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A multi-scale approach for CFD calculations of gas-liquid flow within large size column equipped with structured packing

机译:装有规整填料的大型塔内气液流动CFD计算的多尺度方法

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摘要

This work has been carried out in the framework of post-combustion CO2 capture process development. Considering the huge amount of gases to be treated and the constraints in terms of pressure drop, it appears that the absorption column will be equipped with high efficiency high capacity packings such as structured packings. The present paper focuses on the CFD modellisation of the two-phase flow within this complex geometry. For limited computational resources reasons, it is presently impossible to run computations at large scales taking into account the gas-liquid interaction and the real geometry of the packing and original approaches must be developed. In the present work, a multi-scale approach is proposed. It first considers liquid-wall and liquid-gas interaction at small scale via two-phase flow calculations using the VOF method. Second, the latter results are used in three-dimensional calculations run at a meso-scale corresponding to a periodic element representative of the real packing geometry. Last, those results are further used at large scale in three-dimensional calculations with a geometry corresponding to a complete column. Results are compared with experimental data and with other CFD simulations in terms of liquid hold-up, pressure drop and unit operation. Some suggestions are made for further development. (C) 2007 Elsevier Ltd. All rights reserved.
机译:这项工作是在燃烧后二氧化碳捕集工艺开发的框架内进行的。考虑到要处理的大量气体以及压降方面的限制,看来吸收塔将配备高效高容量填料,例如规整填料。本文着重研究在这种复杂几何形状内的两相流的CFD建模。出于有限的计算资源的原因,考虑到气液相互作用以及填料的实际几何形状,必须开发原始方法,目前无法大规模进行计算。在目前的工作中,提出了一种多尺度方法。它首先使用VOF方法通过两相流计算来考虑小范围的液壁和液-气相互作用。第二,将后者的结果用于以中尺度进行的三维计算中,该尺度对应于代表实际堆积几何形状的周期性元素。最后,这些结果在几何计算对应于完整列的三维计算中进一步被大规模使用。将结果与实验数据以及其他CFD模拟的液体滞留量,压降和单元操作进行比较。为进一步发展提出了一些建议。 (C)2007 Elsevier Ltd.保留所有权利。

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