中国电力 ›› 2024, Vol. 57 ›› Issue (1): 183-194.DOI: 10.11930/j.issn.1004-9649.202306048
• 面向碳达峰碳中和目标的清洁高效发电技术 • 上一篇 下一篇
收稿日期:
2023-06-14
出版日期:
2024-01-28
发布日期:
2024-01-23
作者简介:
晁文浩(1998—),男,硕士研究生,从事碳捕集电厂优化调度研究,E-mail:3074644207@qq.com基金资助:
Wenhao CHAO1(), Zhi YUAN1(
), Ji LI2
Received:
2023-06-14
Online:
2024-01-28
Published:
2024-01-23
Supported by:
摘要:
在风-火-核-碳捕集多源联合系统中,核电机组在参与电网调峰时存在调峰深度选择不精确的问题。此外,该多源联合系统还存在风电消纳不足的问题。为此,构建了一种计及线性化核电机组调峰深度模型的电转气(power to gas,P2G)-风-火-核-碳捕集多源联合系统,并对该系统进行了日前优化调度。首先,基于核电机组负荷跟踪模式,通过引入连续变量,提高了调峰深度选择的准确性;然后,分析了碳捕集电厂-P2G联合运行模式及需求响应资源对促进风电消纳的积极作用;最后,以系统综合运行成本最低为目标函数,同时考虑碳交易机制,在Matlab平台搭建仿真模型,验证了所构建多源联合系统的有效性。结果表明,相较于核电机组采用固定调峰档位的多源联合系统,所构建的多源联合系统能够在保证核电机组安全稳定运行的同时,实现风电完全消纳,系统碳排放量与综合运行成本分别下降了13.74%与6.27%,提高了系统运行的低碳性与经济性。
晁文浩, 袁至, 李骥. 计及电转气-风-火-核-碳捕集的多源联合系统优化调度[J]. 中国电力, 2024, 57(1): 183-194.
Wenhao CHAO, Zhi YUAN, Ji LI. Optimal Dispatch of Power System with P2G-Wind-Thermal-Nuclear-Carbon Capture Units[J]. Electric Power, 2024, 57(1): 183-194.
图 1 计及线性化核电机组调峰深度模型的P2G-风-火-核-碳捕集多源联合系统框架
Fig.1 Framework of P2G-wind-thermal-nuclear-carbon capture multi-source combine system with a linearized nuclear power unit peaking depth model
项目 | 场景1 | 场景2 | 场景3 | 场景4 | ||||
核电调峰成本/万元 | 19.79 | 20.03 | 9.23 | 2.32 | ||||
日折旧成本/万元 | 64.39 | 64.39 | 64.39 | 64.39 | ||||
溶剂损耗成本/万元 | 16.96 | 16.99 | 17.73 | 17.77 | ||||
P2G运行成本/万元 | — | — | 13.33 | 7.16 | ||||
碳封存成本/万元 | 20.56 | 20.50 | 7.71 | 7.86 | ||||
碳交易成本/万元 | –355.36 | –358.93 | –367.53 | –392.22 | ||||
弃风率/% | 1.66 | 1.28 | 0.70 | 0.00 | ||||
碳排放量/t | 30 659.10 | 30 142.90 | 29 831.30 | 26 445.30 | ||||
综合运行成本/万元 | 940.47 | 936.03 | 903.46 | 881.54 |
表 1 不同场景下的调度结果
Table 1 Scheduling results of different scenarios
项目 | 场景1 | 场景2 | 场景3 | 场景4 | ||||
核电调峰成本/万元 | 19.79 | 20.03 | 9.23 | 2.32 | ||||
日折旧成本/万元 | 64.39 | 64.39 | 64.39 | 64.39 | ||||
溶剂损耗成本/万元 | 16.96 | 16.99 | 17.73 | 17.77 | ||||
P2G运行成本/万元 | — | — | 13.33 | 7.16 | ||||
碳封存成本/万元 | 20.56 | 20.50 | 7.71 | 7.86 | ||||
碳交易成本/万元 | –355.36 | –358.93 | –367.53 | –392.22 | ||||
弃风率/% | 1.66 | 1.28 | 0.70 | 0.00 | ||||
碳排放量/t | 30 659.10 | 30 142.90 | 29 831.30 | 26 445.30 | ||||
综合运行成本/万元 | 940.47 | 936.03 | 903.46 | 881.54 |
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