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方形容器内甲烷-空气泄爆数值模拟研究

Numerical simulation study on methane-air explosion venting in a square container

  • 摘要: 当前甲烷气体泄漏所导致的爆炸事故时有发生,泄爆作为常用爆炸抑制手段被广泛应用于工业领域,但泄爆过程极易发生外部二次爆炸现象,导致灾害效应增大。采用FLUENT数值模拟方法,构建方形容器内甲烷-空气混合气体泄爆模型,系统研究甲烷体积分数、泄爆开启压力和泄爆口直径等关键参数对外部火焰演化特征及压力传播规律的影响。结果表明:当甲烷体积分数为9.5%、泄爆开启压力为20 kPa、泄爆口直径为0.5 m时,外部火焰传播速度较高、前沿位移增大,外部二次爆炸响应最为显著。进一步分析外部二次爆炸压力传播特性发现,当甲烷体积分数偏离9.5%(化学计量比附近)、泄爆开启压力为20 kPa、泄爆口直径为0.5 m时,外部压力初始峰值更高、波动幅值更大,且持续时间较长。研究结果表明,合理匹配泄爆开启压力与泄爆口尺寸可有效抑制外部火焰传播及二次爆炸压力效应,可为甲烷泄爆条件优化与风险控制提供参考。

     

    Abstract: Frequent explosion accidents caused by methane gas leakage pose significant safety concerns. Explosion venting is widely used as an explosion suppression measure in industrial fields. However,external secondary explosions can easily occur during the venting process,which increases the hazard severity. To address this,a numerical simulation study using FLUENT was conducted to establish a methane-air mixture explosion venting model in a square container. The effects of key parameters, including methane concentration,vent burst pressure,and vent diameter,on external flame evolution characteristics and pressure propagation behavior were systematically investigated. The results show that at a methane concentration of 9. 5%,a vent burst pressure of 20 kPa,and a vent diameter of 0. 5 m,the external flame propagation speed is higher,the flame front displacement increases,and the external secondary explosion response is most pronounced. Further analysis of the external secondary explosion pressure propagation characteristics reveals that when the methane concentration deviates from the near-stoichiometric value of 9. 5%,with the same vent burst pressure (20 kPa) and vent diameter (0. 5 m),the initial peak external pressure is higher,the fluctuation amplitude is larger,and the pressure duration is longer. These findings indicate that a reasonable match between vent burst pressure and vent diameter can effectively suppress external flame propagation and mitigate the secondary explosion pressure effects,providing a reference for optimizing methane explosion venting conditions and risk control.

     

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