Abstract: An electrode fluid distributor includes a fluid passageway having a plurality of segment pairs each including an inlet segment in fluid communication with an inlet and an outlet segment in fluid communication with an outlet. The fluid passageway may have a length greater than the longest dimension of the distributor. Further, a plurality of fluid passageways may be provided, wherein at least one of the fluid passageways includes at least one turn. A baffle is disposed between adjacent inlet segments and outlet segments of the fluid passageway. Each inlet segment is in fluid communication with adjacent inlet segments and adjacent outlet segments, and each outlet segment is in fluid communication with adjacent outlet segments.

Abstract: A solid oxide fuel cell stack is disclosed. The solid oxide fuel cell stack comprises an electrochemical cell having an electrolyte disposed between and in ionic communication with a first electrode and a second electrode. The solid oxide fuel cell stack also comprises at least one interconnect disposed in fluid and thermal communication with at least a portion of the electrochemical cell, the interconnect comprising an electrical supply connector.

Abstract: A fuel cell having an optimized flow space for the passage of hydrogen gas across the surface of an anode. The invention prevents destructive oxidation of the anode by preventing the buildup of locally high levels of oxygen. The anode surface itself may be shaped in lateral plan to follow the natural contours of gas flow to eliminate hydrogen stagnation areas on the anode surface. Alternatively, the anode surface or the cathode surface may be coated in regions of anode stagnation to prevent the fuel cell reactions from occurring in those regions. Alternatively, the gas seals may be formed to cover the anode surface in stagnation regions. Alternatively, the cathode and/or electrolyte may be shaped or thickened to reduce or prevent diffusion of oxygen ions therethrough.

Abstract: In a solid-oxide fuel cell system, the fuel cell stacks, the fuel reformer, tail gas combuster, heat exchangers, and fuel/air manifold, are contained in a “hot zone” within a thermal enclosure. A separate and larger structural enclosure surrounds the thermal enclosure, defining a “cool zone” outside the thermal enclosure for incorporation of “cool” components such as the air supply system and the electronic control system. To prevent unwanted temperature rise in the cool zone during shutdown, from residual heat escaping from the hot zone through the thermal enclosure, the structural enclosure is provided with vents through the lower and upper walls thereof to permit thermal convective circulation of air through the enclosure. The vents are baffled to prevent entry of splash and other contaminants, and the lower vent is provided with a float valve to prevent flooding of the enclosure in event of immersion of the SOFC system.

Abstract: A solid-oxide fuel cell assembly comprising a stack of individual fuel cells for use as an auxiliary power unit in a vehicle. Each cell generates between 0.7V and 1.0 volts, depending upon load. The total output voltage of the assembly must be maintained between 42V and 48V. An assembly comprising 60 cells is optimal for automotive use, being the minimum number of cells required to provide a minimum of 42V (0.7 times 60) under high load, and requiring the minimum voltage control at low loads 1.0V times 60) to provide a maximum of 48V.

Abstract: Disclosed herein are a solid oxide fuel cell and a method for making the same. In one embodiment, the solid oxide fuel cell comprises: A solid oxide fuel cell, comprising: an electrolyte disposed between and in ionic communication with a first electrode and a second electrode, forming an electrochemical cell; a flow plate disposed adjacent to and in electrical communication with at least a portion of the electrochemical cell; and a seal member sealably engaging the flow plate, wherein the seal member comprises a foam selected from the group consisting of a metal, a metal alloy, and combinations comprising at least one of the foregoing foams.

Abstract: An improved system for more uniformly distributing gaseous fuel over the anode surface of a fuel cell, comprising an interconnect subassembly for electrically connecting anodes and cathodes of adjacent fuel cells in a fuel cell stack. The subassembly includes a perforated plate disposed adjacent the anode surface. The plate may be parallel to or inclined to the anode surface and forms a first wall of a fuel plenum for uniformly distributing fuel via the perforations over the entire surface of the anode. The second wall of the plenum is a plate separating the fuel flow from air flowing across the cathode. Electrical continuity across the interconnect subassembly may be provided, for example, by non-planar upsets such as bumps and dimples in the two plenum plate components, or by metallic foam or filaments disposed between the plates and the electrodes.

