Lithium extraction from salt lake
brines is one of the most important
pathways for obtaining Li-related products, e.g., Li2CO3 and LiOH, and for further fabricating electric energy-storage
products, e.g., lithium ion batteries. The high Mg/Li ratio and high
Mg content are remarkable characteristics of the salt lakes in the
Qaidam Basin in China, making the Mg/Li separation and Li extraction
rather difficult. Herein, we proposed a reaction-coupled separation
technology for Mg/Li separation from brine with a high Mg/Li ratio.
The core idea of this technology is that the Mg2+ cations
were reacted to form a solid via a nucleation–crystallization
separation method. The solid product was MgAl-layered double hydroxide
(MgAl-LDH), a widely used and high-valued product in the family of
LDHs. The Li+ cations were left in the solution after Mg2+ cations were reacted with alkali solution, accompanied by
foreign Al3+ cations. That is to say that the Mg2+ cations can be incorporated into the layers of MgAl-LDH while Li+ cations cannot. The findings indicated that Mg2+ cations were almost completely extracted into the solid phase to
form the LDH. The Li+ cations remained in the solution
having a weight loss less than 8%, which is an excellent level of
Li extraction from the brine with a high Mg/Li ratio. The effects
of reaction parameters, e.g., ionic strength, nucleation rotating
speed, Mg/Al ratio, and crystallization temperature and time, on the
separation performance and lithium loss were investigated. The optimal
conditions were derived for lower lithium loss and more outstanding
Mg/Li separation performance, which can be a useful guide for environmentally
friendly and sustainable Li extraction from the brine.