Separatorless dual GDE cell for electrochemical reactions

1. An electrolysis cell, comprising:

a cathode space comprising a cathode;

an anode space comprising an anode;

a salt bridge space disposed between the cathode and the anode,

wherein the cathode space and the salt bridge space are delimited from one another by the cathode, and the salt bridge space and the anode space are delimited from one another by the anode, and the cathode and the anode take the form of a gas diffusion electrode, wherein the salt bridge space has no separator, and wherein the cathode and the anode have no separator on a salt bridge space side,

a first feed device comprising a source of a first reactant gas which is connected to the cathode space and is designed to supply the cathode space with the first reactant gas, wherein the first reactant gas comprises CO2, CO, or mixtures thereof, and

a first removal device for a first product gas which is connected to the cathode space and is designed to remove the first product gas from the cathode space,

wherein the electrolysis cell optionally comprises a second feed device for a second reactant gas which is connected to the anode space and is designed to supply the anode space with the second reactant gas,

wherein the electrolysis cell optionally comprises a second removal device for a second product gas which is connected to the anode space and is designed to remove the second product gas from the anode space,

wherein the electrolysis cell further comprises: a third feed device which comprises a source of an electrolyte and which is designed to supply the cathode and the anode in the salt bridge space with the electrolyte, and a third removal device for the electrolyte which is designed to remove the electrolyte from the salt bridge space, and

wherein the cathode comprises a multilayer cathode comprising: an active layer comprising an electrocatalyst, wherein the electrocatalyst is based on Ag or Au and/or compounds thereof, and wherein the active layer is locally hydrophobically modified on the salt bridge space side; and a layer that is hydrophobic and non ion conductive on a cathode space side.

2. The electrolysis cell as claimed in claim 1 ,

wherein the anode comprises an active layer comprising an electrocatalyst, wherein the electrocatalyst comprises IrO 2 .

3. The electrolysis cell as claimed in claim 2 ,

wherein the anode on the anode space side comprises a layer that is hydrophobic, not electrochemically active, not ion-conductive, and is a thickest layer of the anode.

4. The electrolysis cell as claimed in claim 1 ,

wherein the anode comprises a layer that is non ion conductive and hydrophobic on an anode space side.

5. The electrolysis cell as claimed in claim 1 ,

wherein the cathode and/or the anode each comprise a porous layer comprising an ion exchange material on the salt bridge space side.

6. The electrolysis cell as claimed in claim 5 ,

wherein the porous layer on the cathode contains an anion exchanger and/or the porous layer on the anode contains a cation exchanger.

7. The electrolysis cell as claimed in claim 1 ,

wherein metal of the electrocatalyst is based solely on Ag or Au and/or compounds thereof.

8. The electrolysis cell as claimed in claim 1 ,

wherein the electrocatalyst comprises a hydrophobic binder.

9. An electrolysis system, comprising:

an electrolysis cell as claimed in claim 1 .

10. The electrolysis cell as claimed in claim 1 , further comprising the second removal device for the second product gas which is connected to the anode space and is designed to remove the second product gas from the anode space.

11. The electrolysis cell as claimed in claim 10 , further comprising the second feed device for the second reactant gas which is connected to the anode space and is designed to supply the anode space with the second reactant gas.

12. The electrolysis cell as claimed in claim 1 , wherein the electrolysis cell is configured so that the first reactant gas is the only reactant gas fed to the cathode space.

13. A method of electrochemical conversion of the first reactant gas in an electrolysis cell as claimed in claim 1 , the method comprising:

supplying the first reactant gas to the cathode space of the electrolysis cell.

14. The method as claimed in claim 13 ,

wherein the anode space and the cathode space have essentially no liquid.

15. A method of producing at least one product gas in an electrolysis cell as claimed in claim 1 , the method comprising:

producing at least one product gas from an electrolyte in the salt bridge space and removing the at least one product gas from the cathode space and/or the anode space.

16. An electrolysis cell, comprising:

a cathode space comprising a cathode;

an anode space comprising an anode;

a salt bridge space disposed between the cathode and the anode,

wherein the cathode space and the salt bridge space are delimited from one another by the cathode, and the salt bridge space and the anode space are delimited from one another by the anode, and the cathode and the anode take the form of a gas diffusion electrode, wherein the salt bridge space has no separator, and wherein the cathode and the anode have no separator on a salt bridge space side,

a first feed device comprising a source of a first reactant gas which is connected to the cathode space and is designed to supply the cathode space with the first reactant gas, and

a first removal device for a first product gas which is connected to the cathode space and is designed to remove the first product gas from the cathode space,

wherein the electrolysis cell optionally comprises a second feed device for a second reactant gas which is connected to the anode space and is designed to supply the anode space with the second reactant gas,

wherein the electrolysis cell optionally comprises a second removal device for a second product gas which is connected to the anode space and is designed to remove the second product gas from the anode space,

wherein the electrolysis cell further comprises: a third feed device which comprises a source of an electrolyte and which is designed to supply the cathode and the anode in the salt bridge space with the electrolyte, and a third removal device for the electrolyte which is designed to remove the electrolyte from the salt bridge space, and

wherein the cathode comprises a multilayer cathode comprising; a porous layer that comprises an ion exchange material on a salt bridge space side.

17. The electrolysis cell of claim 16 ,

wherein the porous layer further comprises charge carrier creation layers.

18. The electrolysis cell of claim 16 ,

wherein the porous layer further comprises multiple ion exchange materials.

19. The electrolysis cell of claim 16 ,

wherein the porous layer further comprises pores, and wherein the ion exchange material of the porous layer is disposed solely in the pores.

20. The electrolysis cell of claim 16 ,

wherein the source of the electrolyte is configured to supply the electrolyte at a pH ranging from 8.0 to 8.5.