Thermodynamic modelling of a thermal energy storage packed bed tank: Exploring the influence of different particle sizes on overall performance

Concentrated solar power combined with thermal energy storage (TES) technology is now widely employed in power generation. To enhance heat transfer efficiency during thermal charging and discharging processes, a packed bed TES system has been developed due to its high heat transfer rate and large heat transfer area. To unveil the overall performance of the packed bed, thermodynamic models are introduced to avoid problems like large size and complex structure. However, current developed models are too vague to study the size effect and pressure drop induced by the particle diameter. In this work, a two-solid-phase model is introduced to evaluate the size effect in packed bed TES systems during charging and discharging, utilizing molten salt and natural volcanic ash as the heat transfer fluid and main solid filler, respectively. Compared to single-phase packed bed, introducing small particles to occupy the void between the large particles yields a low void fraction, and thus the energy storage density is improved by 36.4 %. In the meantime, the thermal charging efficiency is enhanced from 54.37 % to 75.64 %. However, the pressure drop is inevitably increased because of the very low void fraction and the increased surface in contact with the fluid. The pressure drop follows an exponential trend with the changes in particle size. Furthermore, the thermocline in the packed bed requires careful consideration, as it corresponds to the location where the maximum pressure gradient occurs. This work provides insights into the effects of the packed bed induced by the particle size, offering valuable information for the design of next-generation TES packed beds. • Thermodynamic model coupled with particle size and pressure drop is established • Advantages of two-phase TES tank are revealed by comparing with single-phase tank • Size effects on the charging/discharging and pressure drop of TES particles are investigated. • Thermocline is shown as an important location due to the highest temperature and pressure gradient

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Publication Details

Journal
Journal of Energy Storage
Published
2025-03-23
DOI
https://doi.org/10.1016/j.est.2025.116345
Citations
8
Primary Topic
Phase Change Materials Research
Type
article
Field-Weighted Citation Impact
5.71
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article

Thermodynamic modelling of a thermal energy storage packed bed tank: Exploring the influence of different particle sizes on overall performance

Xianglei Liu, Alejandro Calderón, Camila Barreneche, Marc Majó et al.
8 citations
Journal of Energy Storage
Phase Change Materials Research
5.71
article

Thermodynamic modelling of a thermal energy storage packed bed tank: Exploring the influence of different particle sizes on overall performance

Xianglei Liu, Alejandro Calderón, Camila Barreneche, Marc Majó, A. Inés Fernández, Yang Tian, Jiawei Li, Qingyang Luo
article en
8 citations

Abstract

Concentrated solar power combined with thermal energy storage (TES) technology is now widely employed in power generation. To enhance heat transfer efficiency during thermal charging and discharging processes, a packed bed TES system has been developed due to its high heat transfer rate and large heat transfer area. To unveil the overall performance of the packed bed, thermodynamic models are introduced to avoid problems like large size and complex structure. However, current developed models are too vague to study the size effect and pressure drop induced by the particle diameter. In this work, a two-solid-phase model is introduced to evaluate the size effect in packed bed TES systems during charging and discharging, utilizing molten salt and natural volcanic ash as the heat transfer fluid and main solid filler, respectively. Compared to single-phase packed bed, introducing small particles to occupy the void between the large particles yields a low void fraction, and thus the energy storage density is improved by 36.4 %. In the meantime, the thermal charging efficiency is enhanced from 54.37 % to 75.64 %. However, the pressure drop is inevitably increased because of the very low void fraction and the increased surface in contact with the fluid. The pressure drop follows an exponential trend with the changes in particle size. Furthermore, the thermocline in the packed bed requires careful consideration, as it corresponds to the location where the maximum pressure gradient occurs. This work provides insights into the effects of the packed bed induced by the particle size, offering valuable information for the design of next-generation TES packed beds. • Thermodynamic model coupled with particle size and pressure drop is established • Advantages of two-phase TES tank are revealed by comparing with single-phase tank • Size effects on the charging/discharging and pressure drop of TES particles are investigated. • Thermocline is shown as an important location due to the highest temperature and pressure gradient

Journal of Energy StorageVol. 119
Commercial Aircraft Corporation of China (China) (CN), Universitat de Barcelona (ES), Nanjing University of Aeronautics and Astronautics (CN)
Affordable and clean energy
Openalex Percentile: Top 4%
Phase Change Materials Research
5.71
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