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Study on a New type of Gas-Liquid Cyclone used in COIL

机译:用于线圈中使用的新型气液旋风的研究

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In order to separate the gas-liquid products from new ejector singlet oxygen generator (SOG) effectively, we designed a new type of gas-liquid cyclone. The classical Muschelknautz cyclone model method, the improved method and computational fluid dynamics (CFD) code's discrete phase model (DPM) and eddy diffusion concept (EDC) were used for the new type separator's calculation and simulation. The results show that: (1) Compared with classical Muschelnautz model, the improved Muschelknautz model can predict the cyclone's separation performance more accurately; (2) On the design conditions, the smaller droplets have more complex trajectories. For droplets larger than 3 urn, their separation efficiency is over 80% in the new separator; (3) The droplets' entrance locations affect the droplets' trajectories and separation efficiency, (4) The residence time which CFD predicts ranges from 1 to 50 ms and decreases with the droplets size increasing (5) The loss of O2(~1Δ) in the gas phase is less than 1% and it loses primarily on the gas-liquid contact reaction.
机译:为了有效地将气液产品与新的喷射器单线发电机(SOG)分开,我们设计了一种新型的气液旋风。古典的Muschelknautz旋风模型方法,改进的方法和计算流体动力学(CFD)代码的离散相位模型(DPM)和涡流扩散概念(EDC)用于新型分离器的计算和仿真。结果表明:(1)与古典Muschelnelnutz模型相比,改进的Muschelknautz模型可以更准确地预测旋风分离的分离性能; (2)在设计条件下,较小的液滴具有更复杂的轨迹。对于大于3 URN的液滴,它们的分离效率在新分离器中超过80%; (3)液滴的入口位置影响液滴轨迹和分离效率,(4)CFD预测的停留时间为1至50ms,并且随液滴尺寸的减小(5)丢失O2(〜1δ)在气相中小于1%,并且它主要损失在气液接触反应上。

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