A new aqueous mineral carbonation process which utilizes bipolar membrane electrodialysis was proposed. The proposed process consists of four unit operations, (a) acid leaching of alkaline metals (Ca
2+ /Mg
2+) from mineral compounds, (b) carbonate precipitation by addition of Na
2CO
3, (c) acid /alkaline regeneration from salt solution with bipolar membrane electrodialysis, and (d) Na
2CO
3 generation via absorption of CO
2 into NaOH. In the acid leaching step, alkaline metals are extracted from mineral compounds such as alkaline rocks, concrete waste, and steel making slag. In this operation, HNO
3 solution is adopted as a leaching solution. In the carbonation sedimentation step, by adding Na
2CO
3 solution into the leaching solution, sediment of carbonate such as CaCO
3 or MgCO
3 is obtained and NaNO
3 solution is remained. In the acid /alkaline regeneration step, HNO
3 solution and NaOH solution are regenerated from NaNO
3 solution via bipolar membrane electrodialysis treatment. Regenerated HNO
3 solution is then recycled to the acid leaching step. In the Na
2CO
3 generation step, regenerated NaOH solution is contacted with the gaseous CO
2 to form Na
2CO
3 solution. Exhaust gas from power plant can be directly used without compression. Experimental studies were conducted to confirm the technical feasibility of this process. Results demonstrate that the combination of acid leaching and carbonation sedimentation enhances the utilization of alkaline metals in mineral compounds. Also, HNO
3 and NaOH were successfully regenerated from NaNO
3 solution. This result suggests that acid and alkaline solution can be used cyclically in this process.
