Method for producing an active layer of an electrode for electrochemical reduction reactions

Patent metadata

Field	Value
Publication number	US-2022010439-A1
Application number	US-201917295206-A
Country	US
Kind code	A1
Filing date	Nov 19, 2019
Priority date	Nov 30, 2018
Publication date	Jan 13, 2022
Grant date	—

Abstract

A process for the preparation of a catalytic material of an electrode for electrochemical reduction reactions, said material comprising an active phase based on at least one metal from group VIb and an electroconductive support, which process is carried out according to at least the following stages:a stage of bringing said support into contact with at least one solution containing at least one precursor of at least one metal from group VIb;a drying stage at a temperature of less than 250° C., without a subsequent calcination stage;a stage of sulfurization at a temperature of between 100° C. and 600° C.

First claim

1 . A process for the preparation of a catalytic material of an electrode for electrochemical reduction reactions, said material comprising an active phase based on at least one metal from group VIb and an electroconductive support, which process is carried out according to at least the following stages:
a) a stage of bringing said support into contact with at least one solution containing at least one precursor of at least one metal from group VIb; b) optionally a stage of bringing the support into contact with an organic additive, it being understood that stage b) is obligatory when said precursor of at least one metal from group VIb according to stage a) is chosen from polyoxometallates corresponding to the formula (H h X x M m O y ) q− in which H is hydrogen, X is an element chosen from phosphorus (P), silicon (Si), boron (B), nickel (Ni) and cobalt (Co), M is one or more metal(s) chosen from molybdenum (Mo), tungsten (W), nickel (Ni), cobalt (Co) and iron (Fe), 0 being oxygen, h being an integer between 0 and 12, x=0, m being an integer equal to 5, 6, 7, 8, 9, 10, 11, 12 and 18, y being an integer between 17 and 72 and q being an integer between 1 and 20, it being understood that M is not a nickel atom, a cobalt atom or an iron atom alone. stages 1) and 2), if both carried out, being carried out in any order or simultaneously; c) a drying stage on conclusion of stage a), optionally of the sequence of stages a) and b) or b) and a), at a temperature of less than 250° C., without a subsequent calcination stage; d) a stage of sulfurization of the material obtained on conclusion of stage c) at a temperature of between 100° C. and 600° C.

2 . The process as claimed in claim 1 , in which said precursor of at least one metal from group VIb is chosen from polyoxometallates corresponding to the formula (H h X x M m O y ) q− in which H is hydrogen, X is an element chosen from phosphorus (P), silicon (Si), boron (B), nickel (Ni) and cobalt (Co), said element being taken alone, M is one or more element(s) chosen from molybdenum (Mo), tungsten (W), nickel (Ni), cobalt (Co) and iron (Fe), O being oxygen, h being an integer between 0 and 12, x being an integer between 0 and 4, m being an integer equal to 5, 6, 7, 8, 9, 10, 11, 12 and 18, y being an integer between 17 and 72 and q being an integer between 1 and 20; salts of precursors of the elements from group VIb, such as molybdates, thiomolybdates, tungstates or also thiotungstates; organic or inorganic precursors based on Mo or W, such as MoCl 5 or WCl 4 or WCl 6 , and Mo or W alkoxides.

3 . The process as claimed in claim 1 , in which the m atoms M are either solely molybdenum (Mo) atoms, or solely tungsten (W) atoms, or a mixture of molybdenum (Mo) and tungsten (W) atoms, or a mixture of molybdenum (Mo) and cobalt (Co) atoms, or a mixture of molybdenum (Mo) and nickel (Ni) atoms, or a mixture of tungsten (W) and nickel (Ni) atoms.

4 . The process as claimed in claim 1 , in which the m atoms M are either a mixture of nickel (Ni), molybdenum (Mo) and tungsten (W) atoms or a mixture of cobalt (Co), molybdenum (Mo) and tungsten (W) atoms.

5 . The process as claimed in claim 1 , comprising an additional stage of introduction of at least one promoter comprising at least one metal from group VIII by a stage of bringing said support into contact with at least one solution containing at least one precursor of at least one metal from group VIII.

6 . The process as claimed in claim 1 , in which a maturation stage is carried out after stage a) and/or b) but before stage c), at a temperature of between 10° C. and 50° C. for a period of time of less than 48 hours.

7 . The process as claimed in claim 1 , in which the drying stage c) is carried out at a temperature of less than 180° C.

8 . The process as claimed in claim 1 , in which, when the precursor of the catalytic material comprises at least one metal from group VIb and at least one metal from group VIII, the sulfurization temperature in stage d) is between 350° C. and 550° C.

9 . The process as claimed in claim 1 , in which, when the precursor of the catalytic material comprises solely a metal from group VIb, the sulfurization temperature in stage d) is between 100° C. and 250° C. or between 400° C. and 600° C.

10 . The process as claimed in claim 1 , in which the organic additive is chosen from:
chelating agents, nonchelating agents, reducing agents or nonreducing agents; mono-, di- or polyalcohols, carboxylic acids, sugars, noncyclic mono-, di- or polysaccharides, esters, ethers, crown ethers, cyclodextrins and organic compounds containing sulfur or nitrogen.

11 . The process as claimed in claim 1 , in which the support comprises at least one material chosen from carbon structures of carbon black, graphite, carbon nanotubes or graphene type.

12 . The process as claimed in claim 1 , in which the support comprises at least one material chosen from gold, copper, silver, titanium or silicon.

13 . An electrode, characterized in that it is formulated by a preparation process comprising the following stages:
1) at least one ionic conductive polymer binder is dissolved in a solvent or a solvent mixture; 2) at least one catalytic material prepared according to claim 1 , in powder form, is added to the solution obtained in stage 1) in order to obtain a mixture; stages 1) and 2) being carried out in any order or simultaneously; 3) the mixture obtained in stage 2) is deposited on a metallic or metallic-type conductive support or collector.

14 . An electrolysis device comprising an anode, a cathode and an electrolyte, said device being characterized in that one at least of the anode or of the cathode is an electrode as claimed in claim 13 .

15 . A method for performing an electromechanical reaction, comprising performing said reaction by the electrolysis device according to claim 14 .

16 . The method as claimed in claim 15 , in which said device perform as:
water electrolysis device for the production of a gaseous mixture of hydrogen and oxygen and/or the production of hydrogen alone; carbon dioxide electrolysis device for the production of formic acid; nitrogen electrolysis device for the production of ammonia; fuel cell device for the production of electricity from hydrogen and oxygen.

Assignees

• Ifp Energies Now

Inventors

• Bonduelle-Skrzypczak Audrey
• Belaid Sofiane
• Leflaive Philibert
• Pirngruber Gerhard

Classifications

• H01M4/8878

  Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body · CPC title

• C25B11/077

  the compound being a non-noble metal oxide · CPC title

• C25B9/17

  Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof · CPC title

• C25B11/081 Primary

  the element being a noble metal · CPC title

• C25B11/063

  Valve metal, e.g. titanium · CPC title