Abstract: A fuel cell assembly having means for providing tempered air to, and removing spent air from, air-flow passages across the cathode. The air flow path includes means for reversing the direction of flow across the cathode periodically to reverse the roles of the leading and trailing edges of the cathode to prevent temperature differences across the cathode from exceeding 200° C., and thus to prevent damage to the cathode from thermally-induced stresses during startup heating and steady-state cooling.

Abstract: A method of starting a solid oxide fuel cell system is disclosed. The method comprises pressurizing a main plenum to a first pressure. The main plenum comprises a first supply of fuel, blowers, and air control valves. The first supply of fuel and a first supply of air are directed to a preheated micro-reformer. A heated pre-reformate is created in the micro-reformer and discharged from the micro-reformer to a main reformer. The main reformer is preheated with the heated pre-reformate. A second supply of fuel and a second supply of air are introduced to the main reformer. A heated main reformate is created in the main reformer and directed to a waste energy recovery assembly. A cathode supply is heated in the waste energy recovery system and then directed to a solid oxide fuel cell stack in order to heat the solid oxide fuel cell stack. Methods of transitioning, operating, shutting down, and maintaining in standby mode are also disclosed.

Abstract: A fuel cell having a non-uniform electrical resistivity over the flow area of the cell. Resistance is higher in areas of the cell having locally low levels of hydrogen than in areas having locally high levels of hydrogen. Excess oxygen ion migration and buildup is suppressed in regions having low hydrogen concentration and is correspondingly increased in regions having a surfeit of hydrogen. Destructive oxidation of the anode is suppressed and a greater percentage of the hydrogen passed into the cell is consumed, thereby increasing electric output.

Abstract: A fuel cell having an optimized flow space for the passage of hydrogen gas across the surface of an anode. The invention prevents destructive oxidation of the anode by preventing the buildup of locally high levels of oxygen. The anode surface itself may be shaped in lateral plan to follow the natural contours of gas flow to eliminate hydrogen stagnation areas on the anode surface. Alternatively, the anode surface or the cathode surface may be coated in regions of anode stagnation to prevent the fuel cell reactions from occurring in those regions. Alternatively, the gas seals may be formed to cover the anode surface in stagnation regions. Alternatively, the cathode and/or electrolyte may be shaped or thickened to reduce or prevent diffusion of oxygen ions therethrough.

Abstract: The drawbacks and disadvantages of the prior art are overcome by an electrode fluid distributor. The electrode fluid distributor comprises a fluid passageway having a first end with an inlet and a second end with an outlet. A baffle is included that diagonally traverses the fluid passageway from the first end to the second end, and from a base of the fluid passageway toward an at least partially open side of the fluid passageway. The baffle defines at least a portion of a first reservoir and at least a portion of a second reservoir, with the inlet defining at least a portion of one end of the first reservoir and the outlet defining at least a portion of one end of the second reservoir. The inlet is in fluid communication with the outlet over the baffle. The first reservoir has a width proximate the open side which is smaller proximate the inlet than proximate the outlet.

Abstract: An electrode fluid distributor includes a fluid passageway having a plurality of segment pairs each including an inlet segment in fluid communication with an inlet and an outlet segment in fluid communication with an outlet. The fluid passageway may have a length greater than the longest dimension of the distributor. Further, a plurality of fluid passageways may be provided, wherein at least one of the fluid passageways includes at least one turn. A baffle is disposed between adjacent inlet segments and outlet segments of the fluid passageway. Each inlet segment is in fluid communication with adjacent inlet segments and adjacent outlet segments, and each outlet segment is in fluid communication with adjacent outlet segments.

