Separation of K2CO3 from Li+ Brine with Aid of CO2 and Trace of Metastable Quaternary System Li+–K+–CO32−–HCO3−–H2O
AbstractIt is of importance to reclaim single-salt of potash from Li+-type brines of low concentration. In this work the potassium salts KHCO3 was efficiently separated from the lithium carbonate-type brines with the aid of CO2 carbonation. The phase field was provided in which the precipitation of KHCO3 occurs and single-salt of potassium can be obtained. The low concentration of [Li+] was also successfully concentrated to a high level (8.1 g/L), and this concentration can be used as sources for Li+-salts production using pre-developed strategies, which looks forward wider applications of the lithium resources of natural brine. This state-of-art was traced via isotherm evaporation on the quaternary system of Li+–K+–CO32−–H2O at 298.15 K in which the carbonation steps were performed by CO2. Metastable phase diagram was found to consist of three invariant points, seven univariant curves, and four crystallization fields corresponding to Li2CO3, KHCO3, potassium carbonate sesquihydrate (K2CO3 ⋅ 3/2H2O), and a potassium carbonate and potassium bicarbonate double salt (K2CO3 ⋅ 2 KHCO3 ⋅ 1.5H2O). There was no crystallization field corresponding to LiHCO3. The pH-composition diagram and density-composition diagram were also plotted. This work was carried out in aim of extracting/separating single salts of alkali metals from carbonate-type brines of west China.