Energy Storage Science and Technology
Mingjuan GAO1,2(
), Guoliang SONG1,2(
), Weijian SONG1, Jingzhang LIU1
Received:2025-10-22
Revised:2025-11-13
Online:2025-11-17
Contact:
Guoliang SONG
E-mail:gaomingjuan@iet.cn;songgl@iet.cn
CLC Number:
Mingjuan GAO, Guoliang SONG, Weijian SONG, Jingzhang LIU. Research progress on high-temperature flue gas heating solid particle thermal energy storage technology[J]. Energy Storage Science and Technology, doi: 10.19799/j.cnki.2095-4239.2025.0943.
Table 2
Thermal properties of common solid materials"
| 材料 | 温度(℃) | 密度(kg/m3) | 比热容(kJ/(kg·K)) | 热导率(W/(m·K)) | 体积热容(kJ/(m3·K)) |
|---|---|---|---|---|---|
| 混凝土 | 350 | 2250 | 1.01 | 1.23 | 2272.5 |
| 花岗岩 | 20 | 2750 | 0.89 | 2.9 | 2447.5 |
| 玄武岩 | 20 | 2768 | 0.85 | 2.1 | 2352.8 |
| 石灰岩 | 20 | 2600 | 0.81 | 2.2 | 2106 |
| 硅基耐火材料 | 20 | 2340 | 0.86 | 1.75 | 2012.4 |
| 沙子(SiO2) | 20 | 1454 | 0.76 | 0.25 | 1105.04 |
| 600 | 1454 | 1.2 | 0.48 | 1744.8 | |
| 矿渣 | 20 | 2700 | 0.84 | 0.57 | 2268 |
| 可浇注陶瓷 | 20 | 3500 | 0.86 | 1.4 | 3010 |
| 氧化铝 | 20 | 3984 | 0.76 | 33.4 | 3027.84 |
| 岩盐(Halite) | 20 | 2170 | 0.88 | 6.1 | 1909.6 |
| 氯化钠 | 20 | 2165 | 0.86 | 6.5 | 1861.9 |
| 碳化硅(SiC) | 20 | 3220 | 1.15 | 83 | 3703 |
Table 3
Performance comparison of solid particle thermal storage materials"
| 材料 | 密度 (kg/m3) | 比热容 (kJ/(kg·K)) | 热导率 (W/(m·K)) | 体积热容 (kJ/(m3·K)) | 最高使用温度(℃) | 成本 (美元/吨) | 主要优缺点 |
|---|---|---|---|---|---|---|---|
| 玄武岩 | 2768 | 0.85 | 2.1 | 2352.8 | 700 | 126 | 成本较低、中低温下稳定、热导率较低 |
| 硅砂(SiO2) | 1454 | 1.2 | 0.48 | 1744.8 | 1200 | 30-40 | 温域宽、成本低、热导率低 |
| 钢渣 | 3430 | 0.877 | 1.46 | 3008 | ≥700 | 负成本 | 成本极低、固废利用、热导率较低,成分波动 |
| 氧化铝 | 3984 | 0.76 | 33.4 | 3027.84 | 1100-1200 | 1596.8 | 热导率较高、高温稳定、成本高 |
| 碳化硅(SiC) | 3220 | 1.15 | 83 | 3703 | 1400 | 极高 | 热导率和体积热容高、成本极高 |
玻璃化石棉废物 Cofalit® | 3120 | 0.9-0.964 | 1.49-1.55 | 2800-3000 | 1200 | 12 | 成本极低、动态热响应好、长期稳定性待研究 |
回收陶瓷 (ReThinkSeramic-Flora) | 2350-2400 | 1.1 | 2.2 | 2585-2640 | 1200 | 较低 | 成本较低、环境可持续、高温耐受能力强、热导率较低 |
Table 4
Features of flue gas-particle heat exchangers"
| 类型 | 优点 | 缺点 | 适用场景 |
|---|---|---|---|
| 填充床换热器 | 结构简单、成本低、 技术成熟,颗粒磨损小 | 体积庞大、换热性能差、难以平衡传热和压降、热响应速度慢 | 宽温域储热、低成本需求 |
| 移动床直接接触换热器 | 重力驱动、结构简单、 成本低、传热系数高 | 存在颗粒夹带问题、局部颗粒 换热不均匀、难以工业放大 | 中高温、含尘、易腐蚀烟气 |
| 移动床管壳式换热器 | 重力驱动、传热系数高、不存在工质污染风险、结构紧凑 | 管道顶部颗粒的停滞区和底部的 空隙区影响换热,成本较高 | 高温储热、无污染要求场景 |
| 移动床板壳式换热器 | 重力驱动、传热系数高、 结构紧凑且设计灵活 | 压降增加、易堵塞、 制造与维护复杂性增加 | 对工作温度、系统可靠性和 换热效率有极高要求 |
| 流化床换热器 | 技术成熟、传热系数高、 颗粒储热提升一体化 | 不可逆损失大、流化风能量损失、 颗粒夹带与磨损 | 中高温储热、高传热、 高气速、高固含率系统 |
| 回转窑换热器 | 结构紧凑、处理量大、 运行稳定性较高 | 局部换热不均、能耗与维护 成本较高、传热性能受限 | 高温、长停留时间、良好物料混合和高效热交换的固体处理过程 |
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