Various embodiments provide a process roasting a metal bearing material under oxidizing conditions to produce an oxidized metal bearing material, roasting the oxidized metal bearing material under reducing conditions to produce a roasted metal bearing material, and leaching the roasted metal bearing material in a basic medium to yield a pregnant leach solution.

The invention relates to a method and apparatus for recovering metals from metalliferous starting materials comprising steps of i) leaching the metalliferous starting material in chloride-based leaching liquor, ii) withdrawing from the leaching step i) aqueous chloride solution with dissolved metals, iii) recovering metal value from the aqueous chloride solution in a metal recovery process step, iv) neutralizing hydrogen chloride content of the aqueous chloride solution in the metal recovery process step with adding hydrolyzed ammonia to the process solution so as to form ammonium chloride, v) withdrawing ammonium chloride containing process solution to an ammonium regeneration step where calcium-containing reagent is added to generate calcium chloride and ammonia gas and recycling ammonia back to the metal recovery process step iii), vi) regenerating the CaCl.sub.2-solution with H.sub.2SO.sub.4 so as to provide a aqueous HCl solution for recycling to the leaching step i).

Methods of enhancing recovery of value sulfide and/or precious-metal minerals from an ore containing said minerals and a Mg-silicate, slime forming mineral, and/or clay, and which is subjected to a froth flotation process, by adding to one or more stage of the froth flotation process a froth phase modifier having a polymer containing one or more functional groups, and optionally a monovalent ion modifier enhancing agent, thereby enhancing recovery of a value sulfide mineral and/or a precious metal-bearing mineral.

Systems and methods for basic leaching are provided. In various embodiments, a method is provided comprising leaching a slurry comprising a copper bearing material and an ammonia leach medium, adding copper powder to the slurry, separating the slurry into a pregnant leach solution and solids, and performing a solvent extraction on the pregnant leach solution to produce an loaded aqueous stream.

Systems and methods for basic leaching are provided. In various embodiments, a method is provided comprising leaching a slurry comprising a copper bearing material and an ammonia leach medium, adding copper powder to the slurry, separating the slurry into a pregnant leach solution and solids, and performing a solvent extraction on the pregnant leach solution to produce a loaded aqueous stream.

A process for recovering non-ferrous metals from a solid matrix may include: (a) leaching the solid matrix with an aqueous-based solution containing chloride ions, ammonium ions, and Cu.sup.2+ ions, having a pH of 6.5-8.5, in a presence of oxygen, at a temperature of 100 C.-160 C. and a pressure of 150 kPa-800 kPa, so as to obtain an extraction solution comprising leached metals and solid leaching residue; (b) separating the solid leaching residue from the extraction solution; and/or (c) subjecting the extraction solution to at least one cementation so as to recover the leached metals in elemental state. The pH may be greater than or equal to 6.5 and less than or equal to 8.5. Temperature may be greater than or equal to 100 C. and less than or equal to 160 C. Pressure may be greater than or equal to 150 kPa and less than or equal to 800 kPa.

A process for recovering non-ferrous metals from a solid matrix may include: leaching the solid matrix with an aqueous-based solution, in a presence of oxygen, to obtain an extraction solution including leached metals and solid leaching residue; separating the solid leaching residue from the extraction solution; and subjecting the extraction solution to at least one cementation to recover the leached metals in elemental state. The leaching solution may include chloride ions. The leaching solution may further include ammonium ions. A pH of the leaching solution may be greater than or equal to 6.5 and less than or equal to 8.5. A leaching temperature may be greater than or equal to 100 C. and less than or equal to 160 C. A leaching pressure may be greater than or equal to 150 kPa and less than or equal to 800 kPa.

A method of recovering electrode materials includes: a preparing step of preparing an electrode assembly or an electrode sheet, the electrode assembly and the electrode sheet including a current collector and an electrode active material layer formed on the current collector and containing an electrode active material; a dissolving step of immersing the electrode assembly or the electrode sheet in an etchant solution that dissolves the current collector; and a separating step of separating a precipitate containing the electrode active material from the etchant solution in which the current collector is dissolved.

A method for recovering waste lithium battery materials, comprising: (1) performing cell-disassembling on a waste lithium battery to obtain battery powder, ammonia leaching the battery powder to obtain a mixture, and subjecting the mixture to solid-liquid separation to obtain a leached solution and a filter residue; (2) adding a fluorine-phosphorus precipitating agent to the leached solution to obtain a mixture, and subjecting the mixture to solid-liquid separation to obtain a filtrate; (3) subjecting the filtrate to ammonia distillation, subjecting a mixture obtained to solid-liquid separation to obtain a filtrate and a filter residue containing basic copper carbonate and lithium carbonate; (4) washing the filter residue with water, and separating the basic copper carbonate to obtain a washing water; (5) reducing and calcining the filter residue, washing the residue, adding the washing water to the residue to collect lithium by water leaching, and filtering a mixture to obtain a filtrate.

A method of recycling batteries includes steps of: shredding the batteries to generate a shredded battery feed material, wetting the shredded battery feed material with an ammonia carbonate lixiviant to generate a slurry, separating the battery feed material in the slurry into a relatively light fraction material slurry and a relatively heavy fraction material slurry, processing the relatively light fraction material slurry in a first counter current ammoniacal leaching and decanting circuit to produce a first pregnant leaching solution including a soluble lithium (Li) component, and processing the relatively heavy fraction material slurry in a second counter current ammoniacal leaching and decanting circuit to produce a second pregnant leaching solution including, if present in the batteries, soluble nickel (Ni), cobalt (Co), zinc (Zn) and copper (Cu) components and insoluble graphite, iron (Fe), aluminum (Al), manganese (Mn) and rare earth element (REEs) components