综合智慧能源 ›› 2026, Vol. 48 ›› Issue (5): 64-73.doi: 10.3969/j.issn.2097-0706.2026.05.007
收稿日期:2025-09-25
修回日期:2025-11-09
出版日期:2025-12-25
通讯作者:
*耿士敏(1987),女,讲师,硕士,从事电厂热力系统及节能等方面的研究,gengsm@hebust.edu.cn。作者简介:岳柏杨(2000),男,硕士生,从事能源系统设计与优化及热物理测量等方面的研究,resbaiyang@163.com;基金资助:
YUE Baiyang(
), GENG Shimin*(
), CHENG Siyuan(
)
Received:2025-09-25
Revised:2025-11-09
Published:2025-12-25
Supported by:摘要:
为实现“双碳”目标下火电机组的深度调峰与灵活运行,提升大功率凝汽式机组的电网适应性,针对一台600 MW凝汽式机组,开展熔盐储热系统的耦合设计与经济性分析,旨在提出一种兼顾调峰能力与热经济性的技术改造方案。基于EBSILON软件构建机组热力系统仿真模型,并验证了其准确性。提出2种抽汽储热方案:方案1抽取再热蒸汽,方案2抽取主蒸汽。在额定工况下,以90 MW储热负荷为基础,建立储热-释热耦合系统模型,并从调峰容量、全厂热效率、绝对电效率、系统循环效率及工程适用性5个维度进行对比分析。结合河北省峰谷电价政策,估算系统的日均收益与静态投资回收期。仿真结果表明:方案1与方案2的调峰容量分别为38.85 MW与54.70 MW;系统循环效率分别为84.6%与60.1%;在典型峰谷电价下,方案1与方案2的日均净收益分别为9.81万元与7.05万元;静态投资回收期分别为2.08 a与3.53 a。方案1在系统循环效率、绝对电效率及经济性等方面均表现更优。对于大功率凝汽式机组的熔盐储热改造,抽取再热蒸汽的方案在保证显著调峰能力的同时,具有更优的热经济性与更短的投资回收期,综合性能更佳,可作为同类机组灵活性改造的推荐技术路线。
中图分类号:
岳柏杨, 耿士敏, 程思远. 600 MW凝汽式机组熔盐储热系统设计及经济性分析[J]. 综合智慧能源, 2026, 48(5): 64-73.
YUE Baiyang, GENG Shimin, CHENG Siyuan. Design and economic analysis of molten salt thermal storage system for 600 MW condensing unit[J]. Integrated Intelligent Energy, 2026, 48(5): 64-73.
表1
600 MW凝汽式机组原始参数
| 参数 | 数值 |
|---|---|
| 主蒸汽压力p0/MPa | 16.702 0 |
| 主蒸汽温度t0/℃ | 531.80 |
| 高压缸排汽压力p2/MPa | 3.828 0 |
| 高压缸排汽温度t2/℃ | 301.72 |
| 再热蒸汽进口压力 | 3.218 0 |
| 再热蒸汽进口温度 | 300.94 |
| 再热蒸汽出口压力 | 3.218 0 |
| 再热蒸汽出口温度 | 531.80 |
| 低压缸排汽压力pc/MPa | 0.004 5 |
| 低压缸排汽干度xc | 0.905 6 |
| 给水泵出口压力 | 18.784 0 |
| 给水泵出口温度 | 171.88 |
| 小汽轮机排汽压力pc,xj/MPa | 0.006 0 |
| 小汽轮机排汽比焓hc,xj/(kJ·kg-1) | 2 422.6 |
表8
技术指标对比
| 技术指标 | 原始机组 | 方案1 | 方案2 |
|---|---|---|---|
| 高/低温熔盐罐 温度/℃ | 268.5/150.0 | 323.5/205.0 | |
| 熔盐流量/(kg·h-1) | 1.75×106 | 1.75×10⁶ | |
| 抽汽量/(t·h-1) | 122.230 | 129.607 | |
| 调峰容量/MW | 38.846 | 54.698 | |
| 储/释热阶段发电功率/MW | 600.00 | 561.15/623.49 | 545.30/623.49 |
| 储/释热过程全厂 热效率 | 0.412 0 | 0.498 7/0.554 2 | 0.484 7/0.554 2 |
| 储/释热过程 绝对电效率 | 0.456 0 | 0.552 5/0.613 9 | 0.536 9/0.613 9 |
| 系统循环效率 | 0.846 | 0.601 |
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