The present invention concerns a method of retrofitting of a membrane electrolysis cell, wherein a rigid cathode is shaped by plastic deformation of the regions in correspondence of cathodic supports; a pre-shaped conductive elastic element having compressed regions in correspondence of said cathodic supports is overlaid onto said rigid cathode; a flexible planar cathode provided with a catalytic coating is overlaid onto said conductive elastic element. The invention also concerns a correspondingly retrofitted electrolysis cell.

The invention relates to a cell of a modular electrolyzer having a frame-shaped flange formed by two superposed elements, welded along the internal periphery in order to increase the local flange thickness in a portion of higher exposure to corrosion, for the sake of improving its resistance. A method of repairing electrolysis cells having a frame-shaped flange formed by two superposed elements by removing and replacing only the outermost frame, more subject to corrosion, is also described.

A syngas generation system that combines a solid oxide electrolysis cell (SOEC) and a carbon gasification unit is described. On the cathode side of the SOEC, CO.sub.2 and H.sub.2O are electrochemically converted to syngas. At the anode side of the system, a second stream of syngas is produced through a carbon gasification process in which solid carbon is reacted with H.sub.2O/CO.sub.2. Oxygen ion transported across the SOEC electrolyte reacts at the anode with a portion of the syngas produced in the gasification process. This reaction product (H.sub.2O/CO.sub.2) can be fed back to the gasification unit.

A high pressure water electrolysis device includes an electrolyte membrane, an anode power supplying body, a cathode power supplying body, an anode separator, a cathode separator, a cathode chamber, a seal member, and a protective sheet member. The protective sheet member is interposed between the electrolyte membrane and the anode power supplying body and includes a frame part and a through hole formation part. The frame part faces the seal member as a seal receiving part in a stacking direction. The through hole formation part is provided inwardly of the frame part. In the through hole formation part, a plurality of through holes are provided. The through hole formation part has the plurality of through holes from an inner side to outer side of a range that faces an anode catalyst part in the stacking direction.

Disclosed is a pipe-type electrolysis cell including: a pair of terminal electrodes including an outer electrode and an inner electrode that are electrically connected to each other at respective first ends thereof and separated from each other at respective second ends thereof; and a bipolar electrode installed between the terminal electrodes and electrically insulated the terminal electrodes.

A heat exchanger can be integrated into an interconnector that can be used in both a SOFC fuel cell and an EHT electrolyser, which allows a heat-transfer fluid different from that in the reactive and drainage gas circuits to be circulated from the inlet of the reactor, thereby allowing the best possible management of the exothermic operating modes of the SOFC cell and the exothermic or endothermic operating modes of the EHT electrolyser and the SOFC cell, especially in the absence of current for the latter.

A hydrogen and oxygen generator has two end plates, at least two electrode assemblies defining an electrolysis chamber therebetween and being disposed between the two end plates, and at least one fastener connecting the two end plates together. Each electrode assembly has a plate defining an electrode portion having a perimeter and defining inlet and outlet apertures, an inlet insulating grommet disposed in the inlet aperture and covering an edge thereof, an outlet insulating grommet disposed in the outlet aperture and covering an edge thereof, and an insulating band disposed around the electrode portion and covering an edge of the electrode portion defining the perimeter. The insulating bands of the at least two electrode assemblies abut each other. The inlet and outlet apertures of the at least two electrode assemblies fluidly communicate with the electrolysis chamber. An electrode assembly and a hydrogen and oxygen generation system are also disclosed.

In a hydrogen producing device, an electrolyte flow path between a plurality of hydrogen producing cells is disposed in a hydrogen production side and in an oxygen production side, separately. Further, an electrolyte flow path is formed through which the electrolyte flows downward from the top between the plurality of hydrogen producing cells, and on the other hand the electrolyte flows upward from the bottom within each hydrogen producing cell. Moreover, a contact point with a produced gas or an atmosphere is provided in a pathway of the electrolyte flow path.

An electrolysis method comprising an electrolysis cell (4), which method uses at least one recirculating flushing medium (50, 60). The invention further relates to an electrolysis system, in particular for carrying out the electrolysis method.

An assembly of electrochemical cells for an electrochemical reactor, including a first electrochemical cell, including a first membrane/electrode assembly including a first anode and a first cathode on either side of a proton exchange membrane; first and second flow guides positioned on either side of the first assembly; a second electrochemical cell, including a second membrane/electrode assembly including a second anode and a second cathode on either side of a proton exchange membrane; third and fourth flow guides on either side of the second membrane/electrode assembly; the first and third flow guides have one and the same geometry; the first anode and the second anode have different distributions of surface densities of electrocatalytic material on respective faces of the first and second proton exchange membranes.