王超, 张宝瑞, 郭亚龙, 刘斌, 全向, 白文刚, 王利民, 车得福. S-CO2布雷顿循环发电系统启停控制策略及动态特性研究[J]. 中国电机工程学报, 2025, 45(3): 999-1009. DOI: 10.13334/j.0258-8013.pcsee.231327
引用本文: 王超, 张宝瑞, 郭亚龙, 刘斌, 全向, 白文刚, 王利民, 车得福. S-CO2布雷顿循环发电系统启停控制策略及动态特性研究[J]. 中国电机工程学报, 2025, 45(3): 999-1009. DOI: 10.13334/j.0258-8013.pcsee.231327
WANG Chao, ZHANG Baorui, GUO Yalong, LIU Bin, QUAN Xiang, BAI Wengang, WANG Limin, CHE Defu. Research on Start-stop Control Strategy and Dynamic Characteristics of S-CO2 Brayton Cycle Power Generation System[J]. Proceedings of the CSEE, 2025, 45(3): 999-1009. DOI: 10.13334/j.0258-8013.pcsee.231327
Citation: WANG Chao, ZHANG Baorui, GUO Yalong, LIU Bin, QUAN Xiang, BAI Wengang, WANG Limin, CHE Defu. Research on Start-stop Control Strategy and Dynamic Characteristics of S-CO2 Brayton Cycle Power Generation System[J]. Proceedings of the CSEE, 2025, 45(3): 999-1009. DOI: 10.13334/j.0258-8013.pcsee.231327

S-CO2布雷顿循环发电系统启停控制策略及动态特性研究

Research on Start-stop Control Strategy and Dynamic Characteristics of S-CO2 Brayton Cycle Power Generation System

  • 摘要: 为使超临界二氧化碳(supercritical carbon dioxide,S-CO2)发电系统启停兼具安全性与快速性,该文针对600 MW S-CO2再压缩循环发电系统,提出一种两段式的热态启停控制策略。两阶段分别利用阀门联合库存控制负荷策略和改变透平入口温度控制负荷策略来实现。并提出系统各设备依次冷态启停的实施方案。利用该文提出的启停控制策略,实现600 MW S-CO2再压缩循环发电系统的启停过程。对系统启停过程的安全指标:压缩机喘振裕度、加热器最低流量、管壁温变化速率、工质高低压进行检验,所有安全指标均可得到满足。停机过程所花时间为1.11 h;启动过程所花时间为1.09 h,与文献相比,启动时长缩短0.57 h,停机时长缩短0.83 h,证明该文所设计启停控制策略的合理性和有效性。

     

    Abstract: To ensure safe and fast startup and shutdown of supercritical carbon dioxide (S-CO2) power generation system, the paper proposes a two-stage control strategy for the warm start-stop of a 600 MW S-CO2 recompression cycle power generation system. The two stages employ the valve joint inventory to control load strategy and the turbine inlet temperature control strategy, respectively. Besides, the implementation schemes of cold start and stop of each equipment in the system are put forward. Based on the start- stop control strategy proposed, the start-stop process of 600 MW S-CO2 recompression cycle power generation system is simulated. The safety indexes of the system during start and stop are tested and satisfied, including the compressor surge margin, the heater minimum flow rate, the tube wall temperature change rate, and the working fluid maximal and minimal pressures. The stop process takes 1.11 h, and the start process takes 1.09 h. Compared with the literature, the start time is shortened by 0.57 h and the stop time is shortened by 0.83 h, validating the effectiveness of the start-stop control strategy designed in this paper.

     

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