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Fluid hydrodynamics in submerged and sidestream membrane bioreactors

机译:淹没式和侧流式膜生物反应器中的流体动力学

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As with all membrane processes, turbulence, as promoted by aeration in submerged membrane bioreactors (MBRs) or pumping in sidestream (SS) systems to produce somewhat higher effective cross-flow velocities, increases mass transfer and reduces fouling. This is manifested in an elevated critical flux, the flux at which the membrane permeability is sustained. However, the non-Newtonian nature of the sludge makes precise rheological characterisation difficult. In this study, a calculation of the appropriate hydrodynamics parameters for a SS MBR configuration is presented. Optimisation of the aeration in a submerged MBR system has been attained by defining the minimum air velocity required for Taylor bubble formation. [References: 17]
机译:与所有的膜工艺一样,在深层膜生物反应器(MBR)中通气或在侧流(SS)系统中进行泵送以产生更高的有效错流速度会引起湍流,从而增加了传质并减少了结垢。这表现为临界通量升高,该通量维持了膜渗透性。但是,污泥的非牛顿性质使精确的流变学表征变得困难。在这项研究中,提出了针对SS MBR配置的适当流体力学参数的计算。通过定义泰勒气泡形成所需的最小空气速度,可以实现潜水式MBR系统中的曝气优化。 [参考:17]

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