The extraction of lithium from salt lake brine in the Chinese Qaidam Basin is challenging due to its high Mg/Li and Na/Li ratios.Herein,we utilized a reaction-coupled separation technology to separate sodium and lithium ions from a high Na/Li ratio brine (Na/Li =48.7,w/w) and extracted lithium with LiAl-layered double hydroxides (LiAl-LDHs).The LiAl-LDHs act as lithium-ion-selective capturing materials from multication brines.That is,the lithium ions selectively enter the solid phase to form LiAl-LDHs,and the sodium ions are still retained in the liquid phase.This is because the lithium ions can be incorporated into the structural vacancies of LiAl-LDHs,whereas the sodium ions cannot.The effects of reaction conditions on lithium loss and separation efficiency were investigated at both the nucleation and the crystallization stage,e.g.,the nucleation rotating speed,the Li/Al molar ratio,the crystallization temperature and time,and co-existing cations.The lithium loss is as low as 3.93% under optimal separation conditions.The sodium ions remained in the solution.Consequently,an excellent Na/Li separation efficiency was achieved by this reaction-coupled separation technology.These findings confirm that LiAl-LDHs play a critical function in selectively capturing lithium ions from brines with a high Na/Li ratio,which is useful for the extraction of lithium ions from the abundant salt lake brine resources in China.