超临界/密相CO2输送管道动态水击实验

Dynamic water hammer experiment on supercritical/dense-phase CO2 transportation pipelines

  • 摘要:
    目的 超临界/密相CO2的密度较大,管道输送过程中因计划或事故关阀会引起瞬态水击。目前针对CO2管道水击的研究以模拟为主,缺乏水击规律的实验分析。
    方法 设计并搭建了长238 m、管径56 mm、设计压力20 MPa的超临界/密相CO2管道瞬态水击实验系统,开展15组瞬态水击实验,包括不同初始温度、压力、CO2流速及不同关阀时间工况,环道沿线布置有多个压力传感器,精确捕捉水击过程中的压力波动变化,分析超临界/密相CO2管道的水击响应规律。
    结果 在相同初始温度下,随着初始压力升高,管道内CO2密度增加,单位体积流体的动能更大,转化为压力能后导致更强烈的水击效应,水击压力增大,水击周期缩短。在相同初始压力下,随着初始温度升高,CO2的密度、黏度、声速下降,压缩性减弱,从而减弱了水击压力并延长了水击周期。关阀时间越短,水击压力越大,延长关阀时间可显著降低最大水击压力,是缓解水击压力的有效措施。在9 MPa、20 ℃工况下,关阀时间延长1 s,水击压力降低约30%。管道内CO2流速增加时,系统动能增大,尤其在超临界/密相CO2工况的高密度特性下,快速关阀引起的动能释放更剧烈,使得水击强度显著增加;但管道内CO2流速与关阀时间并不影响水击周期,水击周期主要受初始温度、压力控制。
    结论 在设计与运行管道系统时,需重点考虑水击超压风险,适当降低运行压力、升高运行温度以降低水击引起的瞬态压力冲击,同时应避免在高流速状态下进行快速启闭阀门操作。文章通过实验揭示了超临界/密相CO2管道关阀水击的响应特性及规律,为建立超临界CO2水击模型与CO2管道设计、防护提供了重要依据。

     

    Abstract:
    Objective Supercritical/dense-phase CO2 exhibits relatively high density. During pipeline transport, planned or accidental valve closures can induce transient water hammer. Current research on CO2 pipeline water hammer primarily relies on simulations, with limited experimental investigation into its governing dynamics.
    Methods A 238 m-long experimental setup for transient water hammer in a supercritical/dense-phase CO2 pipeline (56 mm diameter, 20 MPa design pressure) was designed and constructed. Fifteen groups of experiments were conducted at varying initial temperature, pressure, CO2 flow velocity, and valve closing time. Multiple pressure sensors positioned along the pipeline loop captured pressure fluctuations, enabling detailed analysis of water hammer behavior in supercritical/dense-phase CO2 pipelines.
    Results At a constant initial temperature, increasing the initial pressure raised CO2 density and fluid kinetic energy per unit volume. When converted to pressure energy, this intensified the water hammer effect, increasing pressure and shortening the cycle. At a constant initial pressure, higher initial temperature reduced CO2 density, viscosity, sound velocity, and compressibility, thereby weakening water hammer pressure and extending the cycle. Shorter valve closing time increased water hammer pressure, while prolonging closure significantly reduced peak pressure —under 9 MPa and 20 °C, a 1-second delay lowered pressure by about 30%. Increasing CO2 flow velocity raised system kinetic energy, and under supercritical/dense-phase CO2 conditions, rapid valve closure released this energy more intensely, amplifying water hammer intensity. However, flow velocity and valve closing time did not affect the water hammer cycle which was mainly governed by initial temperature and pressure.
    Conclusion When designing and operating pipeline systems, the risk of water hammer overpressure must be addressed. Reducing operating pressure and increasing temperature can mitigate transient pressure shocks caused by water hammer. Additionally, rapid valve operations under high flow velocity should be avoided. This study experimentally characterizes valve-closing water hammer behavior in supercritical/dense-phase CO2 pipelines, providing a critical foundation for developing water hammer models for supercritical CO2 pipelines and guiding CO2 pipeline design and protection.

     

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