Abstract: A glass ceramic seal is formed from a precursor material that includes from 80 mol % to 100 mol % of a primary component containing, on an oxide basis, from 25 mol % to 55 mol % SiO2, from 20 mol % to 45 mol % CaO, from 5 mol % to 30 mol % MgO, and from 0 mol % to 15 mol % Al2O3.

Abstract: A glass ceramic seal contains by weight, on an oxide basis 40-60% of SiO2, 25-28% of BaO, 10-20% of B2O3, 8-12% of Al2O3, 0-2% of ZrO2, 0-1% of Y2O3, 0-1% of CaO, and 0-1% of MgO.

Abstract: A technique includes operating a fuel cell, which produces an effluent flow. The technique includes routing the effluent flow through an electrochemical pump to extract fuel from the effluent flow and providing the extracted fuel to the fuel cell.

Abstract: A technique includes operating a fuel cell, which produces an effluent flow. The technique includes routing the effluent flow through an electrochemical pump to extract fuel from the effluent flow to produce a first feedback flow. The technique includes using the effluent flow to produce a second feedback flow separate from the first feedback flow and routing the second feedback flow through a venturi to the fuel cell.

Abstract: Hydrogen pumps include a proton conducting medium, and a nonporous hydrogen permeable anode electrode and/or nonporous hydrogen permeable cathode electrode. For example, the electrodes may be a solid thin metallic film such as palladium or a palladium alloy such as a palladium-copper alloy that allow for hydrogen permeation but not impurities, and thus, purifying a supply containing hydrogen. The proton conducting medium may be a solid anhydrous proton conducting medium disposed between the anode electrode and the cathode electrode. The anode electrode and the cathode electrode may be directly sealed to at least one of the proton conducting medium, a first member for distributing the supply containing hydrogen to the anode electrode, a second member for collecting a supply of purified hydrogen, and a gasket disposed around the proton conducting medium.

Abstract: A hydrogen reclamation system comprises a first hydrogen separator having an inlet and an outlet and a second hydrogen separator having an inlet and an outlet wherein an inlet gas stream having a first concentration of hydrogen gas enters said first hydrogen separator inlet and is processed into an outlet gas stream having a second concentration of hydrogen gas which exits said first hydrogen separator outlet and subsequent to exiting said first hydrogen separator outlet, said outlet gas stream enters said second hydrogen separator inlet and is processed into a second outlet gas stream having a third concentration of hydrogen gas which exits said second hydrogen separator outlet.

Abstract: A technique includes removing nitrogen from an air stream to produce an enriched oxygen stream and communicating the enriched oxygen stream to a cathode chamber of a fuel cell. The technique includes transferring the nitrogen that is removed from the air stream to a reactant stream of the fuel cell system.

Abstract: An electrochemical cell includes an anode, a cathode and a proton conductor. The anode includes a catalyst to reform a hydrocarbon to generate hydrogen at the anode. The proton conductor is in electrical contact with the anode and cathode to receive an applied voltage to cause protons to be transferred from the anode to the cathode to produce hydrogen at the cathode.

Abstract: Apparatus and operating methods are provided for integrated electrochemical hydrogen separation and compression systems. In one possible embodiment, an electrical connection is initiated between an anode and a cathode of an electrochemical cell. Hydrogen is ionized at the anode to flow protons through a proton exchange membrane to the cathode. The protons are reacted with oxygen at the cathode to form water. The electrical connection between the anode and the cathode is removed, and a power supply is connected to the anode and cathode so that the anode has a higher electrical potential with respect to zero than the cathode. Various methods, features and system configurations are discussed.

Abstract: Apparatus and operating methods are provided for integrated electrochemical hydrogen separation systems. In one possible embodiment, an electrical potential is applied between a first electrode and a second electrode of an electrochemical cell. The first electrode has a higher electrical potential with respect to zero than the second electrode. Electrical current is flowed through the cell as hydrogen is ionized at the first electrode and evolved at the second electrode. i.e., “pumped” across the cell. The hydrogen outlet flow and pressure from the cell can be controlled by adjusting the potential and current provided by the power supply. Various methods, features and system configurations are discussed.

Abstract: Techniques are provided for system operation and performance management of electrochemical cells. Electrochemical cells using polybenzimidazole (PBI) proton exchange membranes may be used. In certain embodiments, performance enhancements are achieved through water management via anode and/or cathode humidification, and reactant air injection.

Abstract: A technique includes introducing an electrical perturbation to a fuel cell system during operation of the fuel cell system. This electrical perturbation does not substantially disrupt the operation of the fuel cell system. In response to the perturbation, an electrical parameter of the fuel cell system is measured.