Thermochemical energy storage using the material system CaO/Ca(OH)2 is regarded as one of the most promising
technologies for application temperatures between 400 ◦C and 600 ◦C. There is still a lack of information
concerning the transfer of laboratory results to industrially-relevant conditions. This study addresses this
research gap and provides data for a continuously operated pilot-scale fluidized-bed storage reactor (257 mm
diameter, up to 31 L fluidized bed volume, maximal 700 ◦C and 6 barg). The reactor is operated near the thermodynamic
equilibrium at varying space times of the storage material (250 - 400 μm). The bed height is
maintained at 390 mm during continuous operation. The results indicate good fluidization quality at steady-state
operation for up to 9 h. Based on the results, a CSTR-type reactor model is proposed and validated, giving good
results in predicting the fluidized bed’s steady-state conversion and temperature. The model is based on material
and fluidization properties, such as the fluidized beds porosity, that are measured in dependence of temperature
and superficial gas velocity. The simulation results indicate that the heat transfer characteristics are crucial for
adequate storage power.
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Thermochemical energy storage using the material system CaO/Ca(OH)2 is regarded as one of the most promising
technologies for application temperatures between 400 ◦C and 600 ◦C. There is still a lack of information
concerning the transfer of laboratory results to industrially-relevant conditions. This study addresses this
research gap and provides data for a continuously operated pilot-scale fluidized-bed storage reactor (257 mm
diameter, up to 31 L fluidized bed volume, maximal 700 ◦C and 6...
»