Abstract

CaO and MgO are important industrial raw materials commonly produced by either the decomposition of calcium carbonate at about 900 °C, or the calcination of dolomite, a mixed calcium and magnesium carbonate, calcined either to MgO.CaCO 3 at about 750 °C, or to MgO.CaO at 900 °C. ln this research, the decomposition reaction of 104–147 μm dolomite and limestone particles was investigated, both without and with steam added to the reaction. A series of experiments was performed in terms of relevant parameters such as time, temperature and amount of H 2 O added. Reactants and reaction products were fully characterized and demonstrate the different morphology and specific surface area of the raw carbonate ores and the calcined oxides. Adding H 2 O during calcination has a significant positive effect. The calcination shows that steam can significantly accelerate the reaction rate, and reduce the decomposition temperature by ∼100 °C, thus reducing the cost of the decomposition by increasing the yield for a given reaction time, while also reducing the required sensible heat of the feedstock and combustion air . This ultimately reduces the amount of fossil fuel or alternative energy carriers, thus reducing the CO 2 footprint of the system. The improved operating conditions foster the use of concentrated solar calcination. The CO 2 footprint of the carbonate decomposition can be reduced by ∼4% in traditional kilns , and by as much as 20% if concentrated solar kilns are used. Both applications are currently investigated in pilot-scale operations. • Calcination of dolomite and limestone particles was studied, without and with adding steam. • Steam accelerates the reaction rate and reduces the calcination temperature by ∼100 °C. • Adding steam reduces the energy requirement, thus reducing the CO 2 footprint of the system. • CO 2 emissions are reduced by ∼4% in conventional kilns, and by ∼20% in solar kilns applications.

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