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    两相流环境下小质量阻尼参数传热管的流体弹性不稳定性

    Fluid-Elastic Instability of Heat-Transfer Tubes with Small Mass Damping Parameters in Two-Phase Flow Environment

    • 摘要: 以与蒸汽发生器U型管段单跨传热管频率等效的小质量阻尼参数弹性管为研究对象,在空气-水两相流环境中模拟汽水工况,对不同含气率(10%~80%)下节径比为1.483、转角三角形排布的弹性管进行流致振动试验,研究了不同含气率下弹性管顺流向和横流向的流体弹性不稳定性,确定了临界流速预测用准静态模型中的流体弹性不稳定性常数。结果表明:含气率10%~70%下弹性管顺流向和横流向均出现流体弹性不稳定性,含气率80%下仅顺流向发生流体弹性失稳。含气率10%~30%下弹性管顺流向和横流向的临界流速相同;含气率40%~70%下横流向的临界流速均低于顺流向,横流向更易发生流体弹性不稳定性。随着含气率升高,弹性管顺流向和横流向的临界流速均呈先增后减再增的趋势,当含气率为50%~70%时临界流速最低,此时弹性管易发生流体弹性失稳,此区间工况为危险工况。采用准静态模型进行临界流速预测时,推荐危险工况(含气率50%~70%)下的流体弹性不稳定性常数取1.93,非危险工况(含气率10%~40%,80%)下取3.94。

       

      Abstract: An elastic tube with small mass-damping parameters and frequency equivalence to a single-span heat transfer tube in the U-bend section of a steam generator was taken as the research object. The steam-water working condition was simulated in an air-water two-phase flow environment, and flow-induced vibration tests were conducted on an elastic tube bundle with a pitch-to-diameter ratio of 1.483 arranged in a rotated triangular layout under different void fractions (10%–80%). The fluid-elastic instability in the in-flow and cross-flow directions of the elastic tube under different void fractions was investigated, and the fluid-elastic instability constant in the quasi-static model for critical flow velocity prediction was determined. The results show that fluid-elastic instability both occurred in the in-flow and cross-flow directions at void fractions of 10%–70%, and only the in-flow direction exhibited fluid-elastic instability at the void fraction of 80%. At void fractions of 10%–30%, the critical flow velocities in the in-flow and cross-flow directions were identical. At void fractions of 40%–70%, the critical flow velocity in the cross-flow direction was consistently lower than that in the in-flow direction, indicating that the cross-flow direction was more prone to fluidelastic instability. As the void fraction increased, the critical flow velocities in both the in-flow and cross-flow directions first increased, then decreased, and subsequently increased again. The lowest critical flow velocities were observed at void fractions of 50%–70%, where the elastic tube was most susceptible to fluid-elastic instability, identifying these conditions as hazardous. When the quasi-static model was used to predict the critical flow velocity, the fluid-elastic instability constant was recommended to be 1.93 for hazardous conditions (void fraction of 50%–70%) and 3.94 for non-hazardous conditions (void fraction of 10%–40% and 80%).

       

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