闭式循环柴油机旋转碟片吸收器流动特性研究

    Research on Flow Characteristics of Rotating Disc Absorber for Closed Cycle Diesel Engines

    • 摘要: 为满足闭式循环柴油机(closed cycle diesel engine, CCDE)气体吸收器结构紧凑、传质效率高的要求,并解决吸收器微观流动特性与转速、流量之间关联关系不明确的问题,采用可视化试验与计算流体力学(computational fluid dynamics, CFD)数值模拟相结合的方法开展研究。结果表明:腔体内液相主要呈液线流与液滴流形态,沿渐开线方向延展;液滴脱离转盘后速度趋于稳定,其平均速度仅与转速呈正相关。基于流体体积(volume of fluid, VOF)函数模型与k-ω湍流模型建立的转盘区域CFD模型具有良好的可靠性,液滴速度计算值与试验值误差≤7%。转盘区域流型包括液膜、液线、液滴三种形式;随着转速/液量增大,碟片表面流型依次呈现“纯液膜流→液膜−液滴流→液膜−液线−液滴流”,且通过定量关系式确定了转变临界条件。转速升高会降低持液量与湿润面积,但增大液相比表面积;液量增大则仅显著提高持液量与湿润面积。其中,“液膜−液线−液滴”流型下液相分散效果最优,是强化气体吸收器性能的关键状态。

       

      Abstract: To meet the requirements of compactness and high mass transfer efficiency for the gas absorber of closed cycle diesel engine (CCDE), and address the issue of unclear correlation between the microflow characteristics of the absorber and rotating speed as well as liquid flow rate, visualization experiments and computational fluid dynamics (CFD) simulations were carried out in combination. The results show that the liquid phase in the cavity region is mainly composed of liquid line flow and droplet flow, extending along the involute, and the velocity of droplets remains stable after they fly off the rotating disc, with the average velocity being only positively correlated with the rotating speed. A CFD model of the disc region established based on the volume of fluid (VOF) model and k-ω turbulence model has good reliability, and the error between the calculated and experimental values of droplet velocity is ≤7%. The flow patterns in the disc region include three forms, i.e., liquid film, liquid line and droplet. With the increase of rotating speed/liquid flow rate, the upper surface presents a transition of “pure liquid film flow → liquid film−droplet flow → liquid film−liquid line−droplet flow”, and the transition critical conditions can be defined by quantitative relational expressions. An increase in rotating speed reduces the liquid holdup and wetted area but increases the specific surface area of the liquid, while an increase in liquid flow rate only significantly increases the liquid holdup and wetted area. Among them, the liquid phase dispersion is optimal under the “liquid film−liquid line−droplet” flow pattern, which is the key state for enhancing the performance of the gas absorber.

       

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