thereof.
4. The method according to claim 1 , wherein the metal-based catalyst comprises one or more further catalytically active metals, and at least 50 wt/wt % of the catalytically active metals of the metal based catalyst is selected from the group consisting of palladium, platinum, and mixtures thereof.
5. The method according to claim 1 , wherein the metal-based catalyst further comprises catalytically active gold.
6. The method according to claim 1 , wherein the metal-based catalyst does not comprise catalytically active gold.
7. The method according to claim 1 , wherein the metal-based catalyst comprises platinum dispersed on a support of active carbon.
8. The method according to claim 1 , wherein the oxidation is performed at a temperature between −10° C. and 100° C.
9. The method according to claim 1 , wherein the oxidant is selected from the group consisting of oxygen, hydrogen peroxide, and mixtures thereof.
10. The method according to claim 1 , wherein the oxidant is oxygen and the oxidation is performed at a O 2 partial pressure between 0.1-40 bar.
11. The method according to claim 1 , wherein the at least one carbohydrate is a mono- and/or di-saccharide(s).
12. The method according to claim 1 , wherein the oxidation step is followed by isolation, and optionally further purification, of glycolic acid.
13. The method according to claim 12 , wherein the isolation is performed by precipitating glycolic acid.
14. The method according to claim 12 , wherein glycolic acid is isolated in the form of a salt via precipitation.
15. The method according to claim 14 , wherein the precipitation is performed by reacting glycolic acid with a base to form glycolate.
16. The method according to claim 11 , wherein the mono- and/or di-saccharide(s) is selected from the group consisting of sucrose, lactose, xylose, arabinose, ribose, mannose, tagatose, galactose, glucose, fructose, and mixtures thereof.
17. The method according to claim 1 , wherein glycolic acid is produced in yields ranging from 30-90%.
18. The method according to claim 1 , wherein the C 1 -C 3 oxygenate mixture further comprises acetol.
19. The method according to claim 1 , wherein the C 1 -C 3 oxygenate mixture further comprises glyoxal.