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    50 MW超临界二氧化碳燃煤锅炉热力性能研究及计算平台开发

    Thermodynamic study and computational platform development for a 50 MW coal-fired supercritical CO2 boiler

    • 摘要: 实现煤炭的高效、清洁利用是燃煤发电领域长期以来最为关心的课题之一,持续提升发电效率、降低碳排放是实现绿色低碳转型的重中之重。超临界二氧化碳(Sc-CO2)发电技术作为新兴的动力循环发电技术之一,其具有更高的理论发电效率,有望在未来燃煤发电机组效率提升和热力系统优化等方面发挥至关重要的作用。相较于传统蒸汽锅炉,Sc-CO2锅炉的工程设计经验相对缺乏,如何校核给定设计方案下烟气能否实现全温区高效换热、工质能否达到预期热力参数,已成为该领域技术突破的关键研究课题。因此,建立一套完整的Sc-CO2锅炉热力计算体系进而计算得到各受热面处烟气与工质的温度分布情况尤为重要。基于国内自主设计的世界首台50 MW的29.2 MPa/602 ℃/602 ℃ Sc-CO2锅炉箱式布置方案建立了Sc-CO2锅炉热力计算模型,使用Fortran 90与Python 3.11搭建了超临界二氧化碳热力计算平台,并通过该计算平台开展了热力计算工作,得到了各受热面进出口烟气与工质温度分布情况。根据热力性能分析,该设计方案下过热、再热CO2能够达到预期的热力参数,烟道设计合理,但省煤器处存在进出口温差过大的问题。此外,针对Sc-CO2锅炉与传统蒸汽锅炉的设计特征进行了对比分析。

       

      Abstract: Achieving highly-efficient and clean utilization of coal has long been a primary concern in coal-fired power generation. Continuously improving power generation efficiency and reducing carbon emissions are paramount to the green-oriented and low-carbon transition. As an emerging power cycle technology, supercritical carbon dioxide (Sc-CO2) power generation offers higher theoretical efficiency than conventional steam cycles and is expected to play a crucial role in enhancing future coal-fired unit efficiency and optimizing thermal systems. Compared to conventional steam boilers, Sc-CO2 boilers exhibit a significant lack of engineering design experience. The validation of whether flue gas achieves efficient heat transfer across the entire temperature range and whether the working fluid attains the targeted thermodynamic parameters under a given design scheme has emerged as a pivotal research challenge for technological breakthroughs in the field of Sc-CO2 boiler engineering. Therefore, establishing a complete Sc-CO2 boiler thermal calculation system to obtain the temperature distributions of flue gas and working fluid at each heating surface is particularly important. Based on the domestically developed world's first 50 MW, 29.2 MPa/602 ℃/602 ℃ Sc-CO2 boiler with a box-type configuration, a Sc-CO2 boiler thermal calculation model is established. A thermal calculation platform for supercritical carbon dioxide has been developed using Fortran 90 and Python 3.11, enabling thermal calculations to obtain flue gas and CO2 temperature distributions at each heating surface inlet and outlet. Based on the thermodynamic performance analysis, the current design successfully enables the superheated and reheated CO2 to achieve the targeted thermodynamic parameters, and the flue gas duct arrangement is considered sound. However, an issue of excessive temperature differential between the inlet and outlet of the economizer has been identified. A comparative analysis of the design characteristics between the Sc-CO2 boiler and conventional steam boilers is also provided.

       

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