The characteristics of CO 2 reacting with CaO in a molten eutectic mixture of CaF 2 and NaF has been investigated. Calculations of the Gibbs free energy, temperature analysis of the decomposition of the formed carbonates, and XRD analyses of quenched samples taken during CO 2 absorption or desorption were employed to identify the phases present in the melt. Efficient CO 2 absorption from a simulated flue gas was observed, due to a combined reaction where CaO initially reacts with CO 2 and forms CaCO 3 . Subsequently, Na 2 CO 3 is formed by an ion exchange reaction between CaCO 3 and NaF. It was found that the CaO activity is highest in the temperature range 826-834°C. Increasing the CaO concentration from 5 to 20 wt% in the molten salt resulted in reduced CO 2 reactivity efficiency, probably because of precipitation and agglomeration of the sorbent. The total carbonation conversion was independent of the CO 2 concentration in the inlet gas, and the sorbent carrying capacity was in the range 0.722-0.743 g CO 2 /g CaO corresponding to 0.037-0.144 g CO 2 /g total liquid. Decarbonation was conducted by raising the temperature. 40% conversion back to CaO was recorded at 1160°C. The recorded curves for the CO 2 concentration in the outlet gas exhibited a rapid desorption step followed by a slow step.
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