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A CFD-DEM study of single bubble formation in gas fluidization of spherical and non-spherical particles

机译:CFD-DEM研究球形和非球形颗粒气体流化过程中单个气泡的形成

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Bubble dynamics significantly affect the hydrodynamics of gas-solid fluidized bed since they influence the gas-solid mixing. In this study, simulations using CFD-DEM were carried out to characterize the bubble size and shape for a bubble formed at a single orifice in gas-solid fluidized bed. Impact of parameters such as jet velocity, orifice size and particle shape on bubble equivalent diameter and bubble aspect ratio were analysed and discussed. Bubble equivalent diameter was found to increase with increasing jet velocity, decreasing bed width to orifice width ratio, and particle shape deviating from spherical. The bubble shape illustrated by aspect ratio, was found to elongate more as it rise through the bed and then commence to expand horizontally after it was detached from the orifice. Aspect ratio was found to be closer to a circle for the bubble at higher jet velocity, lower orifice width to bed ratio and for non-spherical particles.
机译:气泡动力学显着影响气固流化床的流体动力学,因为它们影响气固混合。在这项研究中,使用CFD-DEM进行了模拟,以表征气固流化床中单个孔口处形成的气泡的气泡大小和形状。分析并讨论了射流速度,孔口尺寸和颗粒形状等参数对气泡当量直径和气泡长宽比的影响。发现气泡当量直径随着射流速度的增加,床宽度与孔口宽度的比率减小以及颗粒形状偏离球形而增加。发现以纵横比表示的气泡形状随着其穿过床层的上升而进一步伸长,然后在从孔中分离后开始水平膨胀。对于较高的喷射速度,较低的孔口宽度与床层比率以及非球形颗粒,发现气泡的长宽比接近圆形。

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