超临界/密相CO2输送管道动态水击实验

Dynamic Water Hammer Experiment in Supercritical/Dense-Phase CO₂ Transmission 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。目前缺乏CO2管道的水击实验研究。【方法】设计并搭建了长238m、管径56mm、设计压力20MPa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,分析超临界/密相CO2水击响应规律并验证水击理论模型和OLGA仿真模型。【结果】在相同初始温度下,初始压力升高显著增强水击压力幅值,并缩短水击周期。而在同一初始压力下,升高温度会降低CO2密度与声速,从而削弱水击压力幅值并延长水击周期。当管内CO2流速增加,关阀时间越短,高流速下系统能量更高,快速关阀引起的动能释放更剧烈,则会显著加剧水击强度,但CO2流速和关阀时间并不影响水击周期,水击周期主要受初始温压控制。在设计和运行管道系统时,需重点考虑水击超压风险,适当降低运行压力和升高运行温度以降低水击引起的瞬态压力冲击,同时避免在高流速状态下进行快速启闭阀门操作。【结论】本文通过系统实验揭示了超临界/密相CO2管道关阀水击的响应特性及影响规律,为建立超临界CO2水击模型和CO2管道设计与防护提供了重要依据。

     

    Abstract: Objective Due to its high density, supercritical/dense CO₂ may cause transient water hammer during pipeline transportation when valves are closed for planned or emergency shutdowns. Currently, there is a lack of experimental research on water hammer in CO₂ pipelines. Methods: A transient water hammer test system for supercritical/dense-phase CO₂ pipelines was designed and constructed, featuring a 238-meter length, 56-mm diameter, and a design pressure of 20 MPa. Fifteen transient water hammer experiments were conducted to analyze the response patterns of supercritical/dense-phase CO₂ water hammer and validate theoretical models and OLGA simulation models. 【Results】At identical initial temperatures, increased initial pressure significantly amplified water hammer pressure amplitude while shortening the water hammer cycle. Conversely, at the same initial pressure, elevated temperatures reduced CO₂ density and sound velocity, thereby diminishing water hammer pressure amplitude and prolonging the cycle. Increased CO₂ flow velocity within the pipe and shorter valve closure times result in higher system energy at high velocities. The more intense kinetic energy release caused by rapid valve closure significantly exacerbates water hammer intensity. However, CO₂ flow velocity and valve closure time do not affect the water hammer cycle, which is primarily controlled by initial temperature and pressure. When designing and operating pipeline systems, priority should be given to mitigating water hammer overpressure risks. Appropriately reducing operating pressure and increasing operating temperature can lessen transient pressure shocks caused by water hammer. Additionally, rapid valve opening or closing operations should be avoided during high flow rate conditions. Conclusion This study systematically investigates the response characteristics and influencing factors of valve-closing water hammer in supercritical/dense-phase CO₂ pipelines through experimental validation, providing crucial evidence for establishing supercritical CO₂ water hammer models and guiding CO₂ pipeline design and protection.

     

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