Process for the facile electrosynthesis of graphene from co2

Patent metadata

Field	Value
Publication number	US-2022372634-A1
Application number	US-202217812510-A
Country	US
Kind code	A1
Filing date	Jul 14, 2022
Priority date	May 28, 2019
Publication date	Nov 24, 2022
Grant date	—

Abstract

The present invention relates to the production of graphene from CO2 through electrolysis and exfoliation processes. One embodiment is a method for producing graphene comprising (i) performing electrolysis between an electrolysis anode and an electrolysis cathode in a molten carbonate electrolyte to generate carbon nanomaterial on the cathode, and (ii) electrochemically exfoliating the carbon nanomaterial from a second anode to produce graphene. The exfoliating step produces graphene in high yield than thicker, conventional graphite exfoliation reactions. CO2 can be the sole reactant used to produce the valuable product as graphene. This can incentivize utilization of CO2, and unlike alternative products made from CO2 such as carbon monoxide or other fuels such as methane, use of the graphene product does not release this greenhouse gas back into the atmosphere.

First claim

1 - 36 . (canceled)

37 . A method for producing carbon nano-onions comprising:
(a) heating a carbonate electrolyte comprising an oxide additive to obtain a molten carbonate electrolyte; (b) disposing the molten carbonate electrolyte between an electrolysis anode and an electrolysis cathode in a cell, wherein the electrolysis anode and the molten carbonate electrolyte do not include a transition metal nucleating agent; (c) applying an electrical current to the electrolysis cathode and the electrolysis anode in the cell to electrolyze the carbonate and generate carbon nano-onions on the electrolysis cathode without the formation of transition metal nucleation sites on the cathode.

38 . The method of claim 37 , wherein the oxide additive comprises lithium oxide.

39 . A method for producing carbon nano-onions comprising:
(a) heating a carbonate electrolyte comprising an oxide additive to obtain a freshly melted carbonate electrolyte; (b) disposing the freshly melted carbonate electrolyte between an electrolysis anode and an electrolysis cathode in a cell, wherein the electrolysis anode and/or the molten carbonate electrolyte optionally further comprise a transition metal nucleation agent; (c) applying an electrical current to the electrolysis cathode and the electrolysis anode in the cell to electrolyze the freshly melted carbonate and generate carbon nano-onions on the electrolysis cathode, without the formation of transition metal nucleation sites on the cathode.

40 . The method of claim 39 , wherein the oxide additive comprises lithium oxide.

41 - 45 . (canceled)

46 . The method of claim 37 , wherein the conditions for electrolysis reduce the solubility of one or more transition metal nucleating agents.

47 . The method of claim 46 , wherein the transition metal nucleating agents for which solubility has been reduced are selected from nickel, chromium, iron, and any combination of any of the foregoing.

48 . The method of claim 46 , wherein the conditions for reducing the solubility of one or more transition metal nucleating agents during electrolysis include (a) an electrolyte comprising (i) a lithium carbonate and (ii) one or both of sodium carbonate and potassium carbonate, (b) decreasing the electrolysis temperature, (c) decreasing the concentration of lithium in the electrolyte, (d) increasing the electrolysis current density, or (e) any combination of any of the foregoing.

49 . The method of claim 37 , wherein the electrolyzed carbonate in step (c) is replenished by addition of carbon dioxide.

50 . The method of claim 49 , wherein the source of the added carbon dioxide is one of air, pressurized CO 2 , concentrated CO 2 , a power generating industrial process, an iron generating industrial process, a steel generating industrial process, a cement formation process, an ammonia formation industrial process, an aluminum formation industrial process, a manufacturing process, an oven, a smokestack, or an internal combustion engines.

51 . The method of claim 37 , wherein the electrolysis cathode comprises stainless steel, cast iron, a nickel alloy, a material that resists corrosion in the presence of the molten carbonate electrolyte, or any combination of the foregoing.

52 . The method of claim 37 , wherein the electrolysis cathode is coated with zinc.

53 . The method of claim 37 , wherein in step (c), electrical current is applied with stepwise increases.

54 . The method of claim 37 , wherein the molten carbonate electrolyte comprises an alkali metal carbonate, an alkali earth metal carbonate, or any combination thereof

55 . The method of claim 54 , wherein the alkali metal carbonate or alkali earth metal carbonate is lithium carbonate, sodium carbonate, potassium carbonate, rubidium carbonate, cesium carbonate, francium carbonate, beryllium carbonate, magnesium carbonate, calcium carbonate, strontium carbonate, barium carbonate, radium carbonate, or any mixture thereof.

56 . The method of claim 37 , wherein the molten carbonate electrolyte comprises lithium carbonate.

57 . The method of claim 37 , wherein the molten carbonate electrolyte further comprises one or more additional oxygen, sulfur, halide, nitrogen or phosphorous containing inorganic salts.

58 . The method of claim 37 , wherein the method results in a coulombic efficiency of greater than about 80%.

59 . The method of claim 37 , wherein the method results in a coulombic efficiency of about 100%.

60 . The method of claim 37 , wherein the electrolysis reaction is performed at a current density of between about 5 and about 1000 mA cm 2 .

61 . The method of claim 37 , wherein step (c) also produces molecular oxygen (O 2 ).

62 . The method of claim 37 , wherein transition metal nucleating agents are suppressed by performing the electrolysis in step (c) under conditions which reduce the solubility of one or more transition metal nucleating agents.

63 . The method of claim 62 , wherein the transition metal nucleating agents for which solubility has been reduced are selected from nickel, chromium, iron, and any combination of any of the foregoing.

64 . The method of claim 62 , wherein the conditions for reducing the solubility of one or more transition metal nucleating agents during electrolysis include (a) an electrolyte comprising (i) a lithium carbonate and (ii) one or both of sodium carbonate and potassium carbonate, (b) decreasing the electrolysis temperature, (c) decreasing the concentration of lithium in the electrolyte, (d) increasing the electrolysis current density, or (e) any combination of any of the foregoing.

65 . The method of claim 39 , wherein the method further comprises electrochemically exfoliating the carbon nano-onions to produce graphene.

Assignees

• C2Cnt Llc

Inventors

• Licht Stuart

Classifications

• C25B1/135 Primary

  Carbon · CPC title

• C25B11/075

  consisting of a single catalytic element or catalytic compound · CPC title

• C25B15/021

  of heating or cooling · CPC title

• C25B9/09

  Fused bath cells · CPC title

• C25B11/057

  consisting of a single element or compound · CPC title