A method for dissolving a lithium compound according to the present invention includes bringing a lithium compound into contact with water or an acidic solution, and feeding, separately from the lithium compound, a carbonate ion to the water or the acidic solution to produce carbonic acid, and allowing the carbonic acid to react with the lithium compound to produce lithium hydrogen carbonate.

Disclosed is a method for preparing vanadium or vanadium alloy powder from a vanadium-containing raw material through a shortened process, including: calcinating a mixture of a vanadium-containing raw material and an alkali compound for oxidation to form a water-soluble vanadate; purifying the vanadate followed by vanadium precipitation to produce an intermediate CaV.sub.2O.sub.6 with high purity; dissolving CaV.sub.2O.sub.6 in a molten-salt medium together with other raw materials to form a uniform reaction system; and introducing a reducing agent to the system followed by separation, washing and drying to produce vanadium or vanadium alloy powder having a particle size of 50-800 nm and a purity of 99.0 wt % or more. The method can continuously process vanadium-containing raw materials to prepare vanadium or vanadium alloy powder.

A method for preparing iron alloy and a cement material, in the field of solid waste recycling, provides an efficient, synergistic effect between main components of carbon, calcium and heavy metal in municipal solid waste incineration (MSWI) fly ash and main components of iron, aluminum and silicon in red mud, so that the iron alloy and cement material can be readily obtained. By using waste to treat waste and using the complementarity of the components of two waste streams, carbon in the MSWI fly ash may provide a reductant to accelerate an iron mineral in the red mud to reduce into metal iron. With the formation of the metal iron, a siderophile heavy metal element in the MSWI fly ash is also accelerated to enter an iron phase. Meanwhile, the cement material is formed by Al.sub.2O.sub.3 and SiO.sub.2 in the red mud and CaO in the MSWI fly ash.

A method for preparing iron alloy and a cement material, in the field of solid waste recycling, provides an efficient, synergistic effect between main components of carbon, calcium and heavy metal in municipal solid waste incineration (MSWI) fly ash and main components of iron, aluminum and silicon in red mud, so that the iron alloy and cement material can be readily obtained. By using waste to treat waste and using the complementarity of the components of two waste streams, carbon in the MSWI fly ash may provide a reductant to accelerate an iron mineral in the red mud to reduce into metal iron. With the formation of the metal iron, a siderophile heavy metal element in the MSWI fly ash is also accelerated to enter an iron phase. Meanwhile, the cement material is formed by Al.sub.2O.sub.3 and SiO.sub.2 in the red mud and CaO in the MSWI fly ash.

A method (500) for producing a titanium product is disclosed. The method (500) can include obtaining TiO.sub.2-slag (501) and reducing impurities in the TiO.sub.2-slag (502) to form purified TiO.sub.2 (503). The method (500) can also include reducing the purified TiO.sub.2 using a metallic reducing agent (504) to form a hydrogenated titanium product comprising TiH.sub.2 (505). The hydrogenated titanium product can be dehydrogenated (506) to form a titanium product (508). The titanium product can also be optionally deoxygenated (507) to reduce oxygen content.

A method (500) for producing a titanium product is disclosed. The method (500) can include obtaining TiO.sub.2-slag (501) and reducing impurities in the TiO.sub.2-slag (502) to form purified TiO.sub.2 (503). The method (500) can also include reducing the purified TiO.sub.2 using a metallic reducing agent (504) to form a hydrogenated titanium product comprising TiH.sub.2 (505). The hydrogenated titanium product can be dehydrogenated (506) to form a titanium product (508). The titanium product can also be optionally deoxygenated (507) to reduce oxygen content.

A device for thermal treatment of bulk material, includes a travelling grate chain revolving in the direction of movement including an endless travelling grate with movable links. The travelling grate chain features a plurality of pallet cars, and grate rods arranged on crossbars. Further, wind boxes are arranged such that gas flows through the pallet cars and their grate rods from or into the wind boxes. At each pallet car at least one sealing blade is mounted in parallel to the moving direction and flush with the pallet car, whereby a sealing box is in parallel to the moving direction. A liquid medium is filled into at least one sealing box, such that the sealing blade is immersed in the liquid.

A device for thermal treatment of bulk material, includes a travelling grate chain revolving in the direction of movement including an endless travelling grate with movable links. The travelling grate chain features a plurality of pallet cars, and grate rods arranged on crossbars. Further, wind boxes are arranged such that gas flows through the pallet cars and their grate rods from or into the wind boxes. At each pallet car at least one sealing blade is mounted in parallel to the moving direction and flush with the pallet car, whereby a sealing box is in parallel to the moving direction. A liquid medium is filled into at least one sealing box, such that the sealing blade is immersed in the liquid.

This method recycles lithium iron phosphate batteries to extract cathode active materials, anode active materials, current collector metals, electrolyte, and separator materials in a highly pure state. The process involves the discharging and subsequent disassembly of used batteries into individual componentsanode and cathode electrodes, electrolyte, separator, tape, and tabs, achieved via a brine bath, a dimethyl carbonate bath, and physical dismounting. Anode and cathode materials are then separated from their respective current collectors using specific solvent-cosolvent combinations, followed by purification procedures involving washing, heat treatment, and additional purification steps for the cathode. The process results in the extraction of highly pure battery materials including active anode and cathode materials, current collector metals, electrolyte, and separators. This approach obtains and purifies battery materials rather than base elemental compounds, thereby using few chemicals and having high reclamation efficiency, leading to enhanced recovery rates and high purity of resulting materials.

This method recycles lithium iron phosphate batteries to extract cathode active materials, anode active materials, current collector metals, electrolyte, and separator materials in a highly pure state. The process involves the discharging and subsequent disassembly of used batteries into individual componentsanode and cathode electrodes, electrolyte, separator, tape, and tabs, achieved via a brine bath, a dimethyl carbonate bath, and physical dismounting. Anode and cathode materials are then separated from their respective current collectors using specific solvent-cosolvent combinations, followed by purification procedures involving washing, heat treatment, and additional purification steps for the cathode. The process results in the extraction of highly pure battery materials including active anode and cathode materials, current collector metals, electrolyte, and separators. This approach obtains and purifies battery materials rather than base elemental compounds, thereby using few chemicals and having high reclamation efficiency, leading to enhanced recovery rates and high purity of resulting materials.