Patent classifications
C25B11/04
Electrochemical cells for hydrogen gas production and electricity generation, and related systems and methods
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.
CATALYST ELECTRODES, AND METHODS OF MAKING AND USING THE SAME
Methods of making catalyst electrodes comprising sputtering at least Pt and Ir onto nanostructured whiskers to provide multiple alternating layers comprising, respectively in any order, at least Pt and Ir. In some exemplary embodiments, catalyst electrodes described, or made as described, herein are anode catalyst, and in other exemplary embodiments cathode catalyst. Catalysts electrodes are useful, for example, in generating H.sub.2 and O.sub.2 from water.
CATALYST ELECTRODES, AND METHODS OF MAKING AND USING THE SAME
Methods of making catalyst electrodes comprising sputtering at least Pt and Ir onto nanostructured whiskers to provide multiple alternating layers comprising, respectively in any order, at least Pt and Ir. In some exemplary embodiments, catalyst electrodes described, or made as described, herein are anode catalyst, and in other exemplary embodiments cathode catalyst. Catalysts electrodes are useful, for example, in generating H.sub.2 and O.sub.2 from water.
METHANOL GENERATION DEVICE, METHOD FOR GENERATING METHANOL, AND ELECTRODE FOR GENERATING METHANOL
The present invention provides a methanol generation device for generating methanol by reducing carbon dioxide, comprising: a container for storing an electrolyte solution containing carbon dioxide; a cathode electrode disposed in the container so as to be in contact with the electrolyte solution; an anode electrode disposed in the container so as to be in contact with the electrolyte solution; and an external power supply for applying a voltage so that a potential of the cathode electrode is negative with respect to a potential of the anode electrode. The cathode electrode has a region of Cu.sub.1-x-yNi.sub.xAu.sub.y (0<x, 0<y, and x+y<1). The anode electrode has a region of a metal or a metal compound.
SUPPORTED METAL CATALYST AND ELECTROCHEMICAL CELL
A support and metal catalyst with improved electric conductivity is provided. A support and metal catalyst, including: a support powder; and metal fine particles supported on the support powder; wherein: the support powder is an aggregate of support fine particles; the support fine particles have a chained portion structured by a plurality of crystallites being fusion bonded to form a chain; the support fine particles are structured with metal oxide; and the metal oxide is doped with a dopant element, and an atomic ratio of titanium with respect to total of titanium and tin is 0.30 to 0.80, is provided.
Light absorbing device, manufacturing method thereof, and photoelectrode
This light absorbing device includes: a light reflecting layer; a dielectric layer disposed on the light reflecting layer; and a plurality of metal nanostructures disposed on the dielectric layer. A portion of each of the plurality of metal nanostructures is buried in the dielectric layer and another portion thereof is exposed to the outside.
Electrochemical oxidation of 5-hydroxymethylfurfural using copper-based anodes
Electrochemical cells for the oxidation of 5-hydroxymethylfurfural are provided. Also provided are methods of using the cells to carry out the oxidation reactions. The electrochemical cells and methods use catalytic copper-based anodes to carry out the electrochemical oxidation reactions.
Electrochemical oxidation of 5-hydroxymethylfurfural using copper-based anodes
Electrochemical cells for the oxidation of 5-hydroxymethylfurfural are provided. Also provided are methods of using the cells to carry out the oxidation reactions. The electrochemical cells and methods use catalytic copper-based anodes to carry out the electrochemical oxidation reactions.
PRODUCTION OF HYDROGEN VIA ELECTROCHEMICAL REFORMING
Herein discussed is an electrochemical reactor comprising a mixed-conducting membrane, wherein the membrane comprises an electronically conducting phase and an ionically conducting phase, wherein the reactor is capable of reforming a hydrocarbon electrochemically, wherein the electrochemical reforming reactions involve the exchange of an ion through the membrane to oxidize the hydrocarbon. Further discussed herein is a method of producing hydrogen comprising providing an electrochemical (EC) reactor having a mixed-conducting membrane, introducing a first stream comprising a hydrocarbon to the reactor, introducing a second stream comprising water to the reactor, and reducing the water in the second stream to produce hydrogen, wherein the first stream and the second stream do not come in contact with each other in the reactor, and wherein the hydrocarbon is reformed electrochemically in the EC reactor.
PRODUCTION OF HYDROGEN VIA ELECTROCHEMICAL REFORMING
Herein discussed is an electrochemical reactor comprising a mixed-conducting membrane, wherein the membrane comprises an electronically conducting phase and an ionically conducting phase, wherein the reactor is capable of reforming a hydrocarbon electrochemically, wherein the electrochemical reforming reactions involve the exchange of an ion through the membrane to oxidize the hydrocarbon. Further discussed herein is a method of producing hydrogen comprising providing an electrochemical (EC) reactor having a mixed-conducting membrane, introducing a first stream comprising a hydrocarbon to the reactor, introducing a second stream comprising water to the reactor, and reducing the water in the second stream to produce hydrogen, wherein the first stream and the second stream do not come in contact with each other in the reactor, and wherein the hydrocarbon is reformed electrochemically in the EC reactor.