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Analyzing dominant particle-flow structures inside a bubbling fluidized bed using POD

机译:使用POD分析型液体化流化床内的主导颗粒流动结构

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The particle velocity field inside a bubbling fluidized bed exhibits strong unsteady flow patterns accompanied by intense meso-scale fluctuations induced by the motion of bubbles: state-of-the-art post-processing methodology, namely the proper orthogonal decomposition (POD), is applied to the fluctuating particle flow fields predicted by a two-fluid model of a bubbling bed to identify and analyze the dominant spatio-temporal patterns of the particle phase. Three-dimensional POD results indicate that the dominant particle fluctuating velocity patterns are principally aligned in the axial direction, corresponding to particle mixing by the bubble wakes, with significant laterally-directed fluctuating velocity vectors at the bed surface, corresponding to mixing caused by the bubbles bursting. The swirling strength criterion is also used to identify particle vortical motions.
机译:鼓泡流化床内的粒子速度场表现出强烈的不稳定流动模式,伴随着由气泡的运动引起的强烈的间隙波动:最先进的后处理方法,即适当的正交分解(POD)是施加到由冒泡床的双流体模型预测的波动颗粒流场,以识别和分析颗粒相的主要时空模式。三维POD结果表明,主导粒子波动速度图案主要在轴向上对准,对应于通过气泡唤醒的颗粒混合,在床面处具有显着的横向定向的波动速度矢量,对应于由气泡引起的混合破裂。旋转强度标准也用于识别粒子涡旋运动。

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