The invention is related to an electrode assembly for an electrochemical process comprising a current supply device, an elongated current distribution bar comprising first and second ends, and a sheet-shaped electrode substrate attached to the current distribution bar and having a longitudinal extension and a lateral extension. The current distribution bar comprises a first portion attached to the current supply device, a second portion extending along the electrode substrate, and a third portion extending between the first and second portions. The current distribution bar is bent between its first and second ends, and the current supply device is laterally and longitudinally positioned beyond the electrode substrate. The second portion at least partly extends longitudinally along the electrode substrate.

The invention is related to an electrode assembly for an electrochemical process comprising a current supply device, an elongated current distribution bar comprising first and second ends, and a sheet-shaped electrode substrate attached to the current distribution bar and having a longitudinal extension and a lateral extension. The current distribution bar comprises a first portion attached to the current supply device, a second portion extending along the electrode substrate, and a third portion extending between the first and second portions. The current distribution bar is bent between its first and second ends, and the current supply device is laterally and longitudinally positioned beyond the electrode substrate. The second portion at least partly extends longitudinally along the electrode substrate.

A method for recovering metal resources in coal ash by molten salt electrolysis includes: calcinating the coal ash for decarburization to obtain the decarburized coal ash; subjecting the decarburized coal ash to ball milling to obtain coal ash powders; pressing the coal ash powders to form a plate; placing the plate as a cathode into an electrolyte in a reactor, and performing electrolytic reaction under an oxygen-free condition at an electrolytic reaction temperature of 550° C. to 900° C. in the reactor to obtain a reaction product; and removing the reaction product from the reactor, cooling the reaction product to room temperature in an inert atmosphere, and cleaning the cooled reaction product to obtain a silicon-aluminum based alloy.

Methods for electrochemical extraction of metals, and methods for determining electrolyte fluids suitable therefor. A method of extracting, separating, and/or purifying a method includes immersing an electrochemical cell including an anode and a cathode in a liquid including the metal to form a layer including the metal on the cathode. The immersing includes applying an electrochemical potential across the anode and cathode.

Methods for electrochemical extraction of metals, and methods for determining electrolyte fluids suitable therefor. A method of extracting, separating, and/or purifying a method includes immersing an electrochemical cell including an anode and a cathode in a liquid including the metal to form a layer including the metal on the cathode. The immersing includes applying an electrochemical potential across the anode and cathode.

A cathode assembly for an electrolytic cell including a cathode block having a second surface and a first surface. The cathode block also including at least one sealing groove opening onto its first surface and a plurality of electrical contact plugs mounted in electrical contact with the first surface of the cathode block. The cathode assembly includes at least one current supply plate in electrical contact with at least one electrical contact plug, and is connected to at least one unit for connection to an electric current source. The cathode assembly includes at least one current supply bar having a coefficient of thermal expansion substantially identical to the coefficient of thermal expansion of the current supply plate and is sealed within the at least one sealing groove while being fastened to at least one current supply plate.

A method for producing metal titanium by carrying out electrolysis using an anode and a cathode in a molten salt bath, the method using an anode containing metal titanium as the anode, the method comprising a titanium deposition step of depositing metal titanium on the cathode, wherein, in the titanium deposition step, a temperature of the molten salt bath is from 250° C. or more and 600° C. or less, and an average current density of the cathode in a period from the start to 30 minutes later of the titanium deposition step is maintained in a range of 0.01 A/cm.sup.2 to 0.09 A/cm.sup.2.

A desalination and lithium collection system has a primary brine chamber receiving brine from a brine inlet. A charged metal has anodes and cathodes, submerged in the brine in the primary brine chamber. Electrical power applied is to the charged metal as alternating current having a frequency of less than 2kHz for conducting a primary electrolysis. A water vapor collection chamber fluidly connected to the primary brine chamber and configured to collect water vapor generated from the charged metal. A condenser chamber is fluidly connected to the water vapor collection chamber and configured to condense water vapor. A freshwater chamber is fluidly connected to the condenser and configured to collect freshwater.

A desalination and lithium collection system has a primary brine chamber receiving brine from a brine inlet. A charged metal has anodes and cathodes, submerged in the brine in the primary brine chamber. Electrical power applied is to the charged metal as alternating current having a frequency of less than 2kHz for conducting a primary electrolysis. A water vapor collection chamber fluidly connected to the primary brine chamber and configured to collect water vapor generated from the charged metal. A condenser chamber is fluidly connected to the water vapor collection chamber and configured to condense water vapor. A freshwater chamber is fluidly connected to the condenser and configured to collect freshwater.

A membrane-stacked electrolytic bath for lithium extraction from salt lakes by electrochemical intercalation/deintercalation includes a positioning supporting plate as well as a first compressing plate, a first rubber gasket, at least one electrochemical intercalation/deintercalation unit, a second rubber gasket, and a second compressing plate which are sequentially arranged in an overlapped manner; a compressing apparatus for abutting against the second compressing plate is arranged on one side of the second compressing plate to enable peripheral edges of the first compressing plate, the first rubber gasket, the electrochemical intercalation/deintercalation unit, the second rubber gasket, and the second compressing plate to be sealed; the first compressing plate is provided with water outlet pipes communicated with the electrochemical intercalation/deintercalation unit; and the second compressing plate is provided with water inlet pipes communicated with the electrochemical intercalation/deintercalation unit.