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Two-fluid simulation of liquid drainage in oscillating packed beds for offshore floating applications

机译:用于海上漂浮应用的振动填充床中液体排放的两流体模拟

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Three-dimensional modeling of liquid drainage dynamics in vertical, inclined and oscillating packed bed reactors is virtually inexistent in the literature. An attempt was made in this work where liquid drainage dynamics in vertical, inclined and oscillating packed bed reactors was analyzed via an unsteady-state three-dimensional two-fluid hydrodynamic model. Angular oscillations of the packed bed reactor between two angled symmetrical positions and between vertical and inclined position were considered while bed non-uniformity was described using radial porosity distributions. The simulation results highlighted the fully interpretable trends of the transient liquid flow in packed beds and underlined the differences in the transient behavior of the vertical, inclined and oscillating packed bed reactors. Although the initial period of liquid drainage was dominated by gravity regardless of bed configuration, the packed bed angle with respect to gravity direction had a significant impact on the liquid drainage dynamics. Cross-sections along streamwise direction both for static and oscillating inclined positions of the bed highlighted gas-rich uppermost and liquid-rich lowermost domains. Unlike vertical beds for which drainage occurred according to a quasi-plug flow of the liquid core region, drainage of inclined beds underlined 3D liquid flow structures with liquid-rich lowermost cross-sections which accelerated liquid withdrawal. Compared to the inclined bed case, liquid drainage was delayed under oscillating regimes as a result of reverse secondary flows induced by the column motion. The initial drainage process was controlled by the liquid flow in the bed lowermost part whereas oscillations between two symmetrically angled positions led to almost cross-sectionally uniform liquid drainage distribution. This is valuable and it is plausible that at long time the performance of packed bed reactors onboard offshore floating non stationary platforms is insignificantly affected by the oscillations between two symmetrically angled positions. (C) 2016 Elsevier Ltd. All rights reserved.
机译:垂直,倾斜和振荡填充床反应器中液体排泄动力学的三维模型在文献中几乎不存在。尝试通过非稳态三维二维流体动力学模型分析立式,倾斜和振荡填充床反应器中的液体排放动力学。考虑了填充床反应器在两个成角度的对称位置之间以及垂直和倾斜位置之间的角振荡,同时使用径向孔隙率分布描述了床的不均匀性。模拟结果突出了填充床中瞬态液体流动的完全可解释的趋势,并强调了垂直,倾斜和振荡填充床反应器的瞬态行为的差异。尽管无论床的配置如何,排液的初始阶段都由重力决定,但相对于重力方向的填充床角度对排液动力学有重大影响。床的静态和振荡倾斜位置沿流向的横截面突出显示了气体富集的最上方区域和液体富集的最下方区域。与根据液芯区域的准塞流而发生排水的垂直床不同,倾斜床的排水在3D液流结构下划线,这些液流结构具有最富液体的最低横截面,从而加速了液体的排出。与倾斜床相比,由于柱运动引起的反向二次流,在振荡状态下排液被延迟。最初的排水过程由床最下部的液体流控制,而两个对称角度位置之间的振荡导致横截面的排水分布几乎均匀。这是很有价值的,而且很可能在很长一段时间内,海上浮置非固定平台上的填充床反应堆的性能不受两个对称角度位置之间的振荡的影响很小。 (C)2016 Elsevier Ltd.保留所有权利。

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