The possibility of performance recovery of the sulfurated Ni-yttria stabilized zirconia anode electrode by shifting the anode electrode potential to the stable region, in which nickel exists as metal, is investigated. The effect of controlling the potential of the anode electrode to the stable region to suppress the generation of nickel sulfide is also revealed. The surface of Ni particle reacts with sulfur to form Ni 3 S 2 in a low temperature region; however, the nickel is reduced to metallic by shifting the electrode potential to −1.9 V vs reference electrode exposed to O 2 . When the potential of the Ni-based anode electrode is maintained at the value of ≤ −1.9 V vs the reference electrode potential, the sulfidation of nickel is inhibited. A small and high-performance solid oxide fuel cell (SOFC) system without any external equipment for fuel reforming has a potential as a power source for mobile machine like automobiles and robots. To realize the small SOFC system, the direct use of liquid hydrocarbon fuel, which has high energy density and is easy to storage and supply, is desirable. In order to use the existing fuel supply infrastructure, the SOFC should be operated by gasoline. For instance, gasoline sold in Japan contains H 2 S up to 10 ppm. Thus, the SOFC must be able to be stably operated at 10 ppm H 2 S-containing gasoline. A porous cermet of Ni and yttria-stabilized zirconia (YSZ), which has widely been studied as an anode electrode for the internal reforming operation SOFC, is one of promising anode electrode materials; however, performance degradation of anode electrode due to sulfur poisoning occurs by trace amounts of the impurity sulfur.1-9 To date, extensive efforts have been taken to gain a profound understanding of the sulfur poisoning by both experimental and theoretical approaches. Based on the knowledge, promising ways to suppress the sulfur poisoning and recover the degraded performance have discovered as was summarized and reviewed in some papers. [10][11][12] Previous studies revealed that the sulfur poisoning of the Ni-YSZ anode is a two-step process. The first process is physical-and/or chemical-adsorption of sulfur onto the surface of Ni particles 2,3,5,8,13 to block the active sites for electrochemical oxidation of fuel, and causes a rapid increase in anode overpotential. The subsequent second process is arise from the microstructure change and the formation of sulfur compounds such as Ni 3 S 2 and NiS, and generates a gradual degradation that lasts for hundred hours or even longer. [2][3][4][5][6]8,[13][14][15] The sulfur poisoning rate of both processes is dependent on the partial pressure of the sulfur species in the fuel and temperature, 1,3,5,7,8,16,17 and the poisoning is stopped and recovered by introducing a fuel that does not contain sulfur. 1,3,[5][6][7]9,15,16 However, the recovery by the introduction of pure gases (e.g., H 2 , N 2 ) without sulfur species is unrealistic because it is difficult to equip the pure gases in a limited space of the mobile machines. To overcom...