Hydrocarbon-selective electrode

1. An electrode comprising:

a gas diffusion layer comprising a catalyst, the catalyst comprising a plurality of different tetragonally crystallized compounds, wherein each of the plurality of different tetragonally crystallized compounds comprises at least one element selected from Cu and Ag,

wherein the crystal lattice of each of the plurality of different tetragonally crystallized compounds belongs to the I4 1 /amd space group,

wherein each of the plurality of different compounds is selected from Cu 4 O 3 and a compound isomorphous with Cu 4 O 3 that is selected from Ag 0.58 CeSi 1.42 , Ag 0.28 Si 1.72 Yb, Cu 1.035 TeI, C 4 H 4 CuN 6 , Ag 0.7 CeSi 1.3 , Ag 8 O 4 S 2 Si, Ag 3 CuS 2 , CuTeCl, Ba 2 Cs 2 Cu 3 F 12 , Ag 0.3 CeSi 1.7 , Ag 6 O 8 SSi, BaCuInF 7 , Cu 0.99 TeBr, BaCu 2 O 2 , Cu 16 O 14.15 , YBa 2 Cu 3 O 6 and C 9 Ag 9 Cl 6 Cs 5 N 8 .

2. The electrode as claimed in claim 1 ,

wherein the catalyst is present in an amount of 0.1-100% by weight, based on the electrode or on a region of the electrode; and/or

wherein the catalyst has been applied to a support.

3. An electrolysis cell comprising:

an electrode as claimed in claim 1 .

4. The electrode as claimed in claim 2 ,

wherein the catalyst is present in an amount of 40-100% by weight based on the electrode or on a region of the electrode.

5. The electrode as claimed in claim 2 ,

wherein the catalyst is present in an amount of 70-100% by weight, based on the electrode or on a region of the electrode.

6. The electrode as claimed in claim 1 , wherein the catalyst comprises a plurality of particles, the plurality of particles comprising the plurality of different tetragonally crystallized compounds and at least one additive,

wherein the particles have a size of from 0.01 to 100 μm,

wherein the at least one additive comprises a metal, and

wherein the particles have an electrical conductivity of greater than 10 3 S/m.

7. A process for producing an electrode as claimed in claim 1 , comprising:

providing a plurality of tetragonally crystallized compounds containing at least one element selected from Cu and Ag, wherein the crystal lattice of the compounds belongs to the I4 1 /amd space group; and

further comprising a step selected from:

applying the compounds to a support;

and forming the compound to an electrode.

8. The process as claimed in claim 7 ,

wherein the step of applying the compounds to the support is selected from applying a mixture or powder comprising the compounds to the support and dry rolling the mixture or powder onto the support;

applying a dispersion comprising the compounds to the support; and

contacting the support with a gas phase comprising the compounds, and applying the compounds to the support from the gas phase.

9. The process as claimed in claim 8 ,

wherein the compounds are applied with a mass coverage of at least 0.5 mg/cm 2 ; and/or wherein the rolling application is effected at a temperature of 25-100° C.

10. The process as claimed in claim 7 ,

wherein the support is a gas diffusion electrode, a support of a gas diffusion electrode, or a gas diffusion layer.

11. The process as claimed in claim 7 ,

wherein the step of forming the compounds to an electrode comprises rolling of a powder comprising the compounds to give the electrode.

12. The process as claimed in claim 7 ,

wherein the electrode is produced in such a way that the compounds are present in an amount of 0.1-100% by weight, based on the electrode or on a region of the electrode; and/or

wherein the compounds are provided and applied or formed in a mixture comprising at least one binder.

13. The process as claimed in claim 12 ,

wherein the at least one binder is present in the mixture in an amount of >0% to 30% by weight, based on the total weight of the compounds and the at least one binder.

14. A process for electrochemical conversion of CO 2 and/or CO,

wherein CO 2 and/or CO is introduced into an electrolysis cell comprising an electrode as claimed in claim 1 as a cathode and reduced at the cathode.

15. A process for reduction or electrolysis of CO 2 and/or CO, comprising: using the electrode of claim 1 .