“…Apparently, the carbonation of sodium aluminate solutions is a process not sufficiently understood, as suggested by the literature review that was presented, concerning: the composition of the PLS undergoing precipitation is not always mentioned, temperature can range from RT to 90 • C, ending pH from 9.5 to 11, gas composition (% of CO 2 in gas), the gas flow rate, stirring, reactor design, the phases precipitating mentioned are not always the same, etc. [9][10][11][12][14][15][16][17][18][19]23,24,27]. The focus of the current work is to understand the effect of the concentration of unreacted sodium carbonate that remains from the leaching step and how it affects the type/composition of the precipitates and at the same time to maximize the recovery of aluminum in the form of alumina hydrates in synthetic sodium aluminate/sodium carbonate solutions.…”