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Direct numerical simulation of turbulent particle dispersion in an unbaffled stirred-tank reactor

机译:无挡板搅拌釜反应器中湍流颗粒分散的直接数值模拟

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Turbulent dispersion of inertial particles in a flat-bottom stirred-tank reactor equipped with an eight-blade Rushton impeller is investigated using accurate numerical techniques (Verzicco et at., 2004, Flow in an impeller-stirred tank using an immersed-boundary method. A.I.Ch.E. Journal, 50(6), 1109-1118.). Direct Numerical Simulation of the turbulent flow field in the vessel is obtained using a second-order finite-difference scheme coded in a cylindrical reference frame, and an immersed-boundary approach is used to simulate the motion of the impeller. The flow scales are resolved explicitly down to the Kolmogorov scale. To give a comprehensive picture of the turbulence structure in the vessel angle-resolved averages of turbulent kinetic energy, turbulent energy dissipation rate and Kolmogorov time-scales are evaluated in vertical planes aligned with the blade and mid-way between two blades. The dispersion of heavy particles of different diameter is then investigated by Lagrangian tracking. The particle-to-fluid mass loading ratio is low enough to assume one-way coupling momentum transfer between continuous and dispersed phase. Three sets of particles, characterized by different response time, are investigated and, for each set, two equal, randomly distributed swarms are initially released above and below the impeller, which is placed mid-way between top and bottom of the tank. Statistics calculated after 3 impeller revolutions are used to evaluate the evolution of particle dispersion in the flow and to quantify their preferential accumulation into specific regions of the tank. (c) 2005 Elsevier Ltd. All rights reserved.
机译:使用精确的数值技术研究了配备八叶片Rushton叶轮的平底搅拌釜反应器中惯性颗粒的湍流扩散(Verzicco等人,2004,使用浸入边界法在叶轮搅拌槽中的流动。 AICh.E. Journal,50(6),1109-1118。)。使用在圆柱参考框架中编码的二阶有限差分方案,获得了容器中湍流场的直接数值模拟,并采用了浸入边界方法来模拟叶轮的运动。流量比例显式降低到Kolmogorov比例。为了全面了解脉动结构在容器中的角动能平均值,在与叶片对齐的垂直平面中以及两个叶片之间的中间平面中评估了湍流能量耗散率和Kolmogorov时间尺度。然后通过拉格朗日跟踪研究不同直径的重颗粒的分散性。颗粒与流体的质量负载比很低,足以假设连续相和分散相之间存在单向耦合动量传递。研究了三组以不同的响应时间为特征的颗粒,对于每一组,最初在叶轮的上方和下方释放两个相等的,随机分布的群,叶轮位于叶轮顶部和底部之间的中间位置。叶轮旋转3圈后计算出的统计数据可用于评估流中颗粒分散的演变,并量化它们在储罐特定区域内的优先积累。 (c)2005 Elsevier Ltd.保留所有权利。

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