IP Library Granted Patent US 10,808,328
Granted Patent B2
US 10,808,328 · App. 16/062,747 · Granted Oct 20, 2020

Selective oxidation of furan based alcohols via electro-generative process

Inventors: Mengjia Wu (Shanghai, CN); Pascal Metivier (Shanghai, CN); Peng Li (Shanghai, CN); Armin T. Liebens (Brussels, BE)
Assignee: RHODIA OPERATIONS
C25B3/02C25B5/00C25B9/08H01M4/92H01M8/06H01M8/1004H01M8/1009H01M2008/1095H01M2250/00Y02P70/56
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Quick Facts
Patent No.
US 10,808,328
App. No.
16/062,747
Granted
Oct 20, 2020
Kind
B2
Abstract

This invention concerns a method for the production of at least a furanic compound having at least one aldehyde function and electrical power, by oxidizing at least a furanic compound having at least one hydroxyl function.

Claims (14)

1. A process for the production of a furanic compound having at least one aldehyde function and electrical power, by oxidizing a furanic compound having at least one hydroxyl function, wherein the oxidizing is performed in an electro-generative device having an anode, a cathode and a separator, wherein the furanic compound having at least one hydroxyl function is an anode reactant and an oxidant is a cathode reactant.

2. The process according to claim 1 , wherein the furanic compound having at least one hydroxyl function is selected from a group consisting of furfuryl alcohol, hydroxymethylfurfural, bis(hydroxymethyl)furan, 5-methoxymethylfurfuryl alcohol, 5-hydroxymethylfurancarb oxylic acid, and bis(5-hydroxymethylfuranmethyl) ether.

3. The process according to claim 1 , wherein the furanic compound having at least one aldehyde function is selected from a group consisting of furfural, hydroxymethylfurfural, 2,5-furandicarbaldehyde, 5-methoxymethylfurfural, 5-formylfurancarboxylic acid and bis(5-formylmethylfurnmethyl) ether.

4. The process according to claim 1 , wherein the electro-generative device is a fuel cell or H-shape cell.

5. The process according to claim 1 , wherein the anode and cathode comprise a catalyst, said catalyst being Pt.

6. The process according to claim 1 , wherein the anode and cathode comprise at least one catalyst selected from a group consisting of Ru, Rh, Au, Pd, Pt, Ir, Ta, Ni, Ag, Cu, Fe, Mn, Cr, Ti, Co, Zn, Zr, Y, Ce, Al N, and P.

7. The process according to claim 1 , wherein the anode and cathode comprises catalysts applied to a support.

8. The process according to claim 1 , wherein an electric potential is generated and is between 0.001-0.5V.

9. The process according to claim 1 , wherein the furanic compound having at least one hydroxyl function is dissolved in a solvent with a concentration between 0.01 mol/L to 5 mol/L.

10. The process according to claim 1 , wherein the oxidizing is performed for 15-45 hours.

11. The process according to claim 1 , wherein the furanic compound having at least one hydroxyl function is dissolved in a solvent with a pH between 0.01-7.

12. The process according to claim 1 , wherein the oxidizing is performed at a temperature between 10-200° C.

13. The process according to claim 1 , wherein the separator is Nafion proton exchange membrane.

14. The process according to claim 13 , wherein the thickness of membrane is between 100-300 μm.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 26, 2024
From: RHODIA OPERATIONS
To: SPECIALTY OPERATIONS FRANCE
Reel/Frame 066374/0642 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 18, 2018
From: WU, MENGJIA; METIVIER, PASCAL; LI, PENG; LIEBENS, ARMIN T.
To: RHODIA OPERATIONS
Reel/Frame 046117/0554 →