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隧道内氢气管道泄漏扩散规律及泄漏点定位模型

Dispersion law of hydrogen releases from pipelines in the tunnel and leakage point location model

  • 摘要:
    目的 隧道内的氢气长输管道发生泄漏会引起氢气积聚,从而带来燃爆风险。研究氢气在隧道内的泄漏扩散规律可为事故预防和处置提供依据,提高管输安全性。
    方法 以国内某氢气长输管道隧道穿越的设计参数为基础建立数值模型,使用FLUENT软件对泄漏孔径10.0、12.5 和15.0 mm三种事故工况进行了CFD(计算流体力学)模拟,研究了氢气在隧道内泄漏扩散过程和体积分数分布规律,建立了泄漏点定位模型。
    结果 泄漏发生后,氢气主要积聚在隧道顶部,体积分数在水平方向呈现高斯分布,在竖直方向呈现明显分层;随着时间推移,氢气向泄漏口下游扩散,部分滞留于已形成的氢气层中,导致层内体积分数升高。氢气泄漏之后在隧道内的体积分数分布规律具有自相似性,且独立于隧道空间尺寸及泄漏量。基于自相似性建立泄漏点定位数学模型,该模型适用于不同隧道尺寸和泄漏量(泄漏压力和孔径);模型可实现泄漏点定位(精度4.4%)及孔径估算(误差≤15%)。
    结论 隧道内氢气体积分数泄漏扩散分布规律的研究,能够为泄漏监测系统的优化和消氢装置的精准布设提供理论依据;所建泄漏点定位模型可预测事故发展,辅助应急处置。

     

    Abstract:
    Objective Hydrogen leakage in a long-distance pipeline within a tunnel can result in hydrogen accumulation, creating a potential hazard of ignition and explosion. Investigating the leakage and dispersion laws of hydrogen in tunnels offers critical insights into accident prevention and emergency response, contributing to improved safety in pipeline transport.
    Method A numerical model was established based on the design parameters of a hydrogen pipeline in China. Computational fluid dynamics simulations were carried out for three accident cases with leakage hole diameters of 10.0 mm, 12.5 mm and 15.0 mm using FLUENT software. The leakage and diffusion process and volume fraction distribution of hydrogen in the tunnel were studied. A leakage point location model was established.
    Result After the leakage, hydrogen mainly accumulated at the top of the tunnel. The volume fraction showed a Gaussian distribution in the horizontal direction and obvious stratification in the vertical direction. Over time, some of the hydrogen that had leaked moved downstream, while the rest stayed in the formed hydrogen layer, leading to a localized increase in hydrogen volume fraction. The volume fraction field of hydrogen in the tunnel after the leakage had a self-similarity that did not depend on the spatial size of the tunnel and the amount of leakage. Based on the self-similarity, a mathematical model of leakage point location was established, which could be applied to the working conditions of different tunnel sizes and leakage amounts (leakage pressure and hole diameter). The leakage point location and leakage aperture estimation were achievable through the model, with a positioning accuracy of up to 4.4% and an aperture estimation error of ≤15%.
    Conclusion The study of hydrogen leakage and dispersion in the tunnel can provide a basis for the layout of leakage monitoring and hydrogen depletion devices. The leakage point location model enables rapid prediction of accident scenario evolution and formulates disposal measures.

     

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