There are provided processes comprising submitting an aqueous composition comprising lithium sulphate and/or bisulfate to an electrolysis or an electrodialysis for converting at least a portion of said sulphate into lithium hydroxide. During electrolysis or electrodialysis, the aqueous composition is at least substantially maintained at a pH having a value of about 1 to about 4; and converting said lithium hydroxide into lithium carbonate. Alternatively, lithium sulfate and/or lithium bisulfate can be submitted to a first electromembrane process that comprises a two-compartment membrane process for conversion of lithium sulfate and/or lithium bisulfate to lithium hydroxide, and obtaining a first lithium-reduced aqueous stream and a first lithium hydroxide-enriched aqueous stream; and submitting said first lithium-reduced aqueous stream to a second electromembrane process comprising a three-compartment membrane process to prepare at least a further portion of lithium hydroxide and obtaining a second lithium-reduced aqueous stream and a second lithium-hydroxide enriched aqueous stream.

Methods and systems for the production and delivery of lithium metal of high purity are provided herein. In one or more embodiments, method for flowing liquid lithium to a processing chamber is provided and includes flowing liquid lithium from a lithium refill container to a liquid lithium delivery module, where the liquid lithium delivery module is fluidly coupled to the lithium refill container, and flowing the liquid lithium from the liquid lithium delivery module to the processing chamber. The liquid lithium delivery module contains a lithium storage region operable to store liquid lithium and containing a fluid supply line fluidly coupling an outlet port of a liquid lithium storage tank, and a flow meter positioned downstream from the lithium storage region along the fluid supply line and operable to monitor the flow of the liquid lithium through the fluid supply line.

The present disclosure provides a lithium extraction apparatus, which includes a frame and a transmission mesh belt. The transmission mesh belt includes water permeable holes, and is configured to carry an adsorbent. The frame includes an adsorption zone and a desorption zone along a traveling direction of the transmission mesh belt. A brine spraying device is disposed above the transmission mesh belt in adsorption zone. A desorbing liquid spraying device is disposed above the transmission mesh belt in the desorption zone, and a lithium extract collecting device is disposed below the transmission mesh belt in the desorption zone. The transmission mesh belt in the adsorption zone is folded into a multi-layer structure in the vertical direction; and/or the transmission mesh belt in the desorption zone is folded into a multi-layer structure in the vertical direction.

The present disclosure provides a lithium extraction apparatus, which includes a frame and a transmission mesh belt. The transmission mesh belt includes water permeable holes, and is configured to carry an adsorbent. The frame includes an adsorption zone and a desorption zone along a traveling direction of the transmission mesh belt. A brine spraying device is disposed above the transmission mesh belt in adsorption zone. A desorbing liquid spraying device is disposed above the transmission mesh belt in the desorption zone, and a lithium extract collecting device is disposed below the transmission mesh belt in the desorption zone. The transmission mesh belt in the adsorption zone is folded into a multi-layer structure in the vertical direction; and/or the transmission mesh belt in the desorption zone is folded into a multi-layer structure in the vertical direction.

The present disclosure concerns the production of precursor compounds for lithium battery cathodes. Batteries or their scrap are smelted in reducing conditions, thereby forming an alloy suitable for further hydrometallurgical refining, and a slag. The alloy is leached in acidic conditions, producing a Ni- and Co-bearing solution, which is refined. The refining steps are greatly simplified as most elements susceptible to interfere with the refining steps concentrate in the slag. Metals such as Co, Ni and Mn are then precipitated from the solution, forming a suitable starting product for the synthesis of new battery precursor compounds.

The present disclosure concerns the production of precursor compounds for lithium battery cathodes. Batteries or their scrap are smelted in reducing conditions, thereby forming an alloy suitable for further hydrometallurgical refining, and a slag. The alloy is leached in acidic conditions, producing a Ni- and Co-bearing solution, which is refined. The refining steps are greatly simplified as most elements susceptible to interfere with the refining steps concentrate in the slag. Metals such as Co, Ni and Mn are then precipitated from the solution, forming a suitable starting product for the synthesis of new battery precursor compounds.

A method for recycling a battery including the following steps: a) dissolution of a battery waste, for example an electrode, including lithium and a metal selected from cobalt and manganese, such that a solution to be treated containing lithium ions and metal ions is formed, b) addition of a peroxymonosulfate salt to the solution to be treated, the solution to be treated being regulated at a pH ranging from 1 to 4 when the metal is cobalt or at a pH ranging from 0.1 to 2.5 when the metal is manganese, such that the metal ions are selectively precipitated in the form of metal oxyhydroxide, c) separation of the lithium ions from the solution to be treated. Advantageously, the solution further comprises nickel ions.

A method for recycling a battery including the following steps: a) dissolution of a battery waste, for example an electrode, including lithium and a metal selected from cobalt and manganese, such that a solution to be treated containing lithium ions and metal ions is formed, b) addition of a peroxymonosulfate salt to the solution to be treated, the solution to be treated being regulated at a pH ranging from 1 to 4 when the metal is cobalt or at a pH ranging from 0.1 to 2.5 when the metal is manganese, such that the metal ions are selectively precipitated in the form of metal oxyhydroxide, c) separation of the lithium ions from the solution to be treated. Advantageously, the solution further comprises nickel ions.

A method that includes contacting a Li-containing aqueous liquid with a Li ion-selective membrane while simultaneously applying an electric field thereby extracting Li ions from the Li-containing aqueous liquid; and intercalating the extracted Li ions into a cathode material.

A method that includes contacting a Li-containing aqueous liquid with a Li ion-selective membrane while simultaneously applying an electric field thereby extracting Li ions from the Li-containing aqueous liquid; and intercalating the extracted Li ions into a cathode material.