Membranes were cast from mixtures of the 3M perfluorinated sulfonic acid ionomer ͓side chain -O-͑CF 2 ͒ 4 -SO 3 H͔ and various heteropoly acids ͑HPAs͒ at a 10 or 20 wt % doping level. Membrane electrode assemblies ͑MEAs͒ fabricated from these membranes were subjected to a fuel cell testing protocol from 70 to 100°C under relatively dry conditions, dew point of 70°C, to avoid leaching of the HPA. The most significant finding was that the more stable HPAs, H 4 SiW 12 O 40 , ␣-H 3 P 2 W 18 O 62 , and H 6 P 2 W 21 O 71 , reduce the rate of F − by over half and improve the power of the MEA by 9% under these conditions. Even with the use of perfluorosulfonated ͑PFSA͒ ionomers, insufficient durability of the proton exchange membrane ͑PEM͒ in the oxidizing acidic environment of an operating PEM fuel cell continues to be a major impediment to the commercialization of these devices. The major cause of the insufficient lifetime of the PEM is thought to be oxidative degradation by hydrogen peroxide via its decomposition to hydroxyl radical. 1 Hydrogen peroxide may be present throughout the membrane electrode assembly ͑MEA͒ as it is thought to be liberated from either the anode ͑derived from crossover oxygen͒ or the cathode after a 2 e − reduction of oxygen. The hydroxyl radical is expected to be particularly damaging to the polymer, and its concentration is known to be dramatically increased by the presence of trace amounts of certain transition-metal cations such as iron, which efficiently produces hydroxyl radical from hydrogen peroxide in Fenton reagents. PEM lifetimes and functionality for operation in hotter and drier conditions may be enhanced by the addition of catalytic amounts of Pt or the cesium salt of 12-phosphotungstic acid, a heteropoly acid ͑HPA͒ that converts any permeating H 2 or O 2 in situ in the PEM into water. 2,3 It has been implied that any peroxide in the membrane is decomposed to water. Whereas improved fuel cell performance under hotter and drier operation has been demonstrated for MEAs containing membranes with these catalytic additives, little data exists to support the assumption that these same additives enhance PEM lifetime in a fuel cell.Of the additives used, the HP A are the most intriguing as they are a subset of a large class of inorganic oxides, the polyoxometalates, and only a few members of this class of compounds have been investigated as PEM additives. 4-6 The most well-known, and common, structure is the Keggin structure in which 12 metal-oxygen octahedra ͑where the metal is typically W or Mo͒ are arranged as four groups of three tetrahedrally around a central heteroatom ͑Fig. 1a͒. More complex structures, including the Dawson structure, are also illustrated in Fig. 1. 1, 2, or 3 metal-oxygen octahedra may be removed from the HPA to form the lacunary HPA. Other metal atoms can easily be substituted into the vacancies of the lacunary HPA, e.g., aluminum, allowing the HPA properties to be fine-tuned for many applications. The chemistry of HPAs and peroxides has been extensively studied...