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.

An electrolysis system, comprising a power supply configured to provide an input voltage; and a controller configured to receive the input voltage and output a pulse width modulated voltage, the output voltage being a 30V square wave having a variable duty cycle in the range of 1% to 10%. The system further comprises at least one electrolysis cell configured to receive the output voltage, each electrolysis cell comprising a plurality of metal plates, each electrolysis cell being configured for receiving water containing an electrolyte to split the water when the output voltage is received.

Hydrogen is produced by electrolysis of water using electricity generated from a renewable energy source such as wind and/or solar radiation, compressed in a multistage compression system and consumed in at least one downstream process. Supply of hydrogen to the downstream process(es) fluctuates with demand and/or the availability of the renewable energy source. In order to accommodate such fluctuations, excess hydrogen is stored during periods when production of hydrogen exceeds that required by the downstream process(es) so that, during periods when demand exceeds production, hydrogen is removed from storage and, after suitable pressure reduction, fed to the downstream process(es) via a stage of the multistage compression system.

The present disclosure relates to a system for producing hydrogen from renewable energy and a control method thereof. The system includes a renewable-energy-based power generation system, a primary hydrogen production system, a secondary hydrogen production system, and a controller. An output end of the renewable-energy-based power generation system is connected to the primary hydrogen production system and the secondary hydrogen production system via an electrical conversion device. A capacity of the primary hydrogen production system is greater than or equal to a capacity of the secondary hydrogen production system. The controller is configured to monitor an output electrical performance parameter of the renewable-energy-based power generation system in real time, and control turn on and turn off of the primary hydrogen production system and the secondary hydrogen production system.

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.

A series of cells for use in an electrochemical device, such as an electrochemical cell or battery, that can operate in a single bulk electrolyte solution shared among the cells. Methods of producing hydrogen or both hydrogen and electricity in appreciable quantifies and in various ratios, and vehicles or other devices and applications powered by electrochemical devices comprising the series.

A series of cells for use in an electrochemical device, such as an electrochemical cell or battery, that can operate in a single bulk electrolyte solution shared among the cells. Methods of producing hydrogen or both hydrogen and electricity in appreciable quantifies and in various ratios, and vehicles or other devices and applications powered by electrochemical devices comprising the series.

The efficiency of a carbon dioxide reduction reaction at a reduction electrode is improved. An oxidation tank including an oxidation electrode, a reduction tank which is adjacent to the oxidation tank and to which carbon dioxide is supplied, and a gas reduction sheet located between the oxidation tank and the reduction tank are included, the gas reduction sheet is a sheet in which an ion exchange membrane and a reduction electrode are laminated, the ion exchange membrane is located on the oxidation tank side, the reduction electrode is located on the reduction tank side, is connected to the oxidation electrode by a lead, and conduct conducts a reduction reaction of the carbon dioxide by a current flowing through the lead.

The efficiency of a carbon dioxide reduction reaction at a reduction electrode is improved. An oxidation tank including an oxidation electrode, a reduction tank which is adjacent to the oxidation tank and to which carbon dioxide is supplied, and a gas reduction sheet located between the oxidation tank and the reduction tank are included, the gas reduction sheet is a sheet in which an ion exchange membrane and a reduction electrode are laminated, the ion exchange membrane is located on the oxidation tank side, the reduction electrode is located on the reduction tank side, is connected to the oxidation electrode by a lead, and conduct conducts a reduction reaction of the carbon dioxide by a current flowing through the lead.