An electrode comprising: NaVOPO.sub.4 having orthorhombic crystalline symmetry and space group Pna2.sub.1, as an active intercalation host material, wherein the electrode is capable of electrochemical insertion and release of greater than one sodium ion per vanadium, wherein the NaVOPO.sub.4 is formed by a solid phase synthesis process from a heated powdered mixture of ammonium metavanadate, ammonium phosphate monobasic, and potassium carbonate, to yield KVOPO.sub.4 having corner-sharing VO.sub.6 octahedra and PO.sub.4 tetrahedra, defining two types of tunnels comprising a first type of tunnel formed of rings of two PO.sub.4 tetrahedra and a second type of tunnel formed of rings of three PO.sub.4 tetrahedra and three VO.sub.6 octahedra, followed by substitution of the potassium ions with sodium ions.

A redox flow battery system includes an anolyte having a first ionic species in solution; a catholyte having a second ionic species in solution, where the redox flow battery system is configured to reduce the first ionic species in the anolyte and oxidize the second ionic species in the catholyte during charging; a first electrode in contact with the anolyte, where the first electrode includes channels for collection of particles of reduced metallic impurities in the anolyte; a second electrode in contact with the catholyte; and a separator separating the anolyte from the catholyte. A method of reducing metallic impurities in an anolyte of a redox flow battery system includes reducing the metallic impurities in the anolyte; collecting particles of the reduced metallic impurities; and removing the collected particles using a cleaning solution.

A redox flow battery system includes an anolyte having a first ionic species in solution; a catholyte having a second ionic species in solution, where the redox flow battery system is configured to reduce the first ionic species in the anolyte and oxidize the second ionic species in the catholyte during charging; a first electrode in contact with the anolyte, where the first electrode includes channels for collection of particles of reduced metallic impurities in the anolyte; a second electrode in contact with the catholyte; and a separator separating the anolyte from the catholyte. A method of reducing metallic impurities in an anolyte of a redox flow battery system includes reducing the metallic impurities in the anolyte; collecting particles of the reduced metallic impurities; and removing the collected particles using a cleaning solution.

Provided is the positive electrode active material for a potassium ion battery according to the embodiment comprises a compound represented by Formula (1), in which M represents at least one element selected from the group consisting of V, Fe, Co, Ni, and Mn, and x represents a number from 0 to 1; and is a positive electrode for a potassium ion battery comprising the positive electrode active material for a potassium ion battery according to the embodiment, or a potassium ion battery comprising the positive electrode for a potassium ion battery.
KMO.sub.xPO.sub.4F.sub.1-x  [Formula (1)].

The present disclosure broadly relates to a process for recovering vanadium, iron, titanium and silica values from vanadiferous feedstocks. More specifically, but not exclusively, the present disclosure relates to a metallurgical process in which vanadium, iron, titanium and silica values are recovered from vanadiferous feedstocks such as vanadiferous titanomagnetite, iron ores, vanadium slags and industrial wastes and by-products containing vanadium. The process broadly comprises digesting the vanadiferous feedstocks into sulfuric acid thereby producing a sulfation cake; dissolving the sulfation cake and separating insoluble solids thereby producing a pregnant solution; reducing the pregnant solution thereby producing a reduced pregnant solution; and crystallizing ferrous sulfate hydrates from the reduced pregnant solution, producing an iron depleted reduced solution. The process further comprises removing titanium compounds from the iron depleted reduced solution thereby producing a vanadium-rich pregnant solution; concentrating vanadium and recovering vanadium products and/or a vanadium electrolyte.

The present disclosure broadly relates to a process for recovering vanadium, iron, titanium and silica values from vanadiferous feedstocks. More specifically, but not exclusively, the present disclosure relates to a metallurgical process in which vanadium, iron, titanium and silica values are recovered from vanadiferous feedstocks such as vanadiferous titanomagnetite, iron ores, vanadium slags and industrial wastes and by-products containing vanadium. The process broadly comprises digesting the vanadiferous feedstocks into sulfuric acid thereby producing a sulfation cake; dissolving the sulfation cake and separating insoluble solids thereby producing a pregnant solution; reducing the pregnant solution thereby producing a reduced pregnant solution; and crystallizing ferrous sulfate hydrates from the reduced pregnant solution, producing an iron depleted reduced solution. The process further comprises removing titanium compounds from the iron depleted reduced solution thereby producing a vanadium-rich pregnant solution; concentrating vanadium and recovering vanadium products and/or a vanadium electrolyte.

