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Comparison of mixed liquor filterability measured with bench and pilot-scale membrane bioreactors

机译:用台式和中试规模的膜生物反应器测量的混合液可过滤性的比较

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Parallel experimental tests to measure mixed liquor filterability for submerged membrane bioreactors were conducted over a six month period using three ZW-500 pilot plants and a ZW-10 lab-scale filterability apparatus. Non-air sparged conditions during the tests yielded operation behaviour that was equivalent to dead-end filtration. The fouling resistance increased linearly with the intercepted mass until a critical point was reached at which point significant cake compression was induced and the resistance began to increase exponentially. Although the point of cake compression appears to be dependent on the membrane module design, similar resistance per unit solid mass intercepted per unit area (Rmass) values were observed when the same mixed liquor was filtered. Coupled with the established correlation between the Rmass and the critical flux, it is suggested that the filterability test results from a side-stream, lab-scale module may be used to predict fouling potential in a full scale MBR wastewater treatment system without interrupting the full-scale MBR operation.
机译:使用三个ZW-500中试装置和ZW-10实验室规模的可过滤性设备,在六个月的时间内进行了平行实验测试,以测量浸没式膜生物反应器的混合液可过滤性。在测试过程中,非空气鼓泡条件产生的操作行为相当于死角过滤。结垢阻力随截留的质量线性增加,直到达到临界点为止,在该临界点处,显着的滤饼压缩,并且阻力开始呈指数增长。尽管滤饼的压缩点似乎取决于膜组件的设计,但是当过滤相同的混合液时,观察到的单位体积截留的单位面积阻力(质量)相似。结合已建立的Rmass和临界通量之间的相关性,建议将侧流实验室规模模块的可过滤性测试结果用于预测全尺寸MBR废水处理系统中的结垢潜力,而