Provided is an electrode for electrolysis and a preparation method of the same. The electrode for electrolysis has an improved needle-like structure of a rare earth metal compared to conventional electrodes, and thus detachment of catalytic materials is reduced, so that the electrode is excellent in durability such as exhibiting stable performance even in a reverse current flow. Further, since the electrode for electrolysis has a low overvoltage value, an overvoltage required amount of the electrolytic cell can be remarkably reduced. In addition, an electrode for electrolysis having the above effect can be prepared without introducing additional precursors or changing manufacturing facilities.

Composite electrocatalytic materials for catalyzing water splitting are provided. Such materials may comprise a porous, conductive support composed of a transition metal foam, the support having a surface, and a coating on the surface of the support. The coating may comprise nanorods of a first transition metal chalcogenide, each nanorod anchored on one end to the surface of the support and extending perpendicularly away from the surface of the support to a free opposing end, nanosheets of a second transition metal chalcogenide, the nanosheets coating a surface of the nanorods of the first transition metal chalcogenide, and nanosheets of a third transition metal chalcogenide, the nanosheets also coating the surface of the nanorods of the first transition metal chalcogenide.

This invention relates generally to novel methods and novel devices for the continuous manufacture of nanoparticles, microparticles and nanoparticle/liquid solution(s). The nanoparticles (and/or micron-sized particles) comprise a variety of possible compositions, sizes and shapes. The particles (e.g., nanoparticles) are caused to be present (e.g., created) in a liquid (e.g., water) by, for example, preferably utilizing at least one adjustable plasma (e.g., created by at least one AC and/or DC power source), which plasma communicates with at least a portion of a surface of the liquid. At least one subsequent and/or substantially simultaneous adjustable electrochemical processing technique is also preferred. Multiple adjustable plasmas and/or adjustable electrochemical processing techniques are preferred. The continuous process causes at least one liquid to flow into, through and out of at least one trough member, such liquid being processed, conditioned and/or effected in said trough member(s). Results include constituents formed in the liquid including micron-sized particles and/or nanoparticles (e.g., metallic-based nanoparticles) of novel size, shape, composition and properties present in a liquid.

This invention relates generally to novel methods and novel devices for the continuous manufacture of nanoparticles, microparticles and nanoparticle/liquid solution(s). The nanoparticles (and/or micron-sized particles) comprise a variety of possible compositions, sizes and shapes. The particles (e.g., nanoparticles) are caused to be present (e.g., created) in a liquid (e.g., water) by, for example, preferably utilizing at least one adjustable plasma (e.g., created by at least one AC and/or DC power source), which plasma communicates with at least a portion of a surface of the liquid. At least one subsequent and/or substantially simultaneous adjustable electrochemical processing technique is also preferred. Multiple adjustable plasmas and/or adjustable electrochemical processing techniques are preferred. The continuous process causes at least one liquid to flow into, through and out of at least one trough member, such liquid being processed, conditioned and/or effected in said trough member(s). Results include constituents formed in the liquid including micron-sized particles and/or nanoparticles (e.g., metallic-based nanoparticles) of novel size, shape, composition and properties present in a liquid.

There is provided a fluorine gas production device in which, even when an electrolytic solution containing hydrogen fluoride is electrolyzed at a high current density, a recombination reaction in the electrolytic solution and a recombination reaction in gas phase parts of an anode chamber and a cathode chamber are less likely to occur and the electrolytic solution can be electrolyzed with high current efficiency to produce fluorine gas. The fluorine gas production device includes an electrolytic cell (1), a partition wall (7) extending downward in the vertical direction from the ceiling surface inside the electrolytic cell (1) to partition the electrolytic cell (1) into an anode chamber (12) and a cathode chamber (14), an anode (3), and a cathode (5). The lower end of the partition wall (7) is immersed in the electrolytic solution (10) and a length (H) in the vertical direction of a portion immersed in the electrolytic solution (10) of the partition wall (7) is 10% or more and 30% or less of the distance from the bottom surface inside the electrolytic cell (1) to the liquid level of the electrolytic solution (10). The cathode (5) is completely immersed in the electrolytic solution (10) and the upper end of the cathode (5) is arranged at a lower position in the vertical direction relative to the lower end of the partition wall (7). The anode 3 is partially exposed from the liquid level of the electrolytic solution (10).