A device including an LED light source optically coupled to a phosphor selected from [Y,Gd,Tb,La,Sm,Pr,Lu].sub.3[Al,Ga].sub.5−aO.sub.12−3/2a:Ce.sup.3+ (wherein 0<a<0.5), beta-SiAlON:Eu.sup.2+, [Sr,Ca,Ba][Al,Ga,In].sub.2S.sub.4:Eu.sup.2+, alpha-SiAlON doped with Eu.sup.2+ and/or Ce.sup.3+, Ca.sub.1−h−rCe.sub.hEu.sub.rAl.sub.1−h[Mg,Zn].sub.hSiN.sub.3, (where 0<h<0.2, 0<r<0.2), Sr(LiAl.sub.3N.sub.4):Eu.sup.2+, [Ca,Sr]S:Eu.sup.2+ or Ce.sup.3+, [Ba,Sr,Ca].sub.bSi.sub.gN.sub.m:Eu.sup.2+ (wherein 2b+4g=3m), quantum dot materials, and combinations thereof; and a green-emitting U.sup.6+-doped phosphor having a composition selected from the group consisting of U.sup.6+-doped phosphate-vanadate phosphors, U.sup.6+-doped halide phosphors, U.sup.6+-doped oxyhalide phosphors, U.sup.6+-doped silicate-germanate phosphors, U.sup.6+-doped alkali earth oxide phosphors, and combinations thereof, is presented.

A device including an LED light source optically coupled to a phosphor selected from [Y,Gd,Tb,La,Sm,Pr,Lu].sub.3[Al,Ga].sub.5−aO.sub.12−3/2a:Ce.sup.3+ (wherein 0<a<0.5), beta-SiAlON:Eu.sup.2+, [Sr,Ca,Ba][Al,Ga,In].sub.2S.sub.4:Eu.sup.2+, alpha-SiAlON doped with Eu.sup.2+ and/or Ce.sup.3+, Ca.sub.1−h−rCe.sub.hEu.sub.rAl.sub.1−h[Mg,Zn].sub.hSiN.sub.3, (where 0<h<0.2, 0<r<0.2), Sr(LiAl.sub.3N.sub.4):Eu.sup.2+, [Ca,Sr]S:Eu.sup.2+ or Ce.sup.3+, [Ba,Sr,Ca].sub.bSi.sub.gN.sub.m:Eu.sup.2+ (wherein 2b+4g=3m), quantum dot materials, and combinations thereof; and a green-emitting U.sup.6+-doped phosphor having a composition selected from the group consisting of U.sup.6+-doped phosphate-vanadate phosphors, U.sup.6+-doped halide phosphors, U.sup.6+-doped oxyhalide phosphors, U.sup.6+-doped silicate-germanate phosphors, U.sup.6+-doped alkali earth oxide phosphors, and combinations thereof, is presented.

The invention provides for the orchestrated treatment of disparate fractions of a shale deposit to recover vanadium values, with distinct steps of beneficiation that together provide a combined vanadium-enriched concentrate amenable to subsequent combined steps of hydrometallurgical vanadium extraction.

Materials, designs, methods of manufacture, and devices are provided for an anode material for a rechargeable lithium-ion battery. For example, an anode material may include Li.sub.3±xV.sub.2±yO.sub.5±z. 0≤x≤7, 0≤y≤1, and z may be based on the charge resulting from Li.sub.3±x and V.sub.2±y. Also, a cell can include a lithiated anode material. The lithiated anode material may include Li3±xV2±yO5±z. The lithiated anode material may be casted on a first substrate to form a lithiated anode, having a separator stacked on the lithiated anode. The separator may include electrolytes. A cathode can be stacked on the separator. The cathode being formed by casting a cathode material on a second substrate.