Abstract: A solid oxide fuel cell stack is disclosed. The solid oxide fuel cell stack comprises an electrochemical cell having an electrolyte disposed between and in ionic communication with a first electrode and a second electrode. The solid oxide fuel cell stack also comprises at least one interconnect disposed in fluid and thermal communication with at least a portion of the electrochemical cell, the interconnect comprising an electrical supply connector.

Abstract: Fuel concentrations are determinable in a solid oxide fuel cell through voltage measurement of one or more fuel cell units, which voltage is a function of hydrogen gas present in the fuel feed stream to the one or more fuel cell units. The voltage in the one or more fuel cell units is proportionally related to the fuel concentration in the fuel feed stream to the entire fuel cell. A sensor determines concentrations of the fuel flowing in the fuel cell. The sensor comprises a fuel cell unit, and an indicator electrically coupled to the fuel cell unit, the indicator being capable of displaying a voltage or being adapted to convert a voltage to a fuel concentration display. The voltage measured is correlated to the fuel concentration flowing in the fuel cell.

Abstract: A fuel cell system includes a fuel cell disposed within an enclosure. Pressure is controlled within the fuel cell by a flow control; and pressure is controlled within the enclosure by an enclosure pressure control. The pressure control system for a reformer within an enclosure, the pressure control system comprises a flow control for controlling pressure within the reformer and a pressure control for controlling pressure within the enclosure. The flow control and pressure control are coordinated to provide a desired pressure differential between the fuel cell and the enclosure.

Abstract: The drawbacks and disadvantages of the prior art are overcome by an electrode fluid distributor. The electrode fluid distributor comprises a fluid passageway having a first end with an inlet and a second end with an outlet. A baffle is included that diagonally traverses the fluid passageway from the first end to the second end, and from a base of the fluid passageway toward an at least partially open side of the fluid passageway. The baffle defines at least a portion of a first reservoir and at least a portion of a second reservoir, with the inlet defining at least a portion of one end of the first reservoir and the outlet defining at least a portion of one end of the second reservoir. The inlet is in fluid communication with the outlet over the baffle. The first reservoir has a width proximate the open side which is smaller proximate the inlet than proximate the outlet.

Abstract: Fuel concentrations are determinable in a solid oxide fuel cell through voltage measurement of one or more fuel cell units, which voltage is a function of hydrogen gas present in the fuel feed stream to the one or more fuel cell units. The voltage in the one or more fuel cell units is proportionally related to the fuel concentration in the fuel feed stream to the entire fuel cell. A sensor determines concentrations of the fuel flowing in the fuel cell. The sensor comprises a fuel cell unit, and an indicator electrically coupled to the fuel cell unit, the indicator being capable of displaying a voltage or being adapted to convert a voltage to a fuel concentration display. The voltage measured is correlated to the fuel concentration flowing in the fuel cell.

Abstract: A method of starting a solid oxide fuel cell system is disclosed. The method comprises pressurizing a main plenum to a first pressure. The main plenum comprises a first supply of fuel, blowers, and air control valves. The first supply of fuel and a first supply of air are directed to a preheated micro-reformer. A heated pre-reformate is created in the micro-reformer and discharged from the micro-reformer to a main reformer. The main reformer is preheated with the heated pre-reformate. A second supply of fuel and a second supply of air are introduced to the main reformer. A heated main reformate is created in the main reformer and directed to a waste energy recovery assembly. A cathode supply is heated in the waste energy recovery system and then directed to a solid oxide fuel cell stack in order to heat the solid oxide fuel cell stack. Methods of transitioning, operating, shutting down, and maintaining in standby mode are also disclosed.

Abstract: A remote control lever module comprising a shaft rotatably mounted on a support. A friction pad has a pair or surfaces each of which frictionally resists rotation of the shaft with respect to the support and permits relative rotation between the shafts and the support. A bearing assembly is loosely fit about the shaft to assure that the shaft may rotate in the support.