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Coupling CFD–DEM and microkinetic modeling of surface chemistry for the simulation of catalytic fluidized systems

机译:耦合CFD-DEM和表面化学微急性建模,用于催化流化系统模拟

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摘要

In this work, we propose numerical methodologies to combine detailed microkinetic modeling and Eulerian–Lagrangian methods for the multiscale simulation of fluidized bed reactors. In particular, we couple the hydrodynamics description by computational fluid dynamics and the discrete element method (CFD–DEM) with the detailed surface chemistry by means of microkinetic modeling. The governing equations for the gas phase are solved through a segregated approach. The mass and energy balances for each catalytic particle, instead, are integrated adopting both the coupled and the operator-splitting approaches. To reduce the computational burden associated with the microkinetic description of the surface chemistry, in situ adaptive tabulation (ISAT) is employed together with operator-splitting. The catalytic partial oxidation of methane and steam reforming on Rh are presented as a showcase to assess the capability of the methods. An accurate description of the gas and site species is achieved along with up to 4 times speed-up of the simulation, thanks to the combined effect of operator-splitting and ISAT. The proposed approach represents an important step for the first-principles based multiscale analysis of fluidized reactive systems.
机译:在这项工作中,我们提出了数值方法,以结合详细的微蓄电图和欧拉维拉格兰语方法,以实现流化床反应器的多尺度模拟。特别地,我们通过微酮造型通过计算流体动力学和离散元件(CFD-DEM)将流体动力学描述耦合。通过隔离方法解决气相的控制方程。每个催化颗粒的质量和能量平衡,相结合采用耦合和操作者分裂方法。为了减少与表面化学的微急性描述相关的计算负担,原位自适应标签(ISAT)与操作员分裂一起使用。甲烷和RH上蒸汽重整的催化部分氧化作为展示,以评估方法的能力。由于操作员分裂和ISAT的综合效果,实现了气体和现场物种的准确描述。所提出的方法代表了流化反应性系统的第一原理的多尺度分析的重要步骤。

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