Siemens Aktiengesellschaft

Fraunhofer-Gesellschaft Zur Foerderung Der Angewandten Forschung E.V.

Siemens Energy, Inc.

Epcos Ag

Siemens Energy Global Gmbh & Co. Kg

Harald Landes

Wolfgang Drenckhahn

Horst Greiner

Carsten Schuh

Thomas Soller

Wolfram Wersing

Norbert Huber

Robert Fleck

Norbert Kellner

Marc Hanebuth

Uday B Pal

Katrin Benkert

Alexander Hahn

Nicolas Vortmeyer

Hartmut Michel

Wolfgang Weydanz

Shailesh D Vora

Michael Meinert

Karsten Rechenberg

Christian Reller

Wolfgang Menapace

Johann Holweg

Christoph Weber

Harald Schmidt

Alessandro Zampieri

Andree Schwake

Ruth M Anner

Manfred Schn Oller

Elvira María Fernández Sanchis

Christoph N Olscher

Ellen Ivers-Tiffee

Roland Reichenbacher

Martin Ise

André Leonide

Edith Kirchner

Barbara Schricker

Hermann Schichl

Franz Richter

Rolf Neubert

Jochen SCHÄFER

Elvira María FERNÁNDEZ Sanchis

Marco Cologna

Various embodiments may include an electrolyzer for electrochemical utilization of carbon dioxide comprising: electrolysis cell defining an anode space and a cathode space; an anode in the anode space; a cathode in the cathode space; a first cation-permeable membrane disposed between the anode space and the cathode space; and a second anion-selective membrane disposed between the first cation-permeable membrane and the cathode. The anode directly adjoins the first cation-permeable membrane. The second anion-selective membrane directly adjoins the first cation-permeable membrane and the second anion-selective membrane directly adjoins the cathode.

Device and method for the electrochemical utilisation of carbon dioxide

The present disclosure relates to semiconductors. Some embodiments may include a series circuit arrangement of power semiconductors comprising: cooling-water boxes arranged on the semiconductors and electrically connected to them; two cooling-water distributor lines; respective branchings on the cooling-water distributor lines for the cooling chambers; and a control electrode arranged on the cooling-water distributor lines. The cooling chambers are connected in parallel between the cooling-water distributor lines with respect to a cooling-water stream. The cooling chambers are connected to the branchings via a respective connecting line. For at least some of the cooling chambers, the branchings on the cooling-water distributor lines are arrayed relative to the position of the respective cooling chamber in offset manner in relation to a geometrically shortest possible link to the cooling-water distributor lines, so that a difference of potential between the cooling chambers and the branchings is minimized.

Series circuit arrangement of power semiconductors

An electrical energy store is provided, including a storage cell, which in turn has an air electrode, which is connected to air channels in an air supply device, and a storage electrode, wherein the storage electrode adjoins a storage structure, wherein electrical contacts rest on the storage electrode, further wherein contact pins which protrude out of a surface of the storage structure are integrated in the storage structure, and the contact pins are in electrical contact with the storage electrode.

Electrical energy store

An electric energy store includes a positive electrode, a negative electrode and an oxygen ion conducting electrolyte separating the positive electrode and the negative electrode from each other. The negative electrode includes a first reservoir having a gas-permeable oxidizable material and, contained therein, a gaseous, oxygen-exchanging redox pair. The positive electrode comprises a second reservoir having a gas-permeable oxidizable material and oxygen transport is effected by means of an oxygen-containing gaseous compound, wherein the positive electrode is closed with respect to the atmosphere.

Electric energy store

An energy store is provided, having at least one stack, each stack having at least one storage cell, which in turn has an air electrode and a storage electrode. The storage electrode is adjacent to channels, which contain a storage medium and water vapor. The channels have a larger cross-sectional area than the cross-section of the storage medium, which condition causes unhindered spreading of a reaction gas in the area between the storage electrode and the storage medium.

An electrical energy store having at least one stack with in each case at least one storage cell. Each storage cell has an air electrode, which is connected to an air supply apparatus, and a storage electrode. The storage electrode adjoins channels which contain a storage medium and a steam/hydrogen mixture. A reservoir of steam/hydrogen is provided, the reservoir being directly connected to the channels.

