Patent classifications
C25C7/02
METHOD FOR EXTRACTING URANIUM WITH COUPLING DEVICE OF WIND POWER GENERATION AND URANIUM EXTRACTION FROM SEAWATER
A method for extracting uranium with a coupling device of wind power generation and uranium extraction from seawater includes the following steps: adding oxygen vacancy (OV)-containing In.sub.2O.sub.3-x to absolute ethanol, and subjecting a resulting mixture to stirring and ultrasonic treatment to obtain a solution of In.sub.2O.sub.3-x in absolute ethanol; coating the solution uniformly on carbon cloth, and drying to obtain carbon cloth coated with OV-containing In.sub.2O.sub.3-x; inserting the coated carbon cloth (as a working electrode) and another blank carbon cloth (as a counter electrode) into a plastic carrier of a coupling device; fixing a small wind power generation apparatus above the plastic carrier, and connecting the working electrode and the counter electrode to a storage battery of the apparatus via wires; and placing the coupling device in seawater, and after the storage battery is charged, energizing the working electrode and the counter electrode to extract uranium from the seawater.
METHOD FOR EXTRACTING URANIUM WITH COUPLING DEVICE OF WIND POWER GENERATION AND URANIUM EXTRACTION FROM SEAWATER
A method for extracting uranium with a coupling device of wind power generation and uranium extraction from seawater includes the following steps: adding oxygen vacancy (OV)-containing In.sub.2O.sub.3-x to absolute ethanol, and subjecting a resulting mixture to stirring and ultrasonic treatment to obtain a solution of In.sub.2O.sub.3-x in absolute ethanol; coating the solution uniformly on carbon cloth, and drying to obtain carbon cloth coated with OV-containing In.sub.2O.sub.3-x; inserting the coated carbon cloth (as a working electrode) and another blank carbon cloth (as a counter electrode) into a plastic carrier of a coupling device; fixing a small wind power generation apparatus above the plastic carrier, and connecting the working electrode and the counter electrode to a storage battery of the apparatus via wires; and placing the coupling device in seawater, and after the storage battery is charged, energizing the working electrode and the counter electrode to extract uranium from the seawater.
LI RECOVERY PROCESSES AND ONSITE CHEMICAL PRODUCTION FOR LI RECOVERY PROCESSES
In this disclosure, a process of recycling acid, base and the salt reagents required in the Li recovery process is introduced. A membrane electrolysis cell which incorporates an oxygen depolarized cathode is implemented to generate the required chemicals onsite. The system can utilize a portion of the salar brine or other lithium-containing brine or solid waste to generate hydrochloric or sulfuric acid, sodium hydroxide and carbonate salts. Simultaneous generation of acid and base allows for taking advantage of both chemicals during the conventional Li recovery from brines and mineral rocks. The desalinated water can also be used for the washing steps on the recovery process or returned into the evaporation ponds. The method also can be used for the direct conversion of lithium salts to the high value LiOH product. The method does not produce any solid effluent which makes it easy-to-adopt for use in existing industrial Li recovery plants.
LI RECOVERY PROCESSES AND ONSITE CHEMICAL PRODUCTION FOR LI RECOVERY PROCESSES
In this disclosure, a process of recycling acid, base and the salt reagents required in the Li recovery process is introduced. A membrane electrolysis cell which incorporates an oxygen depolarized cathode is implemented to generate the required chemicals onsite. The system can utilize a portion of the salar brine or other lithium-containing brine or solid waste to generate hydrochloric or sulfuric acid, sodium hydroxide and carbonate salts. Simultaneous generation of acid and base allows for taking advantage of both chemicals during the conventional Li recovery from brines and mineral rocks. The desalinated water can also be used for the washing steps on the recovery process or returned into the evaporation ponds. The method also can be used for the direct conversion of lithium salts to the high value LiOH product. The method does not produce any solid effluent which makes it easy-to-adopt for use in existing industrial Li recovery plants.
ELECTROLYSIS DEVICE HAVING TWO BORON DOPED DIAMOND LAYERS
The invention relates to a device for electrolysis comprising a substrate (1, 6) on which an anode formed of a first diamond layer (3) and a cathode formed of a second diamond layer (4) are provided, wherein the first (3) and second diamond layers (4) are each made of diamond doped with boron.
ELECTROLYSIS DEVICE HAVING TWO BORON DOPED DIAMOND LAYERS
The invention relates to a device for electrolysis comprising a substrate (1, 6) on which an anode formed of a first diamond layer (3) and a cathode formed of a second diamond layer (4) are provided, wherein the first (3) and second diamond layers (4) are each made of diamond doped with boron.
ELECTRODE ASSEMBLY FOR ELECTROCHEMICAL PROCESSES AND METHOD OF RESTORING THE SAME
The invention relates to an electrode assembly for an electrochemical process comprising a current supply element comprising at least one recessed hole; at least one current distribution bar comprising a first end portion and a second end portion, the first end portion being releasably arranged at the at least one recessed hole; and an electrode substrate arranged at the at least one current distribution bar. The current distribution bar comprises a core and an outer layer, the core being completely covered by the outer layer. The invention also relates to a method of restoring the electrode substrate of the electrode assembly without removing the electrode substrate from the at least one current distribution bar.
ELECTRODE ASSEMBLY FOR ELECTROCHEMICAL PROCESSES AND METHOD OF RESTORING THE SAME
The invention relates to an electrode assembly for an electrochemical process comprising a current supply element comprising at least one recessed hole; at least one current distribution bar comprising a first end portion and a second end portion, the first end portion being releasably arranged at the at least one recessed hole; and an electrode substrate arranged at the at least one current distribution bar. The current distribution bar comprises a core and an outer layer, the core being completely covered by the outer layer. The invention also relates to a method of restoring the electrode substrate of the electrode assembly without removing the electrode substrate from the at least one current distribution bar.
INTEGRATED PROCESS OF PYROLYSIS, ELECTRODE ANODE PRODUCTION AND ALUMINUM PRODUCTION AND JOINT PLANT
An integrated process contains the following steps of: (i) pyrolysis of hydrocarbons to carbon and hydrogen, (iia) removal of at least a part of the produced carbon in step (i) and at least partly further processing of said carbon into a carbon containing electrode, and (iib) removal of the hydrogen produced in step (i) and at least partly using said hydrogen for providing energy, preferably electric energy or heat, for the electrode production in step (iia). A joint plant is also useful, which contains (a) at least one reactor for a pyrolysis process, (b) at least one reactor for the production of electrodes for an aluminum process, (c) a power plant and/or at least one gas-fired burner, and optionally, (d) at least one reactor for the electrolysis for producing aluminum.
ENGINEERING PROCESS FOR HALOGEN SALTS, USING TWO IDENTICAL ELECTRODES
The invention relates to a process and devices for reducing impurities in molten salts, a molten salt being purified in an electrochemical process by applying a voltage between two electrodes. According to the invention, the voltage is varied so that in different phases different electrodes act as cathode or anode.