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The guidelines for assessing the apparent activation energies of gas/solid reactions have been proposed based on the experimental results from literatures. In CO2 free inlet gas flow, CaCO3 decomposition between 950 and 1250 K with thin sample layer could be controlled by the interfacial chemical reaction with apparent activation energy E = (215±10) kJ/mol and E = (200±10) kJ/mol at T = 813 to 1020 K, respectively. With relatively thick sample layer between 793 and 1273 K, the CaCO3 decomposition could be controlled by one or more steps involving self-cooling, nucleation, intrinsic diffusion and heat transfer of gases, and E could vary between 147 and 190 kJ/mol. In CO2 containing inlet gas flow (5%-100% of CO2), E was determined to be varied from 949 to 2897 kJ/mol. For SrCO3 and BaCO3 decompositions controlled by the interfacial chemical reaction, E was (213±15) kJ/mol (1000-1350 K) and (305±15) kJ/mol (1260-1400 K), respectively.
The guidelines for assessing the apparent activation energies of gas / solid reactions have been proposed based on the experimental results from literatures. In CO2 free inlet gas flow, CaCO3 decomposition between 950 and 1250 K with thin sample layer could be controlled by the interfacial chemical reaction with apparent activation energy E = (215 ± 10) kJ / mol and E = (200 ± 10) kJ / mol at T = 813 to 1020 K, respectively. With relatively thick sample layers between 793 and 1273 K, the CaCO3 decomposition could be controlled by one or more steps involving self-cooling, nucleation, intrinsic diffusion and heat transfer of gases, and could C vary between 147 and 190 kJ / mol. In CO2 containing inlet gas flow (5% -100% of CO2) For SrCO3 and BaCO3 decompositions controlled by the interfacial chemical reaction, E was (213 ± 15) kJ / mol (1000-1350 K) and (305 ± 15) kJ / mol. mol (1260-1400 K), respectively.