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Hydrodynamics of Gas-Liquid Bubble Columns and Air-Lift Loop Reactors: Experiments and Numerical Simulations

机译:气液泡塔和气举环流反应器的流体力学:实验和数值模拟

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It is generally accepted that a key to improvements in the modeling of gas-liquid reactors is a realistic description of two-phase flow. One of the main unresolved problems is the modeling of turbulence in the continuous phase. In the majority of publications on numerical simulations of stationary two-phase flows, the standard k-epsilon model developed for single-phase flows has been used. The general applicability of this model to instationary two-phase flows is however disputed. In our last contribution on the ISCRE-15, we discussed the above question with the example of a locally aerated, flat bubble column. The results showed that it is possible to obtain a realistic dynamic solution with the k-epsilon turbulence model. It was however obvious that the general applicability of the 3D k-epsilon turbulence model to the dynamic simulation of bubbly flows needed further validation for a large spectrum of test cases of turbulent gas-liquid flows. A series of new test cases for symmetrically aerated, empty bubble column with different aspect ratios will be presented in this contribution. The comparison of detailed experiments and flow simulation results will be given. Another important unresolved problem is the modeling of the turbulence induced by the gas phase. In the test cases of locally aerated, flat bubble colums mentioned above, the gas phase occupied only a very small part of the reactor, and the influence of the bubble-induced turbulence could be fully neglected. In this contribution some new simulation results for air-lift loop reactors of different geometries will be presented. In this new test cases, the gas phase occupies the whole cross-section of the riser, so that the bubble-induced turbulence is of the same order of magnitude as the shear-induced one. The neglection of this effect in the model leads to very poor agreement between the simulation results and experiments. The most popular modifications of the standard k-epsilon model, which try to describe the influence of the rising gas bubbles on the turbulence in liquid phase will be discussed. Unfortunately, in some test cases, none of them can lead to a better agreement with experiments, so that further investigations in this area are necessary.
机译:人们普遍认为,改进气液反应器建模的关键是对两相流的真实描述。尚未解决的主要问题之一是连续相中湍流的建模。在有关固定两相流数值模拟的大多数出版物中,都使用了为单相流开发的标准k-ε模型。然而,该模型对平稳两相流的一般适用性存在争议。在我们对ISCRE-15的最新贡献中,我们以局部充气的扁平气泡柱为例讨论了上述问题。结果表明,利用kε湍流模型可以获得逼真的动态解。但是,很明显,对于大范围的湍流气液流测试案例,3Dk-ε湍流模型对气泡流动态模拟的普遍适用性需要进一步验证。此贡献将介绍一系列具有不同长宽比的对称充气,空气泡塔的新测试用例。将给出详细实验与流动模拟结果的比较。另一个重要的未解决问题是气相引起的湍流建模。在上面提到的局部充气的扁平气泡柱的测试案例中,气相仅占据了反应器的一小部分,气泡引起的湍流的影响可以完全忽略。在这一贡献中,将提出不同几何形状的气举式环流反应堆的一些新的模拟结果。在这个新的测试案例中,气相占据了立管的整个横截面,因此气泡引起的湍流与剪切引起的湍流处于相同数量级。在模型中忽略此效应会导致仿真结果与实验之间的一致性非常差。将讨论标准k-ε模型的最流行修改,这些修改试图描述上升的气泡对液相湍流的影响。不幸的是,在某些测试用例中,没有一个可以与实验更好地达成一致,因此有必要对该领域进行进一步的研究。

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