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 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 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:
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. A heat source is coupled to the hot zone chamber to heat the reaction zones to the operating reaction temperature, and fuel and air supplies are coupled to the tubes in the cold zones.
Abstract:
Fuel cell devices and fuel cell systems, methods of using same, and methods of making same are provided. In certain embodiments, the fuel cell devices may include one or more active layers containing active cells that are connected electrically in parallel and/or 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. In some embodiments, ceramic end tubes are permanently attached to the ceramic support structure to supply gases to the passages. In certain embodiments, a multilayer active structure is attached upon a flat tube having a plurality of channels therein for feeding gases into the passages of the multilayer active structure. In other embodiments, multilayer active structures are provided in which the electrodes contain pluralities of microtubular or nanotubular passages for feeding gases thereto. In yet other embodiments, the multilayer active structure is contained within a ceramic support structure that includes two elongate members that extend outwardly from one edge for feeding gases into the multilayer active structure.
Abstract:
The invention provides a fuel cell including an elongate substrate the length of which is the greatest dimension such that the elongate substrate exhibits thermal expansion along a dominant axis that is coextensive with the length. A reaction zone is provided along a first portion of the length for heating to an operating reaction temperature, and at least one cold zone is provided along a second portion of the length that remains at a low temperature below the operating reaction temperature when the reaction zone is heated. An electrolyte is disposed between an anode and a cathode in the reaction zone and the electrolyte is monolithic with an interior ceramic support structure of the elongate substrate. The anode and cathode each have an electrical pathway extending to an exterior surface of the at least one cold zone for electrical connection at low temperature.
Abstract:
A fuel cell device includes an elongate substrate having a cold zone adjacent a first end and a reaction zone adjacent a second end configured to be heated to an operating reaction temperature while the cold zone is configured to be shielded from the heat source to remain at a low temperature below the operating reaction temperature. Fuel and air inlets positioned in the cold zone are coupled to respective elongate fuel and oxidizer passages that extend within an interior solid ceramic support structure through the reaction zone in parallel and opposing relation to respective outlets adjacent the second end. Electrodes positioned adjacent the passages in the reaction zone are each electrically coupled from the interior structure to respective exterior contact surfaces in the cold zone. A solid electrolyte monolithic with the ceramic support structure is positioned between electrodes, and electrical connections are made to the exterior contact surfaces.
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. In other embodiments, fuel cell devices include second sub-passages for the active second gas passage and a second artery flow passage coupled thereto, and extending from either the first end or the second end into the reaction zone. In yet other embodiments, one or both electrodes of a fuel cell device are segmented.
Abstract:
A monolithic capacitor structure includes opposed and overlapping plates within a dielectric body, which are arranged to form a lower frequency, higher value capacitor. Other conductive structure is located either inside the dielectric body or on an external surface thereof and is effective to form a higher frequency, lower value capacitor in parallel with the lower frequency, higher value capacitor. The resulting array of combined series and parallel capacitors integral with the dielectric body provides effective wideband performance in an integrated, cost-effective structure.
Abstract:
A substrate includes a single-layer capacitor and various external contacts. A first external contact provides a first electrical connection to the single-layer capacitor. A second external contact provides a second electrical connection to the single-layer capacitor. The first and third external contacts are electrically connectable to another electrical component, and internal metallization structures or vias of conductive material electrically connect the second contact and the third contact to facilitate the single-layer capacitor being connectable in a parallel circuit with the other electrical component.