Electrochemical conversion of organic waste

Patent metadata

Field	Value
Publication number	US-12163239-B2
Application number	US-202218279611-A
Country	US
Kind code	B2
Filing date	Mar 4, 2022
Priority date	Mar 5, 2021
Publication date	Dec 10, 2024
Grant date	Dec 10, 2024

Abstract

The present disclosure refers to a method of electrochemical conversion of organic waste to organic acid and hydrogen, comprising the steps of: (i) subjecting organic waste to ball milling under alkaline or acidic conditions to obtain pre-treated organic waste; (ii) introducing the pre-treated organic waste to a first compartment of an electrochemical cell, wherein the electrochemical cell comprises: the first compartment containing a nickel-based anode, a second compartment containing a cathode, and an electrolyte; and (iii) applying an electrical potential between the anode and the cathode, thereby producing organic acid at the anode, and hydrogen at the cathode. The present disclosure also refers to an organic acid or hydrogen produced from the method disclosed herein.

First claim

The invention claimed is:

1. A method of electrochemical conversion of organic waste to organic acid and hydrogen, comprising the steps of:
(i) subjecting organic waste to ball milling under alkaline or acidic conditions to obtain pre-treated organic waste;
(ii) introducing the pre-treated organic waste to a first compartment of an electrochemical cell, wherein the electrochemical cell comprises:
the first compartment containing a nickel-based anode,
a second compartment containing a cathode, and
an electrolyte; and

(iii) applying an electrical potential between the anode and the cathode, thereby producing organic acid at the anode, and hydrogen at the cathode.

2. The method of claim 1 , wherein the organic waste is selected from the group consisting of sludge optionally selected from the group consisting of waste activated sludge (WAS), food waste, sewage sludge, and sludge treated with thermal hydrolysis process (THP); woody biomass optionally selected from the group consisting of woody plants, cardboard, paper, and packaging material; food waste; horticulture waste; and shellfish optionally selected from the group consisting of shells containing chitin, prawn shells, lobster shells, crab shells, crayfish shells, clam shells, mussel shells, and yabbie shells.

3. The method of claim 1 , wherein the organic waste comprises lignin, cellulose, polysaccharide, and/or chitin.

4. The method of claim 1 , wherein the organic acid is selected from the group consisting of acetic acid, propanoic acid, formic acid, lactic acid, and benzoic acid.

5. The method of claim 1 , wherein the ball milling is performed at a speed of about 500 rpm to about 2000 rpm.

6. The method of claim 1 , wherein step (i) comprises subjecting the organic waste to ball milling with alkali, wherein the alkali is NaOH or KOH, optionally wherein the ratio of organic waste to alkali is in the range of about 4:1 to about 1:2.

7. The method of claim 1 , wherein step (i) comprises subjecting the organic waste to ball milling with acid, wherein the acid is kaolinite.

8. The method of claim 1 , wherein step (i) further comprises solubilising the ball-milled organic waste in water to obtain a solubilised mixture, and centrifuging the solubilised mixture to obtain the pre-treated organic waste as supernatant.

9. The method of claim 1 , wherein step (i) comprises ball milling with zirconia milling balls.

10. The method of claim 1 , wherein the organic waste is ball milled for at least 4 hours.

11. The method of claim 1 , wherein the ball milling is performed at a temperature in the range of about 20° C. to about 70° C.

12. The method of claim 1 , wherein step (ii) further comprises dissolving the pre-treated organic waste in NaOH or KOH solution.

13. The method of claim 1 , wherein the nickel-based anode is hp-Ni/NF and/or wherein the cathode is selected from the group consisting of nickel compounds such as nickel sulfide, and nickel phosphide.

14. The method of claim 1 , wherein the first compartment and second compartment are not separated.

15. The method of claim 1 , wherein the first compartment and second compartment are separated by an anion exchange membrane.

16. The method of claim 1 , wherein the electrolyte is NaOH or KOH.

17. The method of claim 1 , wherein step (ii) further comprises introducing a solution comprising a nitrate salt to the second compartment containing the cathode, optionally wherein the solution comprising the nitrate salt is a solution obtained from the first compartment containing the anode after step (ii), and wherein step (iii) further comprises producing an ammonium salt.

18. The method of claim 1 , wherein the electrical potential is derived from a stored energy source, or a renewable energy source, optionally wherein the renewable energy source is solar energy, wind power, or hydro power.

Assignees

• Univ Nanyang Tech

Inventors

• Li Hong
• Zhao Hu
• Lee Li Quan

Classifications

• C25B1/02

  Hydrogen or oxygen · CPC title

• C02F11/006 Primary

  Electrochemical treatment, e.g. electro-oxidation or electro-osmosis · CPC title

• B09B2101/70

  Kitchen refuse; Food waste · CPC title

• B09B3/35

  Shredding, crushing or cutting · CPC title

• B09B2101/85

  Paper; Wood; Fabrics, e.g. cloths · CPC title