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Experimental and CFD simulation investigations into fouling reduction by gas-liquid two-phase flow for submerged flat sheet membranes

机译:气液两相流对浸没式平板膜结垢减少的实验和CFD模拟研究

摘要

Submerged flat sheet membranes are mostly used in membrane bioreactors forwastewater treatment. The major problems for these modules are concentrationpolarization and subsequent fouling. By using gas-liquid two-phase flow, these problems can be ameliorated. This thesis aimed to optimize the use of gas-liquid two-phase flow as a cleaning mechanism for submerged flat sheet membrane. The effect of various hydrodynamic factors such as airflow rate, nozzle size, nozzle geometry, intermittent bubbling, intermittent filtration, channel gap width, feed concentration and membrane baffles were investigated for model feed materials (yeast suspensions and mixed liquor from activated sludge plants). Insights into mechanisms by which two-phase flow reducesfouling for submerged flat sheet membranes were obtained by using Computational FluidDynamics.Experiments conducted showed that an optimal airflow rate exists beyond which nofurther flux enhancement was achieved. Fouling reduction increased with nozzle size atconstant airflow. Nozzles of equal surface area but different geometries performeddifferently in terms of fouling reduction. Bubble size distribution analyses revealed thatthe percentage of larger bubbles and bubble rise velocities increased with the airflow rateand nozzle size. Thus the results of this study suggest that the effectiveness of two-phaseflow depends on the bubble size. CFD simulations revealed that average shear stress onthe membrane increased with airflow rate and bubble size and further indicated that anoptimal bubble size possible exists. Using intermittent filtration as an operating strategywas found to be more beneficial than continuous filtration. This study also showed theimportance of the size of the gap between the submerged flat sheet membranes.Increasing the gap from 7 mm to 14 mm resulted in an increase in fouling by about 40%based on the rate of increase in suction pressure (dTMP/dt).Finally, this is the first study which investigated the effect of baffles in improving airdistribution across a submerged flat sheet membrane. It was found that baffles decreasedthe rate of fouling at least by a factor of 3.0 based on the dTMP/dt data.
机译:浸没式平板膜主要用于膜生物反应器中以进行废水处理。这些模块的主要问题是浓差极化和随后的结垢。通过使用气液两相流,可以解决这些问题。本文旨在优化利用气液两相流作为浸没平板膜的清洁机制。对于模型进料(酵母菌悬浮液和活性污泥厂的混合液),研究了各种流体力学因素的影响,例如空气流速,喷嘴尺寸,喷嘴几何形状,间歇鼓泡,间歇过滤,通道间隙宽度,进料浓度和膜挡板。通过使用计算流体动力学获得了两相流减少浸没平板膜结垢的机理的见解。进行的实验表明,存在最佳气流速率,超过该气流速率则无法进一步提高通量。恒定的空气流量会随着喷嘴尺寸的增加而减少结垢。表面积相等但几何形状不同的喷嘴在减少结垢方面表现不同。气泡尺寸分布分析表明,较大气泡的百分比和气泡上升速度随气流速率和喷嘴尺寸的增加而增加。因此,这项研究的结果表明,两相流的有效性取决于气泡的大小。 CFD模拟显示,膜上的平均剪切应力随气流速率和气泡大小而增加,并进一步表明可能存在最佳气泡大小。发现使用间歇过滤作为操作策略比连续过滤更有益。这项研究还表明了浸没式平板膜之间间隙的大小的重要性,将间隙从7 mm增加到14 mm会导致污垢增加约40%(基于吸入压力的增加率(dTMP / dt最后,这是首次研究折流板在改善整个水下平板膜的空气分布方面的作用的研究。根据dTMP / dt数据,发现挡板至少使结垢率降低了3.0倍。

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