Methods and systems for production of lithium hydroxide and lithium carbonate are described. One or more embodiments of the method include producing lithium hydroxide from potassium chloride, lithium chloride, and water. One or more embodiments of the method include producing lithium carbonate from potassium chloride, lithium chloride, water, and a carbon dioxide source. One or more embodiments of the method include producing lithium carbonate from sodium chloride, lithium chloride, water, and a carbon dioxide source.

Disclosed herein are methods for the recovery of lithium from lithium-bearing materials. More specifically, disclosed herein are methods comprising heating the lithium-bearing material with a solid roasting agent, forming a water suspension to allow to leach at least a portion of lithium into the water, separating a liquid and solid phase, and then exposing the collected solid phase to acid to allow acid leaching of the remaining amount of lithium.

Disclosed herein are methods for the recovery of lithium from lithium-bearing materials. More specifically, disclosed herein are methods comprising heating the lithium-bearing material with a solid roasting agent, forming a water suspension to allow to leach at least a portion of lithium into the water, separating a liquid and solid phase, and then exposing the collected solid phase to acid to allow acid leaching of the remaining amount of lithium.

In this disclosure, a process of recycling acid, base and the salt reagents required in the Li recovery process is introduced. A membrane electrolysis cell which incorporates an oxygen depolarized cathode is implemented to generate the required chemicals onsite. The system can utilize a portion of the salar brine or other lithium-containing brine or solid waste to generate hydrochloric or sulfuric acid, sodium hydroxide and carbonate salts. Simultaneous generation of acid and base allows for taking advantage of both chemicals during the conventional Li recovery from brines and mineral rocks. The desalinated water can also be used for the washing steps on the recovery process or returned into the evaporation ponds. The method also can be used for the direct conversion of lithium salts to the high value LiOH product. The method does not produce any solid effluent which makes it easy-to-adopt for use in existing industrial Li recovery plants.

In this disclosure, a process of recycling acid, base and the salt reagents required in the Li recovery process is introduced. A membrane electrolysis cell which incorporates an oxygen depolarized cathode is implemented to generate the required chemicals onsite. The system can utilize a portion of the salar brine or other lithium-containing brine or solid waste to generate hydrochloric or sulfuric acid, sodium hydroxide and carbonate salts. Simultaneous generation of acid and base allows for taking advantage of both chemicals during the conventional Li recovery from brines and mineral rocks. The desalinated water can also be used for the washing steps on the recovery process or returned into the evaporation ponds. The method also can be used for the direct conversion of lithium salts to the high value LiOH product. The method does not produce any solid effluent which makes it easy-to-adopt for use in existing industrial Li recovery plants.

Disclosed herein are materials and processes for production of lithium oxide materials, such as lithium lanthanum zirconium oxide (LLZO), having a small particle size and high density for use in lithium-ion batteries. Some embodiments are directed to forming and then heating a multiphase material comprising lithium carbonate and La.sub.2Zr.sub.2O.sub.7 in the presence of hydrogen gas at a temperature below the melting point of the lithium carbonate, such that at least a portion of the lithium carbonate decomposes to form lithium oxide. In some embodiments, the lithium oxide is heated to a temperature sufficient to crystallize the lithium oxide to form the solid electrolyte material comprising lithium lanthanum zirconium oxide (LLZO) particles.

Disclosed herein are materials and processes for production of lithium oxide materials, such as lithium lanthanum zirconium oxide (LLZO), having a small particle size and high density for use in lithium-ion batteries. Some embodiments are directed to forming and then heating a multiphase material comprising lithium carbonate and La.sub.2Zr.sub.2O.sub.7 in the presence of hydrogen gas at a temperature below the melting point of the lithium carbonate, such that at least a portion of the lithium carbonate decomposes to form lithium oxide. In some embodiments, the lithium oxide is heated to a temperature sufficient to crystallize the lithium oxide to form the solid electrolyte material comprising lithium lanthanum zirconium oxide (LLZO) particles.

This invention relates to a method for the preparation of lithium carbonate from lithium chloride containing brines. The method can include a silica removal step, capturing lithium chloride, recovering lithium chloride, supplying lithium chloride to an electrochemical cell and producing lithium hydroxide, contacting the lithium hydroxide with carbon dioxide to produce lithium carbonate.

This invention relates to a method for the preparation of lithium carbonate from lithium chloride containing brines. The method can include a silica removal step, capturing lithium chloride, recovering lithium chloride, supplying lithium chloride to an electrochemical cell and producing lithium hydroxide, contacting the lithium hydroxide with carbon dioxide to produce lithium carbonate.

In a recovery method for a lithium precursor according to embodiments of the present invention, a cathode active material mixture including a lithium composite oxide is prepared. The cathode active material mixture is reacted with a carbon-based solid material in an atmosphere of an inert gas to form a preliminary precursor mixture containing lithium oxide. A washing treatment of the preliminary precursor mixture is performed to separate a lithium precursor. The lithium precursor can be recovered with high yield and high efficiency.