Global cross-scale simulation and experiment of supercritical CO2 boiler tube wall temperature based on bidirectional fluid-thermal coupling

IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Applied Thermal Engineering Pub Date : 2025-06-01 Epub Date: 2025-02-13 DOI:10.1016/j.applthermaleng.2025.125893
Xuan Wang , Jiabao Chen , Yuanxun Ding , Ping Yuan , Jingwen Yan , Ligeng Li , Hua Tian , Gequn Shu
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Abstract

sCO2 cycle power generation, with wide thermal source applicability and flexible maneuverability, is considered one of the transformative technologies for hybrid power generation with renewable energy. sCO2 boilers, as key equipment, are typically equipped with numerous bundles to adapt load changes under varying conditions. Currently, 0/1D modular furnace models cannot accurately capture the temperature distribution of the cold wall, and it’s unrealistic to build the sCO2 boiler’s 3D global transient variation model. Some scholars have used 3D + 1D to explore tube wall temperatures, but lack experiments validated and transient predictions. Therefore, this paper establishes a multi-scale transient coupling model of global sCO2 boiler to predict the tube wall temperature change rate to ensure safe operation under variable operation. It fully considers the structure of the heat exchanger tubes and the deviation of heat transfer between the flue gas and sCO2, and accurately captures the wall temperature variation. The transient coupling model validated with experiments shows a maximum deviation of 24.26 K and an error margin of 2.82 %. And the highest tube wall temperature tends to occur near the outlet of the No. 80 heat exchanger located in the middle of the combustion chamber. Transient simulations also revealed the heat exchanger tubes near the exhaust side have a higher temperature change rate increase on their outer walls compared to the tubes near the ignition side, while their rate of temperature decrease is lower. This study is important for avoiding thermal fatigue of heat exchanger tubes under variable load regulation of the unit.

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基于双向流热耦合的超临界CO2锅炉管壁温度全局跨尺度模拟与实验
sCO2循环发电具有热源适用性广、可操作性强的特点,是可再生能源混合发电的变革性技术之一。sCO2锅炉作为关键设备,为适应不同工况下负荷的变化,通常配置多束。目前,0/1D模块化炉模型无法准确捕捉冷壁温度分布,建立sCO2锅炉三维全局瞬态变化模型是不现实的。一些学者使用3D + 1D方法来探测管壁温度,但缺乏实验验证和瞬态预测。为此,本文建立了全局sCO2锅炉的多尺度瞬态耦合模型,以预测变工况下的管壁温度变化率,保证其安全运行。充分考虑了换热管的结构和烟气与sCO2之间的传热偏差,准确捕捉了壁面温度的变化。经实验验证的瞬态耦合模型最大偏差为24.26 K,误差范围为2.82%。而最高的管壁温度往往出现在位于燃烧室中部的80号换热器出口附近。瞬态模拟还表明,靠近排气侧的热交换器管的外壁温度变化率比靠近点火侧的热交换器管的外壁温度变化率更高,而温度下降速率更低。研究结果对机组变负荷调节下换热器管的热疲劳问题具有重要意义。
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来源期刊
Applied Thermal Engineering
Applied Thermal Engineering 工程技术-工程:机械
CiteScore
11.30
自引率
15.60%
发文量
1474
审稿时长
57 days
期刊介绍: Applied Thermal Engineering disseminates novel research related to the design, development and demonstration of components, devices, equipment, technologies and systems involving thermal processes for the production, storage, utilization and conservation of energy, with a focus on engineering application. The journal publishes high-quality and high-impact Original Research Articles, Review Articles, Short Communications and Letters to the Editor on cutting-edge innovations in research, and recent advances or issues of interest to the thermal engineering community.
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