Synthesis of Ca(OH)(2) and Na(2)CO(3) through anion exchange between CaCO(3) and NaOH: effect of reaction temperature

The CO(2) released upon calcination of limestone accounts for the largest portion of the emissions from the cement, lime, and slaked lime manufacturing industries. Our previous works highlighted the possibility for a no-combustion decarbonisation of CaCO(3) through reaction with NaOH solutions to produce Ca(OH)(2) at ambient conditions, while sequestrating the process CO(2) in a stable mineral Na(2)CO(3)·H(2)O/Na(2)CO(3). In this study, the effect of temperature was assessed within the range of 45–80 °C, suggesting that the process is robust and only slightly sensitive to temperature fluctuations. The proportioning of the precipitated phases Na(2)CO(3)·H(2)O/Na(2)CO(3) was also assessed at increasing NaOH molalities and temperatures, with the activity of water playing a crucial role in phase equilibrium. The activation energy (E(a)) of different CaCO(3) : NaOH : H(2)O systems was assessed between 7.8 kJ·mol(−1) and 32.1 kJ·mol(−1), which is much lower than the conventional calcination route. A preliminary energy balance revealed that the chemical decarbonisation route might be ∼4 times less intensive with respect to the thermal one. The present work offers a further understanding of the effect of temperature on the process with the potential to minimise the emissions from several energy-intensive manufacturing processes, and correctly assess eventual industrial applicability.