Patent classifications
C25C7/08
EWS module device for electro-winning and/or electro-refining, interconnection process, and operating process thereof
The invention relates to an EWS module device for electro-winning and/or electro-refining, based on a saturated leaching solution of PLS/electrolyte/raffmate/ILS without solvent extraction, characterised by comprising: a tank (10 and 12); a set of electrolytic cells contained within the tank, wherein the cells are electrically and volumetrically separated by the internal walls of the module (14), with the cells being connected in series by a joining board or capping board (3); an intercellular bar (1); an intercellular bar guide (2); inlet and outlet ducts for the PLS/electrolyte/raffinate/ILS (17) and (11) for each cell independently; and each EWS module is in turn connected to the other modules by an inter-module connector (18), and same in turn control the connection and disconnection of the EWS modules by an interrupter (25); operating process of the EWS module device; and connection and disconnection process between different EWS module devices.
Electrorefining of magnesium from scrap metal aluminum or magnesium alloys
The invention comprises methods and apparatuses for the electrorefining of Mg from Al or Mg alloy scrap. The invention utilizes the density and charge features of Mg present in a melted alloy to continuously extract Mg and Mg alloys from a melted Al alloy feed.
Electrorefining of magnesium from scrap metal aluminum or magnesium alloys
The invention comprises methods and apparatuses for the electrorefining of Mg from Al or Mg alloy scrap. The invention utilizes the density and charge features of Mg present in a melted alloy to continuously extract Mg and Mg alloys from a melted Al alloy feed.
Dynamic metal-anode flow battery energy-storage system
A dynamic metal-anode flow battery energy-storage system includes a discharge module, a charging module, and a delivery device. The discharge module includes a plurality of discharge reactants to be oxidized to discharge electric energy. The charging module is electrically connected to the discharge module and includes at least one electrolysis device and at least one removal device. The electrolysis device includes a conductive member which is to be energized with electricity, such that a plurality of electrolysis products having the same material with the discharge reactants are adhered to a surface thereof. The removal device includes a scraper adapted to remove the adhered electrolysis products from the surface of the conductive member. The delivery device is adapted to deliver the electrolysis products into the first electrolyte as the discharge reactants, and deliver the discharged products into the second electrolyte as the electrolysis reactants.
CONVERSION OF SPENT URANIUM OXIDE FUEL INTO MOLTEN SALT REACTOR FUEL
There is described a method of reprocessing spent nuclear fuel. The spent nuclear fuel is added to an electro-reduction cell containing a halide salt electrolyte at a temperature above the melting point of the metallic form of uranium and higher actinides present in the spent nuclear fuel. The cell is operated so as to electrochemically reduce the spent nuclear fuel to form an alloy of uranium and higher actinides present in the spent nuclear fuel, wherein electrochemical reduction is continued until a concentration of unreduced components of the spent nuclear fuel is sufficiently low for the alloy to agglomerate.
CONVERSION OF SPENT URANIUM OXIDE FUEL INTO MOLTEN SALT REACTOR FUEL
There is described a method of reprocessing spent nuclear fuel. The spent nuclear fuel is added to an electro-reduction cell containing a halide salt electrolyte at a temperature above the melting point of the metallic form of uranium and higher actinides present in the spent nuclear fuel. The cell is operated so as to electrochemically reduce the spent nuclear fuel to form an alloy of uranium and higher actinides present in the spent nuclear fuel, wherein electrochemical reduction is continued until a concentration of unreduced components of the spent nuclear fuel is sufficiently low for the alloy to agglomerate.
Method and apparatus for recovering metals and sulfur from feed streams containing metal sulfides and polysulfides
A system to remove sodium and Sulfur from a feed stream containing alkali metal sulfides and polysulfides in addition to heavy metals. The system includes an electrolytic cell having an anolyte compartment housing an anode in contact with an anolyte. The anolyte includes alkali metal sulfides and polysulfides dissolved in a polar organic solvent. The anolyte includes heavy metal ions. A separator includes an ion conducting membrane and separates the anolyte compartment from a catholyte compartment that includes a cathode in contact with a catholyte. The catholyte includes an alkali ion-conductive liquid. A power source applies a voltage to the electrolytic cell high enough to reduce the alkali metal and oxidize Sulfur ions to allow recovery of the alkali metal and elemental sulfur. The ratio of sodium to Sulfur is such that the open circuit potential of the electrolytic cell is greater than about 2.3V.
Method and apparatus for recovering metals and sulfur from feed streams containing metal sulfides and polysulfides
A system to remove sodium and Sulfur from a feed stream containing alkali metal sulfides and polysulfides in addition to heavy metals. The system includes an electrolytic cell having an anolyte compartment housing an anode in contact with an anolyte. The anolyte includes alkali metal sulfides and polysulfides dissolved in a polar organic solvent. The anolyte includes heavy metal ions. A separator includes an ion conducting membrane and separates the anolyte compartment from a catholyte compartment that includes a cathode in contact with a catholyte. The catholyte includes an alkali ion-conductive liquid. A power source applies a voltage to the electrolytic cell high enough to reduce the alkali metal and oxidize Sulfur ions to allow recovery of the alkali metal and elemental sulfur. The ratio of sodium to Sulfur is such that the open circuit potential of the electrolytic cell is greater than about 2.3V.
SYSTEM AND DEVICE FOR OPTIMISING METAL ELECTRODEPOSITION
Optimizing device for the electrodeposition of metals which covers the entire range of electrodeposition of metals from the lowest current densities to the highest, which has multiple openings on its entire surface which maximize the free passage of the electrolyte flow without altering the electrodeposition processes and straightening the electrodes causing an equidistribution of current in the electrodes installed in the cells which leads to the production of cathodes with high quality uniform deposits avoiding the loss of current due to short circuits that occur between anodes and cathodes, thereby increasing the current efficiency of the system. The device comprises a single body with a firm skeletal structure formed by different body sections, at least one body section comprising inclined side walls.
DEVICE FOR EXTRACTING A METAL ELECTROLYTICALLY DEPOSITED ON A CATHODE
A device for producing a pure metal or an alloy of the pure metal via electrolytic reduction of an ore of the pure metal or of a substance containing an oxidized form of the pure metal includes: a cell equipped with an anode, a cathode, an electrolytic area comprising an electrolyte, and a removable cell closing system, the cathode having a coating non-adherent for an electrolytically deposited metal; and an electrically conductive metal sheet for extraction of a plate of the electrolytically deposited metal on the cathode, the metal sheet being arranged in the cell in a continuation of the cathode or partially overlapping the cathode, with mechanical and electrical contact at one end with the cathode and extending at least partly beyond the electrolytic area of the cell so as to allow simultaneous depositing of the pure metal on the cathode and on a portion of the metal sheet.