Abstract: A multilayer ceramic capacitor, having a plurality of electrode layers and a plurality of substantially titanium dioxide dielectric layers, wherein each respective titanium dioxide dielectric layer is substantially free of porosity, wherein each respective substantially titanium dioxide dielectric layer is positioned between two respective electrode layers, wherein each respective substantially titanium dioxide dielectric layer has an average grain size of between about 200 and about 400 nanometers, wherein each respective substantially titanium dioxide dielectric layer has maximum particle size of less than about 500 nanometers. Typically, each respective substantially titanium dioxide dielectric layer further includes at least one dopant selected from the group including P, V, Nb, Ta, Mo, W, and combinations thereof, and the included dopant is typically present in amounts of less than about 0.01 atomic percent.

Abstract: Fuel cell devices and fuel cell systems are provided. In certain embodiments, the fuel cell devices may include one or more active layers containing active cells that are connected electrically in series. In certain embodiments, the fuel cell devices include an elongate ceramic support structure the length of which is the greatest dimension such that the coefficient of thermal expansion has only one dominant axis coextensive with the length. In certain embodiments, a reaction zone is positioned along a first portion of the length for heating to a reaction temperature, and at least one cold zone is positioned along a second portion of the length for operating below the reaction temperature. There are one or more gas passages, each having an associated anode or cathode.

Abstract: A fuel cell device including an elongate ceramic substrate having an exterior surface defining an interior ceramic support structure and having a length that is at least 5 times greater than the width and the thickness so as to exhibit thermal expansion along a dominant axis coextensive with the length. The substrate has an active zone and at least one non-active end region. The active zone has an anode and a cathode in opposing relation with an electrolyte therebetween and the non-active end region lacks the anode and cathode in opposing relation and extends away from the active zone to dissipate heat. The electrolyte, anode and cathode extend within the interior ceramic support structure, the anode and cathode each have an electrical pathway extending from within the interior ceramic support structure to the exterior surface in the non-active end region, and the electrolyte is a ceramic co-fired with the interior ceramic support structure.

Abstract: A monolithic fuel cell device is provided by forming anode and cathode layers by dispensing paste of anode or cathode material around pluralities of spaced-apart removable physical structures to at least partially surround the structures with the anode or cathode material and then drying the paste. An electrolyte layer is provided in a multi-layer stack between the cathode layer and the anode layer thereby forming an active cell portion. The multi-layer stack is laminated, and then the physical structures are pulled out to reveal spaced-apart active passages formed through each of the anode layer and cathode layer. Finally, the laminated stack is sintered to form an active cell comprising the spaced apart active passages embedded in and supported by the sintered anode material and sintered cathode material.

Abstract: The present invention relates to a fuel cell system. A hot zone chamber has a wall thickness T and a heat source coupled thereto. An elongate fuel cell device is positioned with a first lengthwise portion within the hot zone chamber, a second lengthwise portion outside the hot zone chamber, and a third lengthwise portion of length T within the chamber wall. The third portion has a maximum dimension L in a plane transverse to the length where T?½L.

Abstract: Fuel cell devices and systems are provided. In certain embodiments, the devices include a ceramic support structure having a length, a width, and a thickness with the length direction being the dominant direction of thermal expansion. A reaction zone having at least one active layer therein is spaced from the first end and includes first and second opposing electrodes, associated active first and second gas passages, and electrolyte. The active first gas passage includes sub-passages extending in the y direction and spaced apart in the x direction. An artery flow passage extends from the first end along the length and into the reaction zone and is fluidicly coupled to the sub-passages of the active first gas passage. The thickness of the artery flow passage is greater than the thickness of the sub-passages.

Abstract: Fuel cell devices are provided having improved shrinkage properties between the active and non-active structures by modifying the material composition of the non-active structure, having a non-conductive, insulating barrier layer between the active structure and surface conductors that extend over the inactive surrounding support structure, having the width of one or both electrodes progressively change along the length, or having a porous ceramic layer between the anode and fuel passage and between the cathode and air passage. Another fuel cell device is provided having an internal multilayer active structure with electrodes alternating in polarity from top to bottom and external conductors on the top and/or bottom surface with sympathetic polarity to the respective top and bottom electrodes. A fuel cell system is provided with a fuel cell device having an enlarged attachment surface at one or both ends, which resides outside the system's heat source, insulated therefrom.

