1.中国科学院工程热物理研究所,北京 100190
2.中国科学院大学,北京 100049
3.长时规模储能重点实验室(中国科学院),北京 100190
4.“压缩空气储能”北京市重点实验室,北京 100190
张艳(2002—),女,硕士研究生,研究方向为填充床储热技术,E-mail:zhangyan@iet.cn;
王亮,研究员,研究方向为大规模储热储冷的基础研究及关键技术研发,E-mail:wangliang@iet.cn
陈海生,研究员,研究方向为新型大规模储能技术,E-mail:chen_hs@mail.etp.ac.cn。
收稿:2026-04-09,
修回:2026-04-29,
网络首发:2026-08-26,
纸质出版:2026-08-28
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ZHANG Yan, WANG Liang, LIN Xipeng, et al. Dynamic characteristics analysis of a novel thermal energy storage packed bed based on a moving airflow inlet and outlet[J]. Energy Storage Science and Technology, 2026, 15(8): 3042-3053. DOI: 10.19799/j.cnki.2095-4239.2026.0301.
为解决传统填充床储热系统出口温度非稳态波动问题,本研究提出一种基于移动气流口的新型储热填充床。该结构通过驱动气流进出口沿填充床纵向动态移动,实现了传热斜温层的准稳定推移,在高效率的同时使得储/释热过程中温度波动分别降低至38.61%和28.66%,提高了出口气流能量品质与系统运行稳定性。针对该新型进出口移动式结构,本研究建立了新型填充床的非稳态换热模型,开展了连续储释热工况的三维动态数值仿真,探究了气流口移动方式、运行条件、材料等因素对新型填充床储热动态特性的作用机制。结果显示,本研究的填充床在长宽比为4∶1时可平衡效率与稳定性;减小填充球粒径能提高效率,但不利于稳定性;对于本研究采用的长宽高比为4∶1∶15、总体积0.06 m
3
的填充床,在质量流量0.007 kg/s、储/释热时间6250 s的运行条件下可满足热效率95.76%的稳定循环运行;93%的进出口移动范围可改善温度“滞后”现象,提升填充床循环性能,使其以较低波动长期循环运行。本研究为大规模高温储热提供了新的技术路线与解决方案。
To address outlet temperature fluctuations in conventional packed-bed thermal energy storage (TES) systems
this study proposes a novel packed bed with moving inlet and outlet. By dynamically moving the inlet and outlet along the longitudinal direction
the system achieves quasi-stable thermocline motion. As a result
temperature fluctuations during the charging and discharging processes are reduced to 38.61% and 28.66%
respectively
improving both outlet airflow quality and system stability. A transient heat transfer model was developed for the new packed bed
and three-dimensional dynamic numerical simulations were carried out under continuous charging and discharging conditions. The effects of inlet/outlet movement mode
operating conditions
and packing materials on dynamic thermal storage characteristics were systematically investigated. The results show that a packed bed with a 4∶1 aspect ratio offers a favorable balance between efficiency and stability. Although reducing particle size improves efficiency
it also reduces system stability. For a packed bed with relative dimensions of 4∶1∶15 (length∶width∶height) and a total volume of 0.06 m
3
stable cyclic operation with a 95.76% thermal efficiency was achieved at a 0.007 kg/s mass flow rate
and 6250 s charging/discharging times. In addition
the 93% inlet and outlet movement range alleviates the temperature lag effect
enhances cyclic performance
and enables long-term operation with low fluctuations. This study provides a new technical route and theoretical basis for applying moving inlet and outlet packed beds in large-scale high-temperature TES systems.
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