Breakthrough analysis for CO 2 removal by activated hydrotalcite and soda ash

Abstract

Carbon dioxide sorption rate parameters and sorption capacities on two different regenerable sorbents, namely hydrotalcite and activated trona, were investigated in a fixed bed flow adsorber, in the temperature range of 400–527 °C and 80–152 °C, respectively. Hydrotalcite, which was activated at 550 °C, was shown to give total and breakthrough CO 2 sorption capacities as high as 1.16 and 0.70 mmol/g, respectively, at 452 °C, in the absence of water vapor. In the presence of excess water vapor, the total CO 2 sorption capacity was not affected much, however a decrease in the breakthrough capacity and on the sorption rate constant was observed, especially at lower temperatures. In the presence of water vapor, activated trona was shown to give comparable total and breakthrough CO 2 sorption capacities, at much lower temperatures ( T < 100 °C). The deactivation model gave good predictions of the CO 2 breakthrough curves and it was successfully used for the evaluation of the adsorption and the deactivation rate constants.