Abstract: Fuel cell devices and systems are provided. In certain embodiments, the devices include a ceramic support structure having a length, a width, and a thickness. A reaction zone positioned along a portion of the length is configured to be heated to an operating reaction temperature, and has at least one active layer therein comprising an electrolyte separating first and second opposing electrodes, and active first and second gas passages adjacent the respective first and second electrodes. At least one cold zone positioned from the first end along another portion of the length is configured to remain below the operating reaction temperature. An artery flow passage extends from the first end along the length through the cold zone and into the reaction zone and is fluidicly coupled to the active first gas passage, which extends from the artery flow passage toward at least one side. The thickness of the artery flow passage is greater than the thickness of the active first gas passage.

Abstract: The present invention relates to a fuel cell system. A hot zone chamber has a wall thickness T and a heat source coupled thereto. An elongate fuel cell device is positioned with a first lengthwise portion within the hot zone chamber, a second lengthwise portion outside the hot zone chamber, and a third lengthwise portion of length T within the chamber wall. The third portion has a maximum dimension L in a plane transverse to the length where T?½L.

Abstract: A multilayer ceramic capacitor, having a plurality of electrode layers and a plurality of substantially titanium dioxide dielectric layers, wherein each respective titanium dioxide dielectric layer is substantially free of porosity, wherein each respective substantially titanium dioxide dielectric layer is positioned between two respective electrode layers, wherein each respective substantially titanium dioxide dielectric layer has an average grain size of between about 200 and about 400 nanometers, wherein each respective substantially titanium dioxide dielectric layer has maximum particle size of less than about 500 nanometers. Typically, each respective substantially titanium dioxide dielectric layer further includes at least one dopant selected from the group including P, V, Nb, Ta, Mo, W, and combinations thereof, and the included dopant is typically present in amounts of less than about 0.01 atomic percent.

Abstract: A fuel cell device including an elongate ceramic substrate having an exterior surface defining an interior ceramic support structure and having a length that is at least 5 times greater than the width and the thickness so as to exhibit thermal expansion along a dominant axis coextensive with the length. The substrate has an active zone and at least one non-active end region. The active zone has an anode and a cathode in opposing relation with an electrolyte therebetween and the non-active end region lacks the anode and cathode in opposing relation and extends away from the active zone to dissipate heat. The electrolyte, anode and cathode extend within the interior ceramic support structure, the anode and cathode each have an electrical pathway extending from within the interior ceramic support structure to the exterior surface in the non-active end region, and the electrolyte is a ceramic co-fired with the interior ceramic support structure.

Abstract: The invention provides tubular solid oxide fuel cell devices and a fuel cell system incorporating a plurality of the fuel devices, each device including an elongate tube having a reaction zone for heating to an operating reaction temperature, and at least one cold zone that remains at a low temperature below the operating reaction temperature when the reaction zone is heated. An electrolyte is disposed between anodes and cathodes in the reaction zone, and the anode and cathode each have an electrical pathway extending to an exterior surface in a cold zone for electrical connection at low temperature. In one embodiment, the tubular device is a spiral rolled structure, and in another embodiment, the tubular device is a concentrically arranged device. The system further includes the devices positioned with their reaction zones in a hot zone chamber and their cold zones extending outside the hot zone chamber.

Abstract: Fuel cell devices and systems are provided. In certain embodiments, the devices include a ceramic support structure having a length, a width, and a thickness. A reaction zone positioned along a portion of the length is configured to be heated to an operating reaction temperature, and has at least one active layer therein comprising an electrolyte separating first and second opposing electrodes, and active first and second gas passages adjacent the respective first and second electrodes. At least one cold zone positioned from the first end along another portion of the length is configured to remain below the operating reaction temperature. An artery flow passage extends from the first end along the length through the cold zone and into the reaction zone and is fluidicly coupled to the active first gas passage, which extends from the artery flow passage toward at least one side. The thickness of the artery flow passage is greater than the thickness of the active first gas passage.

Abstract: Fuel cell devices and fuel cell systems are provided. In certain embodiments, the fuel cell devices may include one or more active layers containing active cells that are connected electrically in series. In certain embodiments, the fuel cell devices include an elongate ceramic support structure the length of which is the greatest dimension such that the coefficient of thermal expansion has only one dominant axis coextensive with the length. In certain embodiments, a reaction zone is positioned along a first portion of the length for heating to a reaction temperature, and at least one cold zone is positioned along a second portion of the length for operating below the reaction temperature. There are one or more gas passages, each having an associated anode or cathode.

