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Wastewater treatment in a pilot-scale submerged membrane bioreactor: study of hydrodynamics under constant operating pressure

机译:试验型浸没膜生物反应器中的废水处理:在恒定工作压力下的流体动力学研究

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摘要

Abstract A pilot-scale Submerged Membrane Bioreactor provided with PEI hollow fiber membranes was operated under constant pressure mode in order to evaluate the effects of hydrodynamic conditions on the process performance, such as air flow rate, module packing density and aeration configuration. For the three different air flow rates studied (2, 5 and 8 L/min), results showed a limit value for this parameter, in which above this value a better performance will not be obtained and can even be worse. The air flow rate of 5 L/min presented the best performance, followed by 8 and 2 L/min. The module packing density was studied for two diameters (0.75 and 1 inch); the best result was observed for the larger diameter module, because lower packing density causes more space between fibers, increasing the aeration homogeneity inside de fiber bundle. Both aeration geometric tested showed similar permeate fluxes, indicating they did not affect the process performance. For all hydrodynamic conditions, the removal of TOC and COD was 96% and 93%, respectively.
机译:摘要在恒压模式下操作提供具有PEI中空纤维膜的先导型浸没膜生物反应器,以评估流体动力条件对过程性能的影响,例如空气流量,模块填充密度和通气配置。对于所研究的三种不同的空气流速(2,5和8L / min),结果显示了该参数的极限值,从而上面该值不会获得更好的性能,并且甚至可以更差。空气流速为5升/分,呈现最佳性能,其次是8和2L / min。研究了模块填充密度两径(0.75和1英寸);对于较大直径模块,观察到的最佳结果,因为较低的填充密度导致纤维之间的空间更多,增加了De纤维束内的曝气均匀性。曝气几何测试显示出类似的渗透助焊剂,表明它们不影响工艺性能。对于所有流体动力学条件,除去TOC和COD分别为96%和93%。

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