A hydrogen generating element of an electrochemical apparatus may include a compacted homogenous body of an alloy-like material which contains at least 60 wt.-%, preferably more than 75 wt.-%, of Mg or a Mg alloy, 5 to 20 wt.-% Fe.sub.2O.sub.3, and 5 to 20 wt.-% of an electrolyte precursor material.

A hydrogen generating element of an electrochemical apparatus may include a compacted homogenous body of an alloy-like material which contains at least 60 wt.-%, preferably more than 75 wt.-%, of Mg or a Mg alloy, 5 to 20 wt.-% Fe.sub.2O.sub.3, and 5 to 20 wt.-% of an electrolyte precursor material.

A method of producing graphite may include beneficiating an amount of coal to form a coal char, grinding the coal char to produce a crushed char and placing the crushed char in a porous container. Then, the method includes immersing the porous container in a molten salt bath. The molten salt bath includes a graphite anode. The method further includes applying an electrical potential across the porous container and the graphite anode such that a graphite deposit forms on the graphite anode. The graphite anode is removed from the molten salt bath and the graphite deposit is separated from the graphite anode to produce graphite fragments.

An electrochemical system and process are provided to convert an amount of chalcopyrite (CuFeS.sub.2) to a product including copper ions. In an electrochemical reactor, a potential is applied across an anode and a cathode to convert the chalcopyrite to an intermediate, chalcocite (Cu.sub.2S). The anode is covered to prevent contact with the intermediate, thus limiting subsequent conversion of the intermediate to covellite (CuS) in favor of conversion to a material more suited to chemical oxidation, cuprite (Cu.sub.2O). For example, the anode can be covered with one or more layers of filter paper. Upon application of an oxidizing agent, the cuprite is oxidized to produce a product including copper ions. The cathode and covered anode allow for efficient and inexpensive processing. The cost of this technique is comparable to industry standards, and moreover, has a much smaller environmental footprint than heat-based copper extraction.

An electrochemical system and process are provided to convert an amount of chalcopyrite (CuFeS.sub.2) to a product including copper ions. In an electrochemical reactor, a potential is applied across an anode and a cathode to convert the chalcopyrite to an intermediate, chalcocite (Cu.sub.2S). The anode is covered to prevent contact with the intermediate, thus limiting subsequent conversion of the intermediate to covellite (CuS) in favor of conversion to a material more suited to chemical oxidation, cuprite (Cu.sub.2O). For example, the anode can be covered with one or more layers of filter paper. Upon application of an oxidizing agent, the cuprite is oxidized to produce a product including copper ions. The cathode and covered anode allow for efficient and inexpensive processing. The cost of this technique is comparable to industry standards, and moreover, has a much smaller environmental footprint than heat-based copper extraction.

The present invention relates to a photo-electrochemical device for production of a gas, liquid or solid using concentrated electromagnetic irradiation. The device comprises a photovoltaic component configured to generate charge carriers from the concentrated electromagnetic irradiation; and an electrochemical component configured to carry out electrolysis of a reactant. The photovoltaic component contacts the electrochemical component at a solid interface to form an integrated photo-electrochemical device; and further includes at least one reactant channel or a plurality of reactant channels extending between the photovoltaic component and the electrochemical component to transfer heat and the reactant from the photovoltaic component to the electrochemical component. The integrated photo-electrochemical device and auxiliary devices (such as concentrator, flow controllers) build a system which can flexibly react to changes in operating condition and guarantee best performance.

THE PRESENT DISCLOSURE RELATES TO A POROUS NANOPARTICLE CATALYST FOR METHANE CONVERSION, INCLUDING A FIRST METAL OXIDE AND A SECOND METAL OXIDE, AND A METHOD OF PREPARING THE SAME.

THE PRESENT DISCLOSURE RELATES TO A POROUS NANOPARTICLE CATALYST FOR METHANE CONVERSION, INCLUDING A FIRST METAL OXIDE AND A SECOND METAL OXIDE, AND A METHOD OF PREPARING THE SAME.

Provided is a three-phase system V.sub.2O.sub.3/VN/Mo.sub.2C nanoelectrode material, and a preparation method and application thereof. The nanoelectrode material comprises V.sub.2O.sub.3 particles, VN particles, and Mo.sub.2C particles. The V.sub.2O.sub.3 particles, VN particles, and Mo.sub.2C particles are interlaced in lattice stripes and are uniformly distributed. The mass ratio of the V.sub.2O.sub.3, VN and Mo.sub.2C is (1 to 4):(10 to 40):(4 to 16). The above-mentioned three kinds of nanoparticles are intertwined to form more incoherent interface area. The increase in the area of the incoherent interface area will cause more defects, so that more active sites are provided, and the hydrogen production performance is improved.

Provided is a three-phase system V.sub.2O.sub.3/VN/Mo.sub.2C nanoelectrode material, and a preparation method and application thereof. The nanoelectrode material comprises V.sub.2O.sub.3 particles, VN particles, and Mo.sub.2C particles. The V.sub.2O.sub.3 particles, VN particles, and Mo.sub.2C particles are interlaced in lattice stripes and are uniformly distributed. The mass ratio of the V.sub.2O.sub.3, VN and Mo.sub.2C is (1 to 4):(10 to 40):(4 to 16). The above-mentioned three kinds of nanoparticles are intertwined to form more incoherent interface area. The increase in the area of the incoherent interface area will cause more defects, so that more active sites are provided, and the hydrogen production performance is improved.