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Micromixing in a Rotor–Stator Spinning DiscReactor

机译:转子-定子纺丝盘中的微混合反应堆

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摘要

This paper presents the micromixing times in a rotor–stator spinning disc reactor. Segregation indices are obtained at different rotational speeds performing the Villermaux–Dushman parallel-competitive reaction scheme. Consequently, the corresponding micromixing times are calculated using the engulfment model, while considering the self-engulfment effect. It was found that the segregation index decreases with an increasing disc speed. Furthermore, for the investigated operational conditions, the estimated micromixing times are in the range of 1.13 × 10–4 to 8.76 × 10–3 seconds, in agreement with the theoretical dependency on the energy dissipation rate of ε–0.5. In a rotor–stator spinning disc reactor it is thus possible to further continue the theoretical trend of decreasing micromixing times with very high levels of energy dissipation rates that are unattainable in traditional types of process equipment.
机译:本文介绍了转子-定子旋转盘式反应器中的微混合时间。在执行Villermaux-Dushman平行竞争反应方案时,在不同转速下可获得偏析指数。因此,在考虑自吞噬效应的同时,使用吞噬模型计算了相应的微混合时间。已经发现,分离指数随着盘速度的增加而降低。此外,对于所研究的操作条件,估计的微混合时间在1.13×10 –4 到8.76×10 –3 秒的范围内,与理论依赖性一致ε –0.5 的能量耗散率因此,在转子-定子旋转盘式反应器中,可以进一步延续减少微混合时间的理论趋势,并具有很高的能量耗散率,这是传统类型的工艺设备无法实现的。

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