A storage structure of an electrical energy storage cell is provided having an active storage material, wherein the active storage material has a particle size distribution which has a dvalue of at least 0.1 &#x3bc;m and a dvalue of between 0.8 &#x3bc;m and 1.1 &#x3bc;m, wherein the dvalue of the particle size distribution is lower than 10 &#x3bc;m.

Storage structure of an electrical energy storage cell

An energy storage device for a reversible storage of energy has a reversibly designed metal/metal oxide storage unit for indirectly storing energy in form of a fluid material and a reversibly designed electrolysis device for providing and using the fluid material in an electrolysis reaction. The metal/metal oxide storage unit is disposed spatially separated from the electrolysis device. A fluid exchanging unit is provided for exchanging the fluid material between the reversibly designed metal/metal oxide storage unit and the electrolysis device, and a heat exchanging unit is provided for exchanging thermal energy between the metal/metal oxide storage unit and the electrolysis device. Further, a method for a reversible storage of energy is provided.

Energy storage device and method for the reversible storage of energy

An electrical energy storage device is provided which comprises at least one module with a negative electrode, a positive electrode made from an anion generating material or material combination and conducting anions, and an anion conducting solid electrolyte located between the negative electrode and the positive electrode. The negative electrode of each module comprises a porous structure that conducts anions and the pore space of which is at least partially filled by a first redox mass which comprises a metal/metal oxide pair. The positive electrode of each module comprises a porous structure that conducts anions and the pore space of which is at least partially filled by a second redox mass which comprises a metal/metal oxide pair with an increased oxidation potential compared to the first redox mass.

Electrical energy storage device

A battery has a cathode and an anode, between which a solid electrolyte is disposed. The battery has a process gas feed on the cathode side. The battery is characterized in that an electrically conductive supporting body is disposed on the cathode surface. At least one chamber connected to the anode has a porous, oxidizable material and a redox pair that is gaseous at an operating temperature of the battery.

Electrochemical battery

A high-temperature fuel cell system includes individual SOFC fuel cells which are in contact with each other for electrically connecting the same in parallel or in series. In at least one embodiment, contacting elements that are suitable for the fuel cell system with a certain flexibility in addition to the required electrical conductivity for continuous operation. The contacting elements between two fuel cells are formed by a metal wire mesh that is advantageously made of nickel. Such nickel wires can be mechanically transformed into a continuous mesh, especially a tube, from which sections having a suitable length can be cut and be provided with the proper shape.

High-temperature fuel cell system and method for the production of contacting elements for such a fuel cell system

Disclosed is a high-temperature fuel cell system including individual SOFC fuel cells which are in contact with each other to be electrically connected in parallel or in series. Contacting elements are provided, in at least one embodiment, that are suitable for the fuel cell system with a certain flexibility in addition to electrical conductivity for continuous operation. The contacting elements are provided, in at least one embodiment, between two fuel cells with an outer, metallically conductive jacket and a ceramic core. For example, ceramic felts can be enveloped by a nickel net by adequately shaping the same.

A double-layer capacitor includes a first electrode having a first polarity, a second electrode having a second polarity, the first polarity being different from the second polarity, and an electrolyte that is in contact with the first electrode and the second electrode. The first electrode has a first charge of the first polarity and the second electrode has a second charge of the second polarity, and maximum values of the first charge and the second charge are substantially equal.

Double-layer capacitor, use of the same, and method for increasing the maximum charges of double-layer capacitor electrodes

A high temperature fuel cell has a cathode which comprises at least a first layer and a second layer disposed on one side of the first layer, in which the first layer contains 30 to 60% by weight of a first electrolyte made up of zirconium oxide ZrO and at least one proportion of scandium oxide Sc O , and the second layer comprises substoichiometric lanthanum strontium manganate having the formula La Sr MnO in which the sum of x and y is less than 1. By means of this, a high ionic conductivity is achieved for the cathode ( ). The ionic conductivity further remains substantially constant as a function of the operating time t.

High temperature fuel cell

High-temperature fuel cell with improved solid-electrolyte/electrode

Growing community of inventors

Rückersdorf, Germany

Harald Landes