A device and method of controlling an electrode and electrolytic cell are provided, which independently utilizes clean energy with large power fluctuation range as an electrolysis power source for hydrogen and oxygen production. The basic number of electrodes is set by the minimum cut-in voltage value of fluctuating power sources such as wind or solar power. According to fluctuating power sources such as wind or solar power, the ratio of the minimum cut-in current and the reference current corresponding to the lowest cut-in voltage value sets the effective size of the electrodes to be connected in or cut out.

A method for obtaining a product by electrolysis, including: a) determining a set point for a production output by minimizing a first mathematical function, which depends on the production output and on a predicted product demand; b) determining respective set points for multiple process parameters by minimizing a second mathematical function, which depends on the set point for the production output determined in a), on the process parameters and on predicted degradation effects; c) determining respective set points for changes of multiple control parameters by minimizing a third mathematical function, which depends on the set points for the process parameters determined in b) and on the changes of the control parameters; and d) obtaining the product by performing the electrolysis using the set points for the changes of the control parameters determined in c).

The present invention relates to: oxygen carrier particles having a metal oxide-perovskite core-shell structure; and a chemical-looping thermochemical water/carbon dioxide splitting process using the same. By using the oxygen carrier particles having a metal oxide-perovskite core-shell structure in the chemical-looping thermochemical water/carbon dioxide splitting process, it is possible to produce hydrogen/carbon monoxide from water/carbon dioxide in high yield by efficiently overcoming the disadvantages of conventionally used oxygen carrier particles.

An electrolysis system includes at least one H.sub.2O electrolysis apparatus that electrolyzes water to produce hydrogen; and at least one CO.sub.2 electrolysis apparatus that electrolyzes carbon dioxide to produce carbon monoxide. The electrolysis system includes a co-electrolysis apparatus that co-electrolyzes water and carbon dioxide to produce less hydrogen per unit time than produced by the at least one H.sub.2O electrolysis apparatus and less carbon monoxide per unit time than produced by the at least one CO.sub.2 electrolysis apparatus.

A controller and an operation control method for electrolysis stack module powered by a renewable energy power generation device and an electrolysis system using the same, the controller being configured to control power supply by receiving the power supply from a renewable energy generator and distributing the power supply to n (n≥2) electrolysis stacks, wherein, the controller is configured to determine whether or not to drive each electrolysis stack according to stack driving conditions, no less than two, determined on the basis of a preset minimum amount of operating power supply for each electrolysis stack, and the stack driving conditions are ranges of an amount of the power supply in which on/off of the electrolysis stacks is predetermined, and the controller is configured to control driving of the electrolysis stacks according to the stack driving conditions corresponding to the amount of supplied power from the renewable energy generator.

An electrochemical cell comprises a first electrode, a second electrode, and a proton-conducting membrane between the first electrode and the second electrode. The first electrode comprises Pr(Co.sub.1-x-y-z, Ni.sub.x, Mn.sub.y, Fe.sub.z)O.sub.3-δ, wherein 0≤x≤0.9, 0≤y≤0.9, 0≤z≤0.9, and δ is an oxygen deficit. The second electrode comprises a cermet material including at least one metal and at least one perovskite. Related structures, apparatuses, systems, and methods are also described.

The present invention provides a process for producing hydrogen iodide. The process includes providing a vapor-phase reactant stream comprising hydrogen and iodine and reacting the reactant stream in the presence of a catalyst to produce a product stream comprising hydrogen iodide. The catalyst includes at least one selected from the group of nickel, cobalt, iron, nickel oxide, cobalt oxide, and iron oxide. The catalyst is supported on a support.

A hydrogen supply device disposed in a high-potential section includes a bottle internally provided with a hydrogen absorbing alloy.

Methods and systems related to the field of carbon capture and utilization are disclosed. Disclosed electrolysis reactors can have a cathode area having a cathode output and a cathode input for an input fluid and an anode area having an anode input and an anode output. The carbon input fluid contains carbon dioxide. The cathode area reduces an oxygen-containing species into hydroxide ions and reacts them with the carbon dioxide to form anions containing carbon. The anode area oxidizes one or more oxidizable species to generate a protonating species. The electrolysis reactors can have a third output for a carbon output fluid. The electrolysis reactors can begin to produce carbon dioxide from the anions containing carbon and the protonating species in response to a potential of less than 1.23 V applied across the cathode terminal and the anode terminal.

An electrocatalyst includes a carbon substrate, metal oxide particles dispersed on the carbon substrate, and metal catalyst particles. The metal catalyst particles are metal substitutions in the metal oxide particles, or adsorbed on the metal oxide particles.