Abstract

The behavior of Fe2O3/Al2O3 particles as oxygen carriers (OCs) for CO chemical looping combustion (CLC) under different reaction temperatures (700 °C, 800 °C, 900 °C, and 1000 °C) were tested in a lab-scale fluidized bed and a thermogravimetric analysis (TGA) unit. The results show that the oxygen carrier presents the highest reactivity at 800 °C, even after 30 cycles of redox reaction in a fluidized bed, while more obvious carbon deposition occurred for the case at 700 °C, and agglomeration for the case at 1000 °C. Moreover, the detailed behavior of the prepared Fe2O3/Al2O3 particle was detected in the TGA apparatus at different reaction temperatures. Furthermore, temperature-programming TGA experiments were performed to investigate the influence of different CO concentrations and CO/CO2 concentrations on the reaction between CO and OC during the chemical looping combustion processes. Based on these experimental behaviors of the prepared Fe2O3/Al2O3 during the CLC of CO, the detailed models and electronic properties of the pure and reduced Fe2O3/Al2O3 supported the slabs, CO adsorption, and oxidation, and the decomposition reactions on these surfaces were revealed using density functional theory (DFT) calculations which went deep into the nature of the synergetic effect of the support of Al2O3 on the activity of Fe2O3 for the CLC of CO.

Highlights

  • Chemical looping combustion (CLC) has been suggested as an effective technology to capture CO2 without extra energy consumption and with nearly zero emission of pollutants [1,2]

  • In the fuel reactor (FR), fossil fuel is oxidized into CO2 and H2 O by an oxygen carrier (OC), while the oxygen carriers (OCs) is reduced to lower valence states

  • Reaction 1 is often endothermic, Reaction 2 is exothermic and the oxidized OC can act as a heat carrier to transfer the energy needed to maintain the reduction reaction that has happened in the FR

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Summary

Introduction

Chemical looping combustion (CLC) has been suggested as an effective technology to capture CO2 without extra energy consumption and with nearly zero emission of pollutants [1,2]. In the FR, fossil fuel is oxidized into CO2 and H2 O by an oxygen carrier (OC), while the OC is reduced to lower valence states (see Reaction 1). The reduced OC is transferred to the AR, and is oxidized into its original state by air (Reaction 2). Reaction 1 is often endothermic, Reaction 2 is exothermic and the oxidized OC can act as a heat carrier to transfer the energy needed to maintain the reduction reaction that has happened in the FR. The total amount of heat obtained from the CLC system is even more than that of conventional combustion because of the lower irreversibility of the two reaction courses [6,7]

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