Electrochemical reaction device
US-2016376713-A1 · Dec 29, 2016 · US
US2022372643A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022372643-A1 |
| Application number | US-202217740193-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 9, 2022 |
| Priority date | May 10, 2021 |
| Publication date | Nov 24, 2022 |
| Grant date | — |
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There is provided a catalytic system including a fibrous hydrophobic substrate, a first layer having a first layer thickness including copper or copper alloy nanoparticles covering the polymeric substrate, and a second layer having a second layer thickness over the first layer and including amorphous nitrogen-doped carbon, wherein the catalytic system includes confined interlayer spaces defined by regions where the first layer and the second layer are spaced apart from each other. The catalytic system can be used for catalyzing the electrochemical reduction of carbon dioxide, carbon monoxide, or a combination thereof. Thus, there is also provided a method for the electrochemical reduction of carbon dioxide, carbon monoxide, or a combination thereof, using the catalytic system.
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1 . A catalytic system comprising a fibrous hydrophobic substrate, a first layer having a first layer thickness comprising copper or copper alloy nanoparticles covering the polymeric substrate, and a second layer having a second layer thickness over the first layer and comprising amorphous nitrogen-doped carbon, wherein the catalytic system comprises confined interlayer spaces defined by regions where the first layer and the second layer are spaced apart from each other. 2 . The catalytic system of claim 1 , wherein the fibrous hydrophobic substrate comprises polymeric nanofibers, carbon nanofibers, or a combination thereof. 3 . The catalytic system of claim 1 , wherein the fibrous hydrophobic substrate comprises at least one fluoropolymer. 4 . The catalytic system of claim 1 , wherein the fibrous hydrophobic substrate comprises polytetrafluoroethylene (PTFE). 5 . The catalytic system of claim 1 , wherein the fibrous hydrophobic substrate comprises a nanofibers membrane. 6 . The catalytic system of claim 1 , wherein the fibrous hydrophobic substrate comprises a nanofibers membrane having a pore size ranging from about 200 nm to about 700 nm. 7 . The catalytic system of claim 1 , wherein the fibrous hydrophobic substrate comprises nanofibers having a diameter ranging from about 50 nm to about 200 nm. 8 . The catalytic system of claim 1 , wherein the first layer thickness is from about 100 nm to about 500 nm and the second layer thickness is from about 20 nm to about 100 nm. 9 . The catalytic system of claim 1 , wherein the copper or copper alloy nanoparticles have a diameter ranging from about 20 nm to about 100 nm. 10 . The catalytic system of claim 1 , wherein in the second layer, the amorphous nitrogen-doped carbon comprises electron-donating nitrogen atoms. 11 . The catalytic system of claim 1 , wherein an atomic percentage of nitrogen in the second layer is from about 3% to about 50%. 12 . The catalytic system of claim 1 , wherein the second layer comprises pyridinic-N, pyrrolic-N and graphitic-N. 13 . The catalytic system of claim 11 , wherein a content of pyridinic-N is higher than a content of pyrrolic-N or graphitic-N. 14 . The catalytic system of claim 1 , wherein the second layer comprises pyridinic-N in an atomic percentage from about 10% to about 21%. 15 . The catalytic system of claim 1 , wherein the second layer comprises a plurality of pores extending through the second layer thickness. 16 . The catalytic system of claim 15 , wherein the pores in the second layer have an average diameter from about 5 nm to about 20 nm. 17 . The catalytic system of claim 1 , wherein the first layer and the second layer are spaced apart from each other in the confined interlayer spaces by a distance that is about 1 nm or below. 18 . A membrane electrode assembly system comprising a cathode side and an anode side, wherein the cathode side comprises the catalytic system as defined in claim 1 . 19 . A method for electrochemical reduction of carbon dioxide, carbon monoxide, or a combination thereof, comprising: contacting a reactant gas comprising carbon dioxide, carbon monoxide, or a combination thereof, in the presence of an electrolyte, with a cathode comprising the catalytic system as defined in claim 1 ; applying a voltage to provide a current density to cause the carbon dioxide, carbon monoxide, or the combination thereof, in the reactant gas contacting the cathode, to be electrochemically reduced. 20 . A method for electrochemical production of ethanol from carbon dioxide, carbon monoxide, or a combination thereof, comprising: contacting a reactant gas comprising carbon dioxide, carbon monoxide, or a combination thereof, in the presence of an electrolyte, with a cathode comprising the catalytic system as defined in claim 1 ; applying a voltage to provide a current density to cause the carbon dioxide, carbon monoxide, or the combination thereof in the reactant gas contacting the cathode, to be electrochemically converted into ethanol. 21 . A process for producing a catalytic system as defined in claim 1 , comprising: sputtering copper or the copper alloy onto the fibrous hydrophobic substrate to form the first layer; and sputtering the nitrogen-doped carbon onto the first layer to form the second layer.
of carbon dioxide · CPC title
Deposition of organic layers from vapour phase (vapour phase deposition in general C23C14/00, C23C16/00) · CPC title
Oxygen containing compounds · CPC title
Alloys · CPC title
characterised by the substrate or carrier material · CPC title
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