There is provided a fluorine gas production device in which, even when an electrolytic solution containing hydrogen fluoride is electrolyzed at a high current density, a recombination reaction in the electrolytic solution and a recombination reaction in gas phase parts of an anode chamber and a cathode chamber are less likely to occur and the electrolytic solution can be electrolyzed with high current efficiency to produce fluorine gas. The fluorine gas production device includes an electrolytic cell (1), a partition wall (7) extending downward in the vertical direction from the ceiling surface inside the electrolytic cell (1) to partition the electrolytic cell (1) into an anode chamber (12) and a cathode chamber (14), an anode (3), and a cathode (5). The lower end of the partition wall (7) is immersed in the electrolytic solution (10) and a length (H) in the vertical direction of a portion immersed in the electrolytic solution (10) of the partition wall (7) is 10% or more and 30% or less of the distance from the bottom surface inside the electrolytic cell (1) to the liquid level of the electrolytic solution (10). The cathode (5) is completely immersed in the electrolytic solution (10) and the upper end of the cathode (5) is arranged at a lower position in the vertical direction relative to the lower end of the partition wall (7). The anode 3 is partially exposed from the liquid level of the electrolytic solution (10).

The invention relates to a device, including: a channel including an inlet at a first end of the channel and an outlet at a second end of the channel; a cathode arranged in the channel, which cathode includes a first segment selected from titanium, stainless steel and titanium provided with a mixed metal oxide coating layer including ruthenium oxide and/or iridium oxide and a second segment including carbon, such as a carbon (felt) segment, arranged downstream of the first segment, an anode, arranged in the channel, selected from titanium or, stainless steel and titanium provided with a mixed metal oxide coating layer including ruthenium oxide and/or iridium oxide, which coating layer faces the cathode; and a power source electrically connected to the cathode and the anode. The invention further relates to a method for the production of chlorine dioxide.

The invention relates to a device, including: a channel including an inlet at a first end of the channel and an outlet at a second end of the channel; a cathode arranged in the channel, which cathode includes a first segment selected from titanium, stainless steel and titanium provided with a mixed metal oxide coating layer including ruthenium oxide and/or iridium oxide and a second segment including carbon, such as a carbon (felt) segment, arranged downstream of the first segment, an anode, arranged in the channel, selected from titanium or, stainless steel and titanium provided with a mixed metal oxide coating layer including ruthenium oxide and/or iridium oxide, which coating layer faces the cathode; and a power source electrically connected to the cathode and the anode. The invention further relates to a method for the production of chlorine dioxide.

Devices for electrochemically activating precursor compound through oxidation (or reduction) to produce active compound are provided. Devices may include an electrochemical reactor having an electrochemical cell including an anode and a cathode housed in a shared compartment, or an anode housed in an anode compartment, a cathode housed in a cathode compartment, and a semipermeable membrane separating the anode and cathode compartments, wherein the anode and cathode form an electrical circuit in the presence of electrolyte solution; and a sealed housing enclosing the electrochemical cell, the housing including a precursor compound input in communication with the anode/cathode/shared compartment, for inputting precursor compound, an active compound output in communication with the anode/cathode/shared compartment for outputting activated compound following activation, and a gas release and/or liquid overflow port; a power supply powering the electrochemical reactor; and, optionally, a pump or valve controlling flow rate of the assembly.

Devices for electrochemically activating precursor compound through oxidation (or reduction) to produce active compound are provided. Devices may include an electrochemical reactor having an electrochemical cell including an anode and a cathode housed in a shared compartment, or an anode housed in an anode compartment, a cathode housed in a cathode compartment, and a semipermeable membrane separating the anode and cathode compartments, wherein the anode and cathode form an electrical circuit in the presence of electrolyte solution; and a sealed housing enclosing the electrochemical cell, the housing including a precursor compound input in communication with the anode/cathode/shared compartment, for inputting precursor compound, an active compound output in communication with the anode/cathode/shared compartment for outputting activated compound following activation, and a gas release and/or liquid overflow port; a power supply powering the electrochemical reactor; and, optionally, a pump or valve controlling flow rate of the assembly.