In this paper, aluminium chloride crystal was used as precursor to prepare silica-alumina aerogel support by sol-gel method, and the active component K2CO3 was supported on the aerogel support by incipient-wetness impregnation method to obtain a modified potassium-based adsorbent. CO2 adsorption experiment was performed on the adsorbent under different reaction conditions using a small fixed-bed reactor self designed. Based on the characterization results of low temperature N2 adsorption-desorption experiments and scanning electron microscopy, CO2 adsorption characteristics of modified potassium-based adsorbents were studied. The prepared silica-alumina aerogel support has good microstructure and uniform pores with specific surface area and pore volume are 445.7517 m2/g and 2.3270 cm3/g, respectively, and the mesopores account for more than 99%. After loading, the active component K2CO3 is uniformly dispersed. Through model comparison, it was determined that the shrinking core model and Avrami fractional kinetic model were used to fit the experimental results in order to study the reaction kinetics and adsorption kinetics. The results show that as the temperature rises, the amount of CO2 adsorbed by the adsorbent increases first and then decreases. The increase in temperature can improve the activity of the active site of the adsorbent and make the reversible exothermic reaction occur while the adsorbent adsorbs CO2 cannot proceed in the forward direction at the same time. According to the kinetic analysis, the control period of the surface chemical reaction is too short due to the high temperature, which caused low carbonation conversion. The optimal designed loading of modified potassium-based adsorbent, reaction temperature, water vapor pretreatment time, CO2 concentration and total gas volume were 30%, 60 °C, 30 min, 12.5%, and 500 mL/min, respectively.
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