首页> 外文会议>WEFTEC 2011;Annual Water Environment Federation technical exhibition and conference >Aeration and Mixing in Loop Reactors Equipped With Fine Bubble Diffusers and Slow Speed Mixers: A Full Scale Study
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Aeration and Mixing in Loop Reactors Equipped With Fine Bubble Diffusers and Slow Speed Mixers: A Full Scale Study

机译:配备细气泡扩散器和慢速混合器的环流反应器中的曝气和混合:大规模研究

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摘要

Mixing and aeration characteristics obtained on three full scale loop reactors for 28rnconfigurations (different mixers’ location and rotation speed, air flow rates and diffuser grids’rnlocation) were analyzed. The propellers’ thrust was measured in situ. Observed values varyrnwith the tank geometry, the location of the mixers and the induced axial velocity. In situ thrustrnvalues are lower than the nominal ones obtained during shop tests, by 10 to 30 %. For thernnominal rotation speed of the propellers, observed thrust-to-power ratios are comprisedrnbetween 685 and 875 N kW~(-1). In agreement with previous results, an increase in the oxygenrntransfer rate with the axial velocity was observed, due to a partial neutralization of the spiralrnflows formed at the edge of the aerated zones. Aeration efficiency is not decreased, as thernadditional power consumption due to mixing is offset by the oxygen transfer enhancement.rnSAE values are comprised between 2.0 and 2.6 kg O2 kWh~(-1). Such on site results arernespecially important to be used as input and output data in CFD models.
机译:分析了三个全尺寸环流反应器在28rn配置下的混合和曝气特性(不同混合器的位置和转速,空气流速和扩散器格栅的位置)。螺旋桨的推力是就地测量的。观测值随储罐几何形状,混合器位置和感应轴向速度而变化。现场推力值比车间测试中获得的名义值低10%至30%。对于螺旋桨的名义转速,观察到的推力/功率比在685和875 N kW〜(-1)之间。与先前的结果一致,观察到氧气传输速率随轴向速度的增加,这是由于在充气区域边缘形成的螺旋流的部分中和作用所致。曝气效率并未降低,因为混合引起的额外功耗被氧气转移增强所抵消。rnSAE值介于2.0和2.6 kg O2 kWh〜(-1)之间。这种现场结果在CFD模型中用作输入和输出数据特别重要。

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