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超临界CO2管道瞬态数值仿真模型开发与停输工况分析

Development of a transient numerical simulation model and analysis of shutdown conditions for a supercritical CO2 pipeline

  • 摘要:
    目的 超临界CO2流体在管道瞬变过程中会发生相变,与天然气管道输送相比,存在更高的流动安全风险。因此,需要对超临界CO2管道瞬态过程进行精确模拟,以保障运行安全。
    方法 基于计算精度最高的GERG-2008方程,自主开发了物性计算模块,并建立了管道水热力瞬态数值仿真模型。通过该模块获取运行区间内离散温度、压力节点上的流体物性表,在仿真中用线性插值得到流体物性,相比于直接迭代调用物性计算模块,大幅提高了仿真速度。针对超临界CO2停输工况,改进了模型控制方程和边界条件:考虑了瞬变过程中的反向流动,对瞬态方程组的流速变量进行了处理;设置了更符合实际的停输后的传热边界条件,替代常用的等温边界条件。
    结果 基于停输工况对模型进行验证,与OLGA模拟结果相比,温度、压力误差分别不超过0.05%和0.80%。
    结论 该模型可用于停输工况下的水热力模拟和水击压力分析,是重要的流动安全分析工具,也可用于一般的压力、温度、流量波动的瞬变过程计算。自主开发的物性仿真模型和水热力仿真技术,可用于推动碳捕捉、利用与封存(carbon capture, utilization and storage, CCUS)项目发展以及智能化建设。

     

    Abstract:
    Objective Phase transitions of supercritical CO2 fluid may happen in the transient process of pipeline transportation, posing higher flow safety risks than those in natural gas pipelines. Therefore, it is essential to precisely simulate the transient process of supercritical CO2 pipelines to ensure operational safety.
    Method Utilizing the GERG-2008 equation, which currently offers the highest computational accuracy, a physical property calculation module was developed, and a pipeline thermohydraulic transient numerical simulation model was established. The physical property calculation module generated a fluid property table within the operating discrete temperature and pressure ranges. During the simulation, fluid properties were obtained through linear interpolation, which significantly enhanced simulation speed compared to directly invoking the physical property calculation module within the thermohydraulic simulation iteration process. For the shutdown conditions of a supercritical CO2 pipeline, the model governing equations and boundary conditions of the model were improved. Such as considering the potential for reverse flow during transient processes in the pipeline, the velocity variable in the transient equations was specifically adjusted. Additionally, more realistic post-shutdown heat transfer boundary conditions were set, replacing the commonly used isothermal boundary condition.
    Result The model was validated based on shutdown conditions, and compared with OLGA simulation results, the temperature and pressure errors were not more than 0.05% and 0.80%, respectively.
    Conclusion This model can be used for thermohydraulic simulations and water hammer pressure analysis under shutdown conditions, serving as an important tool for flow safety analysis. It can also be applied to calculations for general transient conditions involving fluctuations in pressure, temperature, and flow rate. The proposed physical property model and thermohydraulic simulation technology can contribute to the development and intelligent construction of carbon capture, utilization, and storage (CCUS) projects.

     

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