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Optimisation of a torus reactor geometry usingCFD

机译:使用CFD优化环面反应堆的几何形状

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Different configurations of torus reactors were investigated, batch (close geometry) andcontinuous (open geometry) operating modes, different reactor geometries (square andcircular sectioned) and, a scale-up of the reactor was finally conducted (100 to 300ml).The torus reactor was simulated using the commercial code Fluent? (Fluent Inc.). Inbatch conditions, a linear evolution of the mean circulation velocities with respect to theimpeller rotation speed was obtained. A circular-sectioned torus reactor of 100 ml wasnext tested to compare the performance with a square-sectioned one. Negligibledifferences were found due to the small volume of the reactor and the high turbulencegenerated inside it.A 300 ml square-sectioned reactor was also studied. This reactor seemed to be moreeffective than the 100 ml one because it allowed higher bulk velocities for sameimpeller rotation speed. Reynolds number and Reynolds mixing number were alsocalculated for the 300 ml reactor. A linear relation between those two numbers wasobtained. In continuous mode, only a slight difference in mixing times was observed forsmall values of impeller rotation speeds (200 rpm). For higher velocities of rotation,differences were found negligible.
机译:研究了环面反应堆的不同配置,批处理(紧密几何形状)和 连续(开放几何)运行模式,不同的反应堆几何形状(正方形和正方形) 最后,将反应器按比例放大(100至300毫升)。 使用商业代码Fluent?对环面反应器进行了仿真。 (Fluent Inc.)。在 批处理条件下,平均循环速度相对于 获得叶轮转速。 100毫升的圆截面环形反应器 接下来进行测试,以将其性能与方形截面的效果进行比较。微不足道 由于反应器体积小和湍流大,因此发现差异 里面产生的。 还研究了一个300毫升的方形反应器。这个反应堆似乎更多 比100毫升更有效,因为它允许更高的整体速度 叶轮转速。雷诺数和雷诺混合数也为 计算出的300毫升反应器。这两个数字之间的线性关系是 获得。在连续模式下,仅观察到混合时间的细微差异 叶轮转速(200 rpm)的值较小。对于更高的旋转速度, 发现差异可忽略不计。

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