Electrochemical energy store and method for operating the same
A rechargeable energy storage device according to the invention is based on a metal-air battery, in which a gas electrode is used and an ion-conducting or proton-conducting membrane is used as the electrolyte. In contrast to the known metal-air batteries, the active component on the side of the electrolyte membrane opposite the gas electrode is present in the form of a liquid medium in the energy storage device according to the invention. The liquid-medium/gas battery according to the invention comprises a receptacle, which includes a medium in liquid form as the active material at the operating temperature of the battery.
1. An electrochemical energy storage device, comprising a gas electrode, an ion-conducting electrolyte and a counter electrode comprising an active material, which at operating temperatures between 500 and 1000° C. is present in the liquid state both in at least one reduced form and in at least one oxidized form,
wherein
the electrochemical energy storage device comprises a receptacle that includes the active material,
the electrolyte is a membrane having a thickness no greater than 10 μm and arranged entirely perpendicularly to the surface of the earth,
a solid catalyst layer is provided on the membrane at a side of the membrane facing the liquid active material,
the liquid active material within the receptacle is present in the form of horizontal layers, and
the counter electrode is formed of the liquid active material and the catalyst layer.
2. The energy storage device according to claim 1 , wherein the active material is selected from the group consisting of metals, metalloids, simple or complex oxides, nitrogen compounds, carbon compounds, hydrides, phosphorus compounds, halogen compounds, chalcogen compounds, silicon compounds, germanium compounds or boron compounds, and mixtures of at least two members of this group.
3. The energy storage device according to claim 1 , comprising bismuth as the active material.
4. The energy storage device according to claim 1 , wherein
the gas electrode is disposed perpendicularly to the surface of the earth, and
the horizontal layers of the active material a liquid oxidized phase and a reduced phase, respectively, of the active material, so that
the ion-conducting electrolyte completely is in contact both with a liquid oxidized phase and with a liquid reduced phase of the active material during a charging or discharging process.
5. A battery stack, comprising at least two of the electrochemical energy storage device according to claim 1 .
6. A method for operating an electrochemical energy storage device, the electrochemical energy storage device comprising a gas electrode, an ion-conducting electrolyte and a counter electrode comprising an active material,
which at operating temperatures between 500 and 1000° C. is present in the liquid state both in at least one reduced form and in at least one oxidized form, wherein
the electrochemical energy storage device comprises a receptacle that includes the active material,
the liquid active material within the receptacle is present in the form of horizontal layers, and
the counter electrode is formed exclusively of the liquid active material, or of the liquid active material and a solid catalyst layer disposed on a side of the non-conducting electrolyte facing the liquid active material,
the method comprising:
heating the energy storage device to operating temperatures between 500 and 1000° C.; and
disposing the ion-conducting electrolyte substantially perpendicularly to the surface of the earth; wherein
layering of the two phases along the ion-conducting electrolyte takes place as a result of a difference in density between a phase made of liquid oxidized active material and a liquid active material present in reduced form;
reduction or oxidation of the active material takes place exclusively at the ion-conducting electrolyte or at the solid catalyst layer disposed on the ion-conducting electrolyte, and
varying a contact surface between the ion-conducting electrolyte, or a solid catalyst layer disposed on the ion-conducting electrolyte, and at least one liquid phase of the active material by changing the position of the energy storage device.
7. The method according to claim 6 , wherein oxygen is used as an oxidizing agent.
8. The method according to claim 6 , wherein an anion-conducting membrane is used as the electrolyte.
9. The method according to claim 6 , wherein a cation-conducting or proton-conducting membrane is used as the electrolyte.
10. The method according to claim 6 , wherein the active material is selected from the group consisting of metals, metalloids, simple or complex oxides, nitrogen compounds, carbon compounds, hydrides, phosphorus compounds, halogen compounds, chaicogen compounds, silicon compounds, germanium compounds or boron compounds, and mixtures of at least two of the members of this group.
11. The method according to claim 6 , wherein bismuth is used as the active material.
12. The method according to claim 6 , wherein a chemical reaction at the counter electrode comprising the liquid active material is supported by an additional catalyst layer applied to the electrolyte.
13. The method according to claim 6 , wherein the operating temperature for the electrochemical energy storage device is set by way of an external heat source.
14. A method for operating an electroChemical energy storage device, the electrochemical energy storage device comprising a gas electrode, an ion-conducting electrolyte and a counter electrode comprising an active material, which at operating temperatures between 500 and 1000° C. is present in the liquid state both in at least one reduced form and in at least one oxidized form, wherein
the electrochemical energy storage device comprises a receptacle that includes the active material,
the liquid active material within the receptacle is present in the form of horizontal layers, and
the counter electrode is formed exclusively of the liquid active material, or of the liquid active material and a solid catalyst layer disposed on a side of the non-conducting electrolyte facing the liquid active material,
the method comprising:
heating the energy storage device to operating temperatures between 500 and 1000° C.; and
disposing the ion-conducting electrolyte substantially perpendicularly to the surface of the earth; wherein
layering of the two phases along the ion-conducting electrolyte takes place as a result of a difference in density between a phase made of liquid oxidized active material and a liquid active material present in reduced form; and
reduction or oxidation of the active material takes place with hydrogen as a reducing agent and exclusively at the ion-conducting electrolyte or at the solid catalyst layer disposed on the ion-conducting electrolyte.