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CFD SIMULATION OF MULTIPHASE FLOW IN AN AIRLIFT COLUMN PHOTOBIOREACTOR FOR THE CULTIVATION OF MICROALGAE

机译:气浮柱光生物反应器中微相培养多相流的CFD模拟

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Due to their better operational advantages, such as good scalability, operational flexibility, high mass and heat transfer characteristics, homogenous shear stress, good mixing and better control over fluid circulation, airlift column photobioreactors (PBR) have become a promising design alternative for microalgae culture, among bubble column and other types of photobioreactors. The good hydrodynamic environment for fragile microorganisms in airlift columns have led to numerous investigations in order to understand the hydrodynamic phenomena of multiphase flow, particularly gas-liquid, inside this type of PBR.In the present paper, a CFD (Computer Fluid Dynamics) simulation in CFX, ANSYS Inc. 11.0, is developed following a multiphase flow model with an Eulerian-Eulerian approach. For evaluating turbulence, the modified k — e model is chosen. Gas holdup, gas superficial velocity and liquid velocity profiles for different heights column are obtained by varying air volumetric flow rates at 2, 5 and 8 L/min. Also gas holdup, gas superficial velocity and liquid velocity contours are obtained for a sequence of five step times. An experimental video validation to compare the multiphase flow behavior has been made with a high-resolution video camera. The experiments are carried out by using an airlift column photobioreactor with air supply by a porous sparger.The profiles of the hydrodynamic variables made for 5 different column heights show that the trends of gas holdup and gas superficial velocity are very similar and do not depend on the variation of inlet air flow. For the liquid velocity profiles, the trends don't show the same behavior, the profiles at lower heights are off-centered and less symmetric and the maximum velocities are reached at h=0.2 m.The time sequences with the variable contours are made to enhance the visualization and understanding of the hydrodynamic behavior, especially when air supply begins and the bubble plume starts to form.
机译:由于其更好的操作优势,例如良好的可扩展性,操作灵活性,高质量和传热特性,均一的剪切应力,良好的混合以及对流体循环的更好控制,气举柱光生物反应器(PBR)已成为微藻培养的有前途的设计替代方案,气泡柱和其他类型的光生物反应器之间。空中举升柱中易碎微生物的良好流体力学环境导致人们进行了大量研究,以了解这种PBR内部的多相流尤其是气液的流体动力学现象。在CFX中,ANSYS Inc. 11.0是根据具有Eulerian-Eulerian方法的多相流模型开发的。为了评估湍流,选择了改进的k_e模型。通过改变2、5和8 L / min的空气体积流量,可以获得不同高度塔的气体滞留率,气体表观速度和液体速度曲线。同样,对于五个步骤时间的序列,可以获得气体滞留量,气体表观速度和液体速度等值线。高分辨率视频摄像机已进行了实验视频验证,以比较多相流动行为。实验是通过使用气举柱光生物反应器并通过多孔喷雾器供气来进行的.5个不同柱高的流体动力学变量曲线表明,气体滞留率和气体表观速度的变化趋势非常相似,并且不依赖于进气流量的变化。对于液体速度剖面,趋势没有显示出相同的行为,较低高度处的剖面偏心且不对称,并且在h = 0.2 m时达到最大速度。增强对流体动力学行为的可视化和理解,尤其是当空气供应开始并且气泡羽流开始形成时。

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