Electrochemical carbon oxides reduction to ethylene

Patent metadata

Field	Value
Publication number	US-2024417863-A1
Application number	US-202318723935-A
Country	US
Kind code	A1
Filing date	Jan 3, 2023
Priority date	Jan 10, 2022
Publication date	Dec 19, 2024
Grant date	—

Abstract

The invention relates to a process for electrolyzing carbon oxides selected from carbon monoxide and/or carbon dioxide into ethylene by means of an electrolyser comprising a cathode catalyst being a dendritic copper oxide catalyst or a dendritic copper catalyst.

First claim

1 - 28 . (canceled)

29 . Process for electrolysing one or more carbon oxides into one or more hydrocarbons characterized in that it comprises the following steps:
b) preparing a cathode catalyst by electrodeposition of Cu on a Cu electrode from an acidic CuSO 4 solution; c) providing an electrolyser comprising a gas diffusion cathode, an anode and an ion-exchange membrane in between said gas diffusion cathode and said anode, wherein the electrolyser is selected from a zero-gap electrolyser, a two-gaps electrolyser, a catholyte-free one-gap electrolyser and a catholyte-containing one-gap electrolyser, and wherein the ion-exchange membrane is an anion-exchange membrane or a bipolar membrane; d) providing an input flow at the gas diffusion cathode, the input flow comprising one or more carbon oxides selected from carbon monoxide or a mixture of carbon monoxide and carbon dioxide; e) providing an anolyte solution at the anode and optionally a catholyte solution at the gas diffusion cathode; f) applying an electric current between the gas diffusion cathode and the anode; and g) recovering, at the gas diffusion cathode, an output flow comprising one or more hydrocarbons comprising ethylene:
and in that step (b) of preparing a cathode catalyst by electrodeposition of Cu comprises a calcination sub-step performed at a temperature of at least 300° C. to obtain a dendritic copper oxide catalyst and the electrolyser provided at step (c) further comprises a first interface in between the gas diffusion cathode and the ion-exchange membrane, wherein the first interface comprises a cathode catalyst being a dendritic copper oxide catalyst.

30 . The process according to claim 29 , characterized in that the anode comprises an anode catalyst that is or comprises one or more selected from IrO 2 , nickel foam and nickel-iron oxide.

31 . The process according to claim 29 , characterized in that the acidic CuSO 4 solution contains CuSO 4 at a concentration ranging from 0.05 to 0.5 M and H 2 SO 4 at a concentration ranging from 0.5 to 3.0 M.

32 . The process according to claim 29 , characterized in that step (b) of preparing a cathode catalyst by electrodeposition of Cu is performed at a current ranging from 0.05 A·cm −2 to 5.0 A·cm −2 for a time ranging from 20 to 500 seconds.

33 . The process according to claim 29 characterized in that the cathode catalyst is a dendritic copper oxide catalyst and comprises CuO (111) as determined by XRD.

34 . The process according to claim 29 , characterized in that the cathode catalyst is a porous dendritic material and shows pores with a pore size ranging from 100 nm and 500 μm.

35 . The process according to claim 29 , characterized in that the cathode catalyst is selected to have an electroactive surface area ranging from 15 cm 2 cm −2 to 25 cm 2 cm −2 .

36 . The process according to claim 29 , characterized in that the electric current applied between the gas diffusion cathode and the anode at step (f) has a current density ranging from 25 mA/cm 2 to 300 mA/cm 2 .

37 . The process according to claim 29 , characterized in that the anolyte solution provided at step (e) is an aqueous solution of one or more alkaline compounds wherein the one or more alkaline compounds are selected from KOH, NaOH, Ca(OH) 2 , LiOH, Mg(OH) 2 , RbOH, CsOH and any mixture thereof.

38 . The process according to claim 29 , characterized in that the anolyte solution provided at step (e) is an aqueous solution of one or more alkaline compounds and the concentration of the one or more alkaline compounds in said aqueous solution is ranging from 0.1 M to 7.0 M: with preference from 1.0 to 5.0 M.

39 . The process according to claim 29 , characterized in that the catholyte solution provided at step (e) is an aqueous solution of one or more alkaline compounds wherein the one or more alkaline compounds are selected from KOH, NaOH, Ca(OH) 2 , LiOH, Mg(OH) 2 , RbOH, CsOH and any mixture thereof.

40 . The process according to claim 29 , characterized in that the catholyte solution provided at step (e) is an aqueous solution of one or more alkaline compounds the concentration of the one or more alkaline compounds in said aqueous solution is ranging from 0.1 M to 7.0 M: with preference from 1.0 to 5.0 M.

41 . The process according to claim 29 , characterized in that the process is a tandem carbon dioxide electroreduction process and comprises a step (a) of providing a feedstream comprising carbon dioxide and performing a preliminary conversion of at least a part of the carbon dioxide of said feedstream into carbon monoxide to obtain an input flow comprising at least 1 mol. % of carbon monoxide based on the total molar content of the carbon oxides present in the input flow wherein said input flow is the one provided in step (d).

42 . The process according to claim 41 , characterized in that the conversion of carbon dioxide into carbon monoxide is performed through an electoreduction reaction or a water-gas shift reaction.

43 . The process according to claim 41 , characterized in that the conversion of carbon dioxide into carbon monoxide is performed through an electoreduction reaction or a water-gas shift reaction, to obtain an input flow comprising at least 60 mol. % of carbon monoxide based on the total molar content of the carbon oxides present in the input flow.

44 . The process according to claim 29 , characterized in that the electric current that is applied at step (f) has an electric potential which is ranging from 2.5 V to 4.5 V.

45 . The process according to claim 29 , characterized in that the input flow provided in step (d) comprises one or more carbon oxides selected from carbon monoxide or a mixture of carbon monoxide and carbon dioxide, wherein the input flow comprises carbon monoxide at a content of at least 1 mol. % of carbon monoxide based on the total molar content of the carbon oxides present in the input flow.

46 . The process according to claim 29 , characterized in that the input flow comprises carbon monoxide at a content of at least 60 mol. % of carbon monoxide based on the total molar content of the carbon oxides present in the input flow.

47 . The process according to claim 29 , characterized in that the input flow provided in step (d) comprises carbon monoxide at a content of at least 80 mol. % of carbon monoxide based on the total molar content of the carbon oxides present in the input flow.

48 . The process according to claim 29 , characterized in that the electrolyser is a zero-gap electrolyser or a two-gaps electrolyser.

Assignees

• Totalenergies Onetech
• College France

Inventors

• Schreiber Moritz Wilhelm
• Duong Hong-Phong
• Tran Ngoc Huan
• Fontecave Marc

Classifications

• C25D5/50

  by heat-treatment · CPC title

• C25D3/38

  of copper · CPC title

• C23C28/345

  with at least one oxide layer · CPC title

• C23C28/32

  including at least one pure metallic layer · CPC title

• C23C8/10

  Oxidising · CPC title