Abstract In framework of the thermochemical energy storage (TCES) in concentrating solar power (CSP) applications, great attention is focused on the SrCO3/SrO system, which is characterized by remarkably high theoretical… Click to show full abstract
Abstract In framework of the thermochemical energy storage (TCES) in concentrating solar power (CSP) applications, great attention is focused on the SrCO3/SrO system, which is characterized by remarkably high theoretical volumetric energy density (4 GJ m SrC O 3 - 3 ) and working temperatures (1200 °C). It has been shown that the incorporation of Al2O3 in the SrO/SrCO3 system can successfully hinder the sintering and agglomeration phenomena, thus improving the performances of the system. Aiming at providing useful information for the design, simulation and scale up of a reactor for the energy storage, besides the multicycle carbonation conversion, the evaluation of the reaction kinetics is crucial. Thus, in this work, the kinetics of the carbonation of a SrO-Al2O3 composite (34%wt of Al2O3) for TCES-CSP has been investigated for the first time using a two-stage kinetic model. In particular, tests have been performed in a thermogravimetric analyzer at operating conditions relevant for TCES, namely at 1 atm of CO2 partial pressure within the temperature range of 900–1050 °C. The reaction rate, the intrinsic carbonation kinetic constant, the characteristic product layer thickness and their dependence on the temperature has been evaluated in the temperature range 900–1000 °C; the activation energy has been found to be 52 kJ mol−1. Finally, comparison of the calculated conversion-time profiles, obtained from the applied kinetic models, with experimental data revealed a good agreement.
               
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