1. Performance of an indirect packed bed reactor for chemical energy storage
- Author
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Raffaele Liberatore, Tiziano Delise, Natale Corsaro, Annarita Spadoni, Tania Morabito, Anna Chiara Tizzoni, Salvatore Sau, Emiliana Mansi, Delise, T., Sau, S., Tizzoni, A. C., Spadoni, A., Corsaro, N., Liberatore, R., Morabito, T., and Mansi, E.
- Subjects
Work (thermodynamics) ,Technology ,Materials science ,Nuclear engineering ,Mass flow ,Thermal storage ,Chemical storage ,Indirect heat exchanger ,Thermal energy storage ,Storage efficiency ,Article ,Packed bed ,Heat exchanger ,General Materials Science ,Fluid-dynamic simulations ,Microscopy ,QC120-168.85 ,business.industry ,Thermochemical energy storage ,QH201-278.5 ,Engineering (General). Civil engineering (General) ,TK1-9971 ,Chemical energy ,Descriptive and experimental mechanics ,Computer data storage ,Electrical engineering. Electronics. Nuclear engineering ,TA1-2040 ,business - Abstract
Chemical systems for thermal energy storage are promising routes to overcome the issue of solar irradiation discontinuity, helping to improve the cost-effectiveness and dispatchability of this technology. The present work is concerned with the simulation of a configuration based on an indirect-packed bed heat exchanger, for which few experimental and modelling data are available about practical applications. Since air shows advantages both as a reactant and heat transfer fluid, the modelling was performed considering a redox oxide based system, and, for this purpose, it was considered a pelletized aluminum/manganese spinel. A symmetrical configuration was selected and the calculation was carried out considering a heat duty of 125 MWth and a storage period of 8 h. Firstly, the heat exchanger was sized considering the mass and energy balances for the discharging step, and, subsequently, air inlet temperature and mass flow were determined for the charging step. The system performances were then modelled as a function of the heat exchanger length and the charging and discharging time, by solving the relative 1D Navier-Stokes equations. Despite limitations in the global heat exchange efficiency, resulting in an oversize of the storage system, the results showed a good storage efficiency of about 0.7.
- Published
- 2021