Abstract: The invention relates to fuel cell devices and systems, and methods of using and making fuel cell devices and systems. The fuel cell devices include an elongate ceramic substrate, such as a rectangular or tubular substrate, the length of which is the greatest dimension such that thermal expansion is exhibited along a dominant axis that is coextensive with the length. A reaction zone is positioned along a first portion of the length for heating to an operating reaction temperature, and at least one cold zone is positioned along a second portion of the length for operating at a temperature below the operating reaction temperature. There are one or more fuel passages and one or more oxidizer passages extending within an interior solid support structure of the elongate substrate, each having an associated anode and cathode, respectively, which are separated by an electrolyte. The passages include a neck-down point.

Abstract: The present invention relates to a method of making fuel cell devices. A stack structure is formed having plural ceramic layers, anode layers, cathode layers, and sacrificial layers, where the sacrificial layers are sized to provide internal gas passages. Removable structures are placed in contact with the sacrificial layers and extend to an edge. After laminating the stacked structure, the removable structures are pulled out to form bake-out paths that facilitate removal of the sacrificial material during a heating step, which paths are later sealed.

Abstract: The invention provides tubular solid oxide fuel cell devices and a fuel cell system incorporating a plurality of the fuel devices, each device including an elongate tube having a reaction zone for heating to an operating reaction temperature, and at least one cold zone that remains at a low temperature below the operating reaction temperature when the reaction zone is heated. An electrolyte is disposed between anodes and cathodes in the reaction zone, and the anode and cathode each have an electrical pathway extending to an exterior surface in a cold zone for electrical connection at low temperature. In one embodiment, the tubular device is a spiral rolled structure, and in another embodiment, the tubular device is a concentrically arranged device. The system further includes the devices positioned with their reaction zones in a hot zone chamber and their cold zones extending outside the hot zone chamber.

Abstract: A fuel cell device including an elongate ceramic substrate having an exterior surface defining an interior ceramic support structure having non-active end regions and an active zone therebetween that includes electrodes in opposing relation with an electrolyte therebetween for undergoing a fuel cell reaction when supplied with heat, fuel and oxidizer. The electrolyte is a ceramic co-fired with the interior ceramic support structure. The end regions lack opposing electrodes and extend away from the active zone to dissipate heat. Gas inlets are positioned in the end regions with respective outlets in either the active zone or opposite end region, and elongate passages are coupled therebetween at least partially extending in opposing relation through the active zone. The electrodes are positioned adjacent the gas passages in the active zone and are electrically connected to exterior contact surfaces on the exterior surface of the end regions for external connection to voltage nodes.

Abstract: A capacitor device mountable on a plane of a substrate includes an electrically conductive bottom plate adapted to be mounted substantially parallel to, and in electrical contact at the plane of the substrate and a first multilayer capacitor having substantially parallel first and second electrode plates oriented substantially perpendicular to the bottom plate with the first electrode plates being electrically connected to the bottom plate. An electrically conductive top lead frame overlaps with, and is electrically isolated from, the bottom plate. The top lead frame electrically connected to the second electrode plates and adapted to be electrically connected at the plane of the substrate. The bottom lead frame may have a corrugated shape, where the corrugated shape provides compliance between the first multilayer capacitor and the substrate. A portion of the top lead frame may contact at least a portion of a side of the first multilayer capacitor.

Abstract: The present invention relates to fuel cell devices and fuel cell systems, methods of using fuel cell devices and systems, and methods of making fuel cell devices. According to certain embodiments, the fuel cell devices may include an elongate substrate, such as a rectangular or tubular substrate, the length of which is the greatest dimension such that the coefficient of thermal expansion has only one dominant axis that is coextensive with the length. In addition, or in accordance with other certain embodiments, a reaction zone is positioned along a first portion of the length for heating to an operating reaction temperature, and at least one cold zone is positioned along a second portion of the length for operating at a temperature below the operating reaction temperature. There are one or more fuel passages in the elongate substrate, each having an associate anode, and one or more oxidizer passages in the elongate substrate, each having an associate cathode.