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Abstract The noncatalytic gas solid reaction between calcined dolomite and CO2 g has been studied in an electrobalance reactor as a function of temperature pressure and reactive gas composition Multicycle tests consisting of as many as ten complete calcination carbonation cycles were carried out to obtain information on sorbent durability
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Thermochemical equilibrium calculations indicate the possibility of considerable fuel savings and CO2 emission avoidance in the three steps of the Pidgeon process a calcination of dolomite b production of ferrosilicon from quartz sand coal and iron oxide c silicothermic reduction of calcined dolomite by ferrosilicon to magnesium
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