초록 ▼

In a method for operating a SOFC high-temperature fuel cell, wherein a hydrogen-containing fuel is converted internally in the fuel cell by an endothermic reaction at the anode thereof into a synthesis gas, which is converted by an exothermic reaction into electricity, fuel is supplied to the fuel c

In a method for operating a SOFC high-temperature fuel cell, wherein a hydrogen-containing fuel is converted internally in the fuel cell by an endothermic reaction at the anode thereof into a synthesis gas, which is converted by an exothermic reaction into electricity, fuel is supplied to the fuel cell, to cool the fuel cell, in an excess amount such that, with a predetermined average current density flow, the fuel utilization degree is below 40%, whereas the oxygen is supplied stoichiometrically corresponding to the amount of electricity generating requirements. No additional coolants are therefore reqired for the cooling of the fuel cell.

대표청구항 ▼

1. A method for operating a high-temperature solid oxide fuel cell including an anode and a cathode, said method comprising the steps: converting a hydrocarbon-containing fuel in the fuel cell internally, by an endothermic reaction directly at or in the anode, into a synthesis gas, and convertin

1. A method for operating a high-temperature solid oxide fuel cell including an anode and a cathode, said method comprising the steps: converting a hydrocarbon-containing fuel in the fuel cell internally, by an endothermic reaction directly at or in the anode, into a synthesis gas, and converting the synthesis gas in the fuel cell by an exothermic chemical reaction into electricity, wherein the fuel is supplied to the fuel cell at such an excess that the fuel utilization is below 40%, the temperature difference of the operating media between the entrance into, and the exit out of, the anode space as well as into, and respectively, out of, the cathode space is not more than 20° C., and, the oxygen is supplied to the fuel cell essentially stoichiometrically corresponding to the electric power generating requirement. 2. A method according to claim 1, wherein the fuel cell is operated at temperatures of below 700° C., preferably at temperatures of below 650° C. 3. A method according to claim 1, wherein the fuel utilization degree is below 30%. 4. A method according to claim 1, wherein the temperature difference of the operating media between its entrance into, and its exit from, the anode space and its entry into, and its exit from, the cathode space is not more than 10° C.