Aqueous mineral carbonation is a potentially attractive sequestration technology to reduce CO
2 emissions.The energy consumption of this technology, however, reduces the net amount of CO
2 sequestered. Therefore,the energetic CO
2 sequestration efficiency of aqueous mineral carbonation was studied in dependence ofvarious process variables using either wollastonite (CaSiO
3) or steel slag as feedstock. For wollastonite, themaximum energetic CO
2 sequestration efficiency within the ranges of process conditions studied was 75% at200
C, 20 bar CO
2,
and a particle size of <38
m. The main energy-consuming process steps were thegrinding of the feedstock
and the compression of the CO
2 feed. At these process conditions, a significantlylower efficiency was determined for steel slag (69%), mainly because of the lower Ca content of the feedstock.The CO
2 sequestration efficiency might be improved substantially for both types of feedstock by, e.g., reducingthe amount of process water applied
and further grinding of the feedstock. The calculated energetic efficiencieswarrant a further assessment of the (energetic) feasibility of CO
2 sequestration by aqueous mineral carbonationon the basis of a pilot-scale process.