Lithium aluminum
layered double hydroxide chlorides (LADH-Cl) have
been widely used for lithium extraction from brine. Elevation of the
performances of LADH-Cl sorbents urgently requires knowledge of the
composition–structure–property relationship of LADH-Cl
in lithium extraction applications, but these are still unclear. Herein,
combining the phase equilibrium experiments, advanced solid characterization
methods, and theoretical calculations, we constructed a cyclic work
diagram of LADH-Cl for lithium capture from aqueous solution, where
the reversible (de)hydration and (de)intercalation induced phase evolution
of LADH-Cl dominates the apparent lithium “adsorption–desorption”
behavior. It is found that the real active ingredient in LADH-Cl type
lithium sorbents is a dihydrated LADH-Cl with an Al:Li molar ratio
varying from 2 to 3. This reversible process indicates an ultimate
reversible lithium (de)intercalation capacity of ∼10 mg of
Li per g of LADH-Cl. Excessive lithium deintercalation results in
the phase structure collapse of dihydrated LADH-Cl to form gibbsite.
When interacting with a concentrated LiCl aqueous solution, gibbsite
is easily converted into lithium saturated intercalated LADH-Cl phases.
By further hydration with a diluted LiCl aqueous solution, this phase
again converts to the active dihydrated LADH-Cl. In the whole cyclic
progress, lithium ions thermodynamically favor staying in the Al–OH
octahedral cavities, but the (de)intercalation of lithium has kinetic
factors deriving from the variation of the Al–OH hydroxyl orientation.
The present results provide fundamental knowledge for the rational
design and application of LADH-Cl type lithium sorbents