Abstract: Embodiments in accordance with the present disclosure are directed to methods and apparatuses used for extracting heavy rare gas. An example method includes passing inlet air through an airflow path of an apparatus, removing carbon dioxide and gaseous water from the inlet air, and cooling the inlet air to a threshold temperature while passing along the airflow path. The method further includes passing the cooled inlet air through an adsorption chamber of the apparatus to adsorb heavy rare gas from the cooled inlet air while the cooled inlet air is in a gaseous state, and extracting the heavy rare gas from the adsorption chamber.

Abstract: A system and method that includes flowing brine containing a metal ion through a reactor that includes porous particles having metal ion imprinted polymer having selective binding sites. The system and method further include discharging the brine from the reactor, contacting the porous particles with water, and pressurizing the reactor with carbon dioxide. The carbon dioxide reacts with the adsorbed metal ions to form a metal carbonate solution, where the metal carbonate solution can then be continuously purified with ion exchange. The method can include recycling eluent from the ion exchange back into the system for re-use. The method further includes depressurizing the reactor to precipitate metal carbonate from the metal carbonate solution and discharging the metal carbonate solution from the reactor.

Abstract: Embodiments in accordance with the present disclosure are directed to methods and apparatuses used for extracting heavy rare gas. An example method includes passing inlet air through an airflow path of an apparatus, removing carbon dioxide and gaseous water from the inlet air, and cooling the inlet air to a threshold temperature while passing along the airflow path. The method further includes passing the cooled inlet air through an adsorption chamber of the apparatus to adsorb heavy rare gas from the cooled inlet air while the cooled inlet air is in a gaseous state, and extracting the heavy rare gas from the adsorption chamber.

Abstract: A system and method that includes flowing brine containing a metal ion through a reactor that includes porous particles having metal ion imprinted polymer having selective binding sites. The system and method further include discharging the brine from the reactor, contacting the porous particles with water, and pressurizing the reactor with carbon dioxide. The carbon dioxide reacts with the adsorbed metal ions to form a metal carbonate solution, where the metal carbonate solution can then be continuously purified with ion exchange. The method can include recycling eluent from the ion exchange back into the system for re-use. The method further includes depressurizing the reactor to precipitate metal carbonate from the metal carbonate solution and discharging the metal carbonate solution from the reactor.

Abstract: Example systems are described for producing solar grade silicon from a silicon-generating reaction and recycled silicon particles. In one example, a system for manufacturing high purity solid silicon includes a reactor and a cooling chamber. The reactor includes one or more outlets and a reactor chamber. The one or more outlets are configured to receive a silicon tetrahalide, a reducing agent, and recycled silicon particles. The reactor chamber is configured to react the silicon tetrahalide and the reducing agent to produce fresh silicon, a halide salt, and reaction heat. The reactor chamber heats the recycled silicon particles, the fresh silicon, and the halide salt using at least a portion of the reaction heat to form molten silicon and molten halide salt. The molten silicon includes melted fresh silicon and melted recycled silicon particles. The cooling chamber is configured to cool the molten silicon to form the solid silicon.

Abstract: In one embodiment, the present invention relates generally to a multi-stage system for performing melt coalescence and separation, the multi-stage system. In one embodiment, the multi-stage system includes a first container for mixing a powder with a salt, the first container having an opening, a heating means coupled to the first container for heating the first container and a second container coupled to the first container.

Abstract: Aspects of the invention include methods for producing purified semiconductor or metallic materials. In one embodiment, the methods include admixing a particulate composition of a material, for instance, a metal, with a metal halide to produce a metal-metal halide admixture. The admixture is then heated to a temperature that is above the material's melting point in a container that is chemically and physically stable at that temperature. The molten admixture is allowed to segregate into a lower of the material and an layer of the metal halide and cooled. The metal halide is then separated from the material and a purified semiconductor or metallic material is thereby produced. Also provided are purified material crystals, shaped ingots and/or taper, sheet, or ribbons produced by such methods, as well as the silicon chips and solar panels in which such products are employed.

Abstract: In one embodiment, the present invention relates generally to a multi-stage system for performing melt coalescence and separation, the multi-stage system. In one embodiment, the multi-stage system includes a first container for mixing a powder with a salt, the first container having an opening, a heating means coupled to the first container for heating the first container and a second container coupled to the first container.

Abstract: In one embodiment, the present invention relates generally to a method for reutilizing ionic halides in a production of an elemental material. In one embodiment, the method includes reacting a mixture of an ionic halide, at least one of: an oxide, suboxide or an oxyhalide of an element to be produced and an aqueous acid solution at moderate temperature to form a complex precursor salt and a salt, forming a precursor halide from the complex precursor salt, reducing the precursor halide into the element to be produced and the ionic halide and returning the ionic halide into the mixture of the reacting step.

Abstract: The present invention relates generally to a liquid injector for silicon production. In one embodiment, the injector includes a tube having at least one opening at a first end of said tube, a moveable sealing means disposed inside the tube for sealing the at least one opening and a heating means coupled to the tube for controlling a temperature of a liquid exiting the tube through the at least one opening.

Abstract: Aspects of the invention include methods for producing purified semiconductor or metallic materials. In one embodiment, the methods include admixing a particulate composition of a material, for instance, a metal, with a metal halide to produce a metal-metal halide admixture. The admixture is then heated to a temperature that is above the material's melting point in a container that is chemically and physically stable at that temperature. The molten admixture is allowed to segregate into a lower of the material and an layer of the metal halide and cooled. The metal halide is then separated from the material and a purified semiconductor or metallic material is thereby produced. Also provided are purified material crystals, shaped ingots and/or taper, sheet, or ribbons produced by such methods, as well as the silicon chips and solar panels in which such products are employed.

Abstract: A membrane purification system and method are described in which a first membrane, an osmotically active agent, and a second membrane are utilized to separate fluid components. In general, fluid is moved through the first membrane into an osmosis compartment containing the osmotically active agent by the osmotic force of an osmotically active agent disposed between the first membrane and the second membrane. The fluid is forced from the osmotically active agent and through the second membrane while the second membrane retains the osmotically active agent in the osmosis compartment. The osmotically active agent may include a polymer.