Electrochemical production of a gas comprising co with intermediate cooling of the electrolyte flow

Patent metadata

Field	Value
Publication number	US-2020378015-A1
Application number	US-201916964750-A
Country	US
Kind code	A1
Filing date	Jan 18, 2019
Priority date	Feb 15, 2018
Publication date	Dec 3, 2020
Grant date	—

Abstract

A method for the electrochemical production of a gas including CO, in particular CO or syngas, from CO 2 , wherein the electrochemical production of the gas including CO, in particular CO or syngas, from CO 2 takes place in multiple electrolytic cells, which are arranged in series one behind the other in the direction of at least one electrolyte flow and each include a cathode and an anode, wherein the at least one electrolyte flow is conducted through the electrolytic cells which are arranged in series one behind the other and is intermediately cooled between at least two electrolytic cells which are arranged in series one behind the other. A device is adapted for carrying out the method.

First claim

1 . A method for electrochemical production of a gas comprising CO from CO 2 , wherein the electrochemical production of the gas comprising CO from CO 2 takes place in multiple electrolytic cells which are arranged in series one behind the other in a direction of at least one electrolyte flow and each comprise a cathode and an anode, the method comprising:
conducting the at least one electrolyte flow through the electrolytic cells which are arranged in series one behind the other; and intercooling the at least one electrolyte flow between at least two electrolytic cells which are arranged in series one behind the other.

2 . The method as claimed in claim 1 ,
wherein the at least one electrolyte flow between the multiple electrolytic cells which are arranged in series one behind the other is separated into a catholyte flow and an anolyte flow.

3 . The method as claimed in claim 2 ,
wherein the catholyte flow and the anolyte flow are intercooled between at least two electrolytic cells which are arranged in series one behind the other.

4 . The method as claimed in claim 3 ,
wherein the catholyte flow and anolyte flow are combined and recycled in a common electrolyte flow, wherein the common electrolyte flow is optionally degassed and separated before a first electrolytic cell in the direction of flow into a catholyte flow and an anolyte flow.

5 . The method as claimed in claim 1 ,
wherein, in at least two of the electrolytic cells which are arranged in series one behind the other, a first and a second starting material flow comprising CO 2 are fed separately.

6 . The method as claimed in claim 1 ,
wherein, in at least one electrolytic cell, the cathode is embodied as a gas diffusion electrode.

7 . The method as claimed in claim 1 ,
wherein the intercooling is performed by at least one heat exchanger and/or at least one air cooler.

8 . The method as claimed in claim 7 ,
wherein the intercooling is performed by at least one heat exchanger, wherein waste heat is used as district heating.

9 . A device for electrochemical production of a gas comprising CO from CO 2 , comprising:
multiple electrolytic cells which are arranged one behind the other in a direction of at least one electrolyte flow and each comprise a cathode and an anode; at least one connecting facility between at least two electrolytic cells, which is embodied to conduct the at least one electrolyte flow between the at least two electrolytic cells; at least one first feed facility for a first starting material flow comprising CO 2 , which is embodied to feed the first starting material comprising CO 2 to a first electrolytic cell arranged in the direction of flow of the CO 2 ; and at least one intercooler, which is embodied to cool at least one electrolyte flow of the at least one connecting facility.

10 . The device as claimed in claim 9 ,
wherein the at least one connecting facility is provided between at least two electrolytic cells which are arranged in series one behind the other as at least one first connecting facility and at least one second connecting facility, wherein the at least one first connecting facility is embodied to conduct a catholyte flow and the at least one second connecting facility is embodied to conduct an anolyte flow.

11 . The device as claimed in claim 10 ,
wherein at least two intercoolers are provided of which at least one first intercooler is embodied to cool the catholyte flow in the at least one first connecting facility and at least one second intercooler is embodied to cool the anolyte flow in the at least one second connecting facility.

12 . The device as claimed in claim 9 , further comprising:
at least one second feed facility for a second starting material flow comprising CO 2 , which is embodied to feed a second starting material flow comprising CO 2 to a further electrolytic cell lying in the direction of flow of the at least one electrolyte flow after the first electrolytic cell in the series.

13 . The device as claimed in claim 9 ,
wherein, in at least one electrolytic cell, the cathode is embodied as a gas diffusion electrode.

14 . The device as claimed in claim 9 ,
wherein the at least one intercooler is embodied as a heat exchanger and/or as an air cooler.

15 . The device as claimed in claim 14 ,
wherein the at least one intercooler is embodied as a heat exchanger, wherein the heat exchanger is connected to a district heating network.

Assignees

• Siemens Ag

Inventors

• Hanebuth Marc
• Schmid Günter
• Taroata Dan
• Delhomme-Neudecker Clara
• Hentschel Benjamin
• Peschel Andreas
• Schödel Nicole

Classifications

• C25B15/087

  Recycling of electrolyte to electrochemical cell · CPC title

• C25B15/08

  Supplying or removing reactants or electrolytes; Regeneration of electrolytes · CPC title

• C25B15/021

  of heating or cooling · CPC title

• C25B11/032

  Gas diffusion electrodes · CPC title

• C25B9/70

  Assemblies comprising two or more cells · CPC title