4.7 Article

Mass transfer model based on the spatial superposition assumption for simulating the catalytic ozone decomposition in downer reactor

期刊

POWDER TECHNOLOGY
卷 428, 期 -, 页码 -

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ELSEVIER
DOI: 10.1016/j.powtec.2023.118792

关键词

Mass transfer model; Ozone decomposition; Downer reactor; Spatial superposition; Computational fluid dynamics (CFD)

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A mass transfer model based on spatial superposition assumption is proposed to reflect the effect of heterogeneous structure on downer mass transfer behavior. This model requires fewer concentration parameters compared to the multi-scale method and is in good agreement with experimental data. The presence of clusters significantly affects gas-solid mass transfer effectiveness, deteriorating the reaction rate. The simulation shows that mass transfer near the inlet region plays a dominant role, while along the flow direction, the influence of the reaction process gradually becomes stronger.
A mass transfer model based on the spatial superposition assumption is proposed in this work to better reflect the effect of heterogeneous structure on the mass transfer behavior of the downer. Attributing to the special assumption of this model, fewer concentration parameters are required compared with the classic multi-scale method, which largely saves the calculation consumption. The simulation results of this model also could be in good agreement with the experimental data. Additionally, the calculated mass transfer coefficients are in the range from 10-3 to 10-1, which are approximately three orders of magnitude lower than that of the homogeneous structure. It is proved that the existence of clusters would seriously affect the gas-solid mass transfer effectiveness, thereby deteriorating the reaction rate. By simulating the distribution of ozone concentration in the catalytic ozone decomposition, it can be found that the mass transfer near the inlet region plays the dominant role while along the flow direction, the influence of reaction process becomes stronger than that of the mass transfer process and gradually turns to control the whole decomposition process. These results indicate that the present model is useful and could be applied for the simulation of mass transfer process in other gas-solid fluidized systems with heterogeneous structures.

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