A fuel cell array comprises a plurality of serially connected fuel cell units. A respective fuel cell unit comprises a fuel cell and a cap capped on each end of the fuel cell. The fuel cell unit further comprises an electrically conductive terminal layer forming an outermost laminate of the fuel cell at one end of the fuel cell. The terminal layer is directly laminated on a fuel electrode layer and directly laminated on a solid electrolyte layer. The fuel cell unit further comprises a glass material forming a sealing layer circumferentially around the fuel cell to fill between the inner surface of the cap and the outer surface of the fuel cell. The plurality of fuel cell units are electrically connected in series through the electrically conductive terminal layer, not through the cap.

A fuel cell tube comprises a substrate having a tube interconnect region and a fuel cell region, a plurality of fuel cells disposed on the fuel cell region, and a plurality of primary interconnects formed from an electrically conducting primary interconnect material forming electrically conducting paths between adjacent fuel cells to thereby electrically connect the fuel cells in series. The primary interconnect material extends from the fuel cell region into the tube interconnect region forming an electrically conducting path between the tube interconnect region and the plurality of fuel cells.

A fuel cell tube comprises a substrate having a tube interconnect region and a fuel cell region, a plurality of fuel cells disposed on the fuel cell region, and a plurality of primary interconnects formed from an electrically conducting primary interconnect material forming electrically conducting paths between adjacent fuel cells to thereby electrically connect the fuel cells in series. The primary interconnect material extends from the fuel cell region into the tube interconnect region forming an electrically conducting path between the tube interconnect region and the plurality of fuel cells.

A recombinator for the catalytic recombination of hydrogen and oxygen generated in energy converters, in particular accumulators, to form water, comprising a housing in which a volume space is formed, into which the gases can flow via an opening and in which a recombination device is arranged that comprises a portion for a catalyst material and a portion for an absorption material, wherein the flow path of the gases to be recombined extends through the portion comprising the absorption material into the portion comprising the catalyst material, wherein a distance space is formed between the portion comprising the absorption material and the portion comprising the catalyst material, wherein the catalyst material is configured as a catalyst bar, the catalyst bar is arranged in a first gas-permeable tube and the distance space is formed in a gap space between the inner walling of the first gas-permeable tube and the outer wall of the catalyst bar.

An ion-permeable web-reinforced separator, said ion-permeable web-reinforced separator comprising two separator elements separated by an (optionally integrated) substantially hollow by-pass channel, wherein the separator elements each comprise a binder and a metal oxide or hydroxide dispersed therein and the separator elements have a bubble point of at least 1 bar (0.1 MPa) and a back-wash resistance of at least 1 bar (0.1 MPa) and optionally have a specific resistance less than 4 -cm at 30 C. in 6M potassium hydroxide solution; an electrochemical cell involving the production or consumption of at least one gas, said electrochemical cell comprising said ion-permeable web-reinforced separator; and the use thereof in an electrochemical cell involving the production or consumption of at least one gas.

An ion-permeable web-reinforced separator, said ion-permeable web-reinforced separator comprising two separator elements separated by an (optionally integrated) substantially hollow by-pass channel, wherein the separator elements each comprise a binder and a metal oxide or hydroxide dispersed therein and the separator elements have a bubble point of at least 1 bar (0.1 MPa) and a back-wash resistance of at least 1 bar (0.1 MPa) and optionally have a specific resistance less than 4 -cm at 30 C. in 6M potassium hydroxide solution; an electrochemical cell involving the production or consumption of at least one gas, said electrochemical cell comprising said ion-permeable web-reinforced separator; and the use thereof in an electrochemical cell involving the production or consumption of at least one gas.

Solid oxide fuel cells that include an alumina substrate as support are described. The alumina substrate supported SOFCs can exhibit desirable electrochemical characteristics including high performance at intermediate temperatures and excellent thermal stability. The alumina substrate support is formed according to a modified phase-inversion process that forms a series of aligned micro-channels extending from a first side to a second opposite side of the support enabling gas distribution between an electrode (e.g., an anode) located on one side of the alumina substrate and the other, opposite side of the alumina substrate.

Solid oxide fuel cells that include an alumina substrate as support are described. The alumina substrate supported SOFCs can exhibit desirable electrochemical characteristics including high performance at intermediate temperatures and excellent thermal stability. The alumina substrate support is formed according to a modified phase-inversion process that forms a series of aligned micro-channels extending from a first side to a second opposite side of the support enabling gas distribution between an electrode (e.g., an anode) located on one side of the alumina substrate and the other, opposite side of the alumina substrate.

Implementations of a solid oxide fuel cell (SOFC) include a current collector, an electrolyte layer, and an anode. The electrolyte layer may be a solid electrolyte layer. The anode may include one or more micro-pathways that extend between the current collector and the electrolyte layer. The micro-pathways may be constructed of yttria stabilized zirconia (YSZ). Each micro-pathway is in contact with the electrolyte layer and provides a direct pathway between the electrolyte layer and the current collector. The direct pathway created by the micro-pathways may be the shortest distance between the electrolyte layer and the current collector. Each of the one or more micro-pathways may be coated with electrocatalyst nanoparticles. A barrier material may be disposed between each micro-pathway and the current collector to prevent contact between the current collector and the electrocatalyst nanoparticles.

Implementations of a solid oxide fuel cell (SOFC) include a current collector, an electrolyte layer, and an anode. The electrolyte layer may be a solid electrolyte layer. The anode may include one or more micro-pathways that extend between the current collector and the electrolyte layer. The micro-pathways may be constructed of yttria stabilized zirconia (YSZ). Each micro-pathway is in contact with the electrolyte layer and provides a direct pathway between the electrolyte layer and the current collector. The direct pathway created by the micro-pathways may be the shortest distance between the electrolyte layer and the current collector. Each of the one or more micro-pathways may be coated with electrocatalyst nanoparticles. A barrier material may be disposed between each micro-pathway and the current collector to prevent contact between the current collector and the electrocatalyst nanoparticles.