A novel electrochemical cell is disclosed in multiple embodiments. The instant invention relates to an electrochemical cell design. In one embodiment, the cell design can electrolyze water into pressurized hydrogen using low-cost materials. In another embodiment, the cell design can convert hydrogen and oxygen into electricity. In another embodiment, the cell design can electrolyze water into hydrogen and oxygen for storage, then later convert the stored hydrogen and oxygen back into electricity and water.

An electrolytic water production device 1 includes an electrolytic chamber 40 to which water to be electrolyzed is supplied, a first power feeder 41 and a second power feeder 42 arranged to face each other in the electrolytic chamber 40 and having different polarity, a membrane 43 arranged between the first power feeder 41 and the second power feeder 42 so as to divide the electrolytic chamber 40 into a first pole chamber (40a) positioned on a side of the first power feeder 41 and a second pole chamber (40b) positioned on a side of the second power feeder 42, and a control unit 5 for switching the polarity of the first power feeder 41 and the second power feeder 42 between anode and cathode, wherein surfaces of the first power feeder 41 and the second power feeder 42 are formed of a hydrogen storage metal, and the control unit 5 has an operation mode for switching the polarity each time electrolysis is started in the electrolytic chamber 40.

The present invention provides a chlorine dioxide manufacturing device that can accurately control the amount of chlorine dioxide produced. The present invention provides a chlorine dioxide gas manufacturing device comprising an electrolysis chamber, a liquid surface level measuring chamber, and a bubbling gas feeding device. The electrolysis chamber and the liquid surface level measuring chamber each comprises an electrolytic solution and a gas, wherein the electrolytic solution comprises an aqueous chlorite solution, and the electrolysis chamber and the liquid surface level measuring chamber are joined to each other above each liquid surface via a gas piping and joined to each other below each liquid surface via an electrolytic solution piping so that the height of the electrolytic solutions contained in each chamber are substantially equal.

Systems and processes for the production of hydrogen (H2) gas and oxygen (O2) gas from an aqueous electrolyte solution are described. A water-splitting system can include a reactor that includes H2 and O2 generating chambers that can be separate chambers but are not separated by a H2 and/or O2 gas permeable material. The H2 generating chamber can include a cathode and at least a first fluid inlet. The O2 generating chamber can include an anode in electrical communication with the cathode and at least a first fluid inlet. The first and second fluid inlets can each be configured to receive a purged electrolyte solution, a purge gas, or a mixture thereof.

The invention relates to an electrode arrangement (10) for electrochemically treating a liquid. The electrode arrangement (10) has two electrodes (2), each of which has at least one electrode surface (4) and at least one through-flow chamber (34) with at least one inlet (22) and at least one outlet (24). The at least one through-flow chamber (34) is delimited on at least one first face by at least one electrode (2) which has a structure (8) on its electrode surface (4) such that a distance between the electrode surface (4) and a second through-flow chamber (34) face lying opposite the first face is varied. The invention is characterized in that the structure (8) forms at least 30% of the electrode surface (4) and is designed such that the distance between the electrode surface (4) and the second face increases and decreases multiple times along at least one direction, and the liquid flowing through the through-flow chamber (34) is mixed by means of the structure (8) and is set into a turbulent flow in particular.

A system and a method for the recovery of carbon dioxide from a gas containing it. The system of the invention includes: pressurizing means for pressurizing the gas, an absorption tank for absorbing into water the carbon dioxide contained in a gas pressurized with the pressurizing means, a desorption tank for desorbing from water the carbon dioxide absorbed in water, means for circulating water from the absorption tank into the desorption tank and from the desorption tank back into the absorption tank, and recovering means for the recovery of carbon dioxide capable of being desorbed from the water. The system's absorption tank houses an agitator with a function of enabling water to circulate in the absorption tank by ejecting it into an air space of the absorption tank and by spreading in the absorption tank's air space over an area as extensive as possible.

An electrochemical device is provided that includes a stack of a plurality of electrochemical units that succeed one another in a stacking direction and each include an electrochemically active membrane electrode assembly, at least one gas diffusion layer and a bipolar plate having at least one flow field, in which at least one flow field is sealed off simply and reliably and the occurrence of parasitic flows is prevented, wherein at least one bipolar plate has at least one edge web, which borders a flow field of the bipolar plate and is in contact with a gas diffusion layer adjacent to the bipolar plate, and wherein the electrochemical device further includes at least one flow field seal element that seals off the flow field bordered by the edge web and is in contact with the edge web and in contact with the gas diffusion layer.

The present embodiments provide a reduction catalyst realizing high reaction efficiency and a reduction reactor employing the catalyst. The reduction catalyst of the embodiment comprises an electric conductor and an organic layer having organic modifying groups placed on the surface of the conductor. The organic modifying groups have an aromatic ring having two or more nitrogen atoms. The reduction catalyst is used in a reduction reactor, and the reactor is also provided.

An electrochemical reduction device includes an electrode unit, a power control unit, an organic material storage tank, a concentration measurement unit, a water storage tank, a gas-water separation unit, and a control unit. The electrode unit includes an electrolyte membrane, a reduction electrode, and an oxygen evolving electrode. The control unit controls the power control unit so as to satisfy a relation of V.sub.HERV.sub.allowV.sub.CAV.sub.TRR when the potential at a reversible hydrogen electrode, the standard redox potential of the aromatic compound, and the potential of the reduction electrode are expressed as V.sub.HER, V.sub.TRR, and V.sub.CA, respectively. V.sub.allow is adjusted according to the concentration of the aromatic compound measured by the concentration measurement unit.

In a water electrolysis system and a control method therefor, when a depressurizing process is performed, pressure reducing valves for high pressure reduce the pressure of a high pressure hydrogen. A first pressure detecting sensor detects, as a first pressure, a pressure of the high pressure hydrogen on a more upstream side than the pressure reducing valves for high pressure. A second pressure detecting sensor detects, as a second pressure, a pressure of the high pressure hydrogen on a more downstream side than a first pressure reducing valve of the pressure reducing valves for high pressure. Based on the first pressure or the second pressure, a controller controls a degree of opening of a depressurization control valve.