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应用电导探针测定固-液两相流的局部速度 总被引:2,自引:0,他引:2
研制了用于测定固-液两相流液相局部速度的双电极电导探针,并在0.75m×0.75m×1m方形固-液搅拌槽内测定了叶轮排出流区的速度分布。 相似文献
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Solid-liquid suspension in an agitated tank with a draft tube was investigated witha newly developed infrared turbidimeter for measuring solid concentration.The diameter of theflared inlet transition tube and the distance from the inlet to the tank bottom are two importantparameters for draft tube design The NAX-4 impeller,developed in this study,is characterized byits high flow efficiency and low power consumption.Some modifications are made to the Bald′smodel by considering the effects of solid concentration and fluid viscosity on the critical speed forcomplete off-bottom suspension.The modified equation fits the experimental data satisfactority andcan be used in scale-up design 相似文献
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利用k -ε湍流模型预测了搅拌槽在不同操作条件下宏观速度场 ,模型成功预测了搅拌槽内速度分布 ,计算结果与实验结果吻合较好 .模型预测结果表明 ,搅拌槽内宏观流动场受搅拌桨槽径比影响较大 .对单层搅拌桨 -槽体系 ,挡板前后宏观流动场差别很大 ,在挡板以前区域 ,轴向流动较强 ,在整个r -z断面上形成一个整体循环 ;而在挡板后面区域 ,流体在桨叶安装位置高度附近转向轴心流动 ,槽体上半部区域形成二次循环区域 ,且二次循环区域内流体以向下流动为主 . 相似文献
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引 言在固液两相搅拌反应器中 ,固体颗粒的运动行为直接影响到固液两相流的流体力学及传质特性 ,因此 ,近年来对固液两相体系中颗粒的运动行为研究愈来愈受到重视 .对于流体机械混合操作 ,许多情况下流动均处于湍流区域 ,涉及到多相态时 ,问题变得更为复杂 .颗粒和湍流的相互作用 ,很久以来一直是人们研究的基本问题之一[1~ 3] ,对有固体颗粒存在下液相流体速度及湍流脉动变化规律 ,也是研究人员和工程技术人员关注的重点 .现有文献中用激光测量搅拌槽内固液两相流动的数据很少 ,仅Nouri[3] 测量了六直叶涡轮搅拌槽内固液两相速度分… 相似文献
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The radial and axial distribution of mean 1iquid velocity were measured by a.hot-filmanemometer at the impeller region in an aerated and stirred tank 0.287m in diameter.The tangentialjet model for impeller discharge flow used for single phase flow was modified to conform with thecharacteristics of gas-liquid flow.The radial and axial velocity profiles at the impeller region in thegas-liquid stirred tank were calculated by the model The results predicted by the model were in goodagreement with those obtained in experiment. 相似文献
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The minimum fluid velocity to maintain particles just suspended was deduced, and the theoretical analysis shows that the minimum velocity is influenced by the properties of the solid and liquid, not by the operational conditions. For justification, the local minimum velocity at the bottom of the tank was measured by a bi- electrode conductivity probe, in a square-sectioned stirred tank (0.75 m×0.75m×1.0m) with the glass beads-water system. The experiments showed that the fluid velocities for the same suspension state were identical despite that the power dissipated per unit mass was not the same under different configuration and operation. Both theoretical analysis and experimental results indicate that the off-bottom suspension is controlled by the local fluid flow over the bottom of the stirred tank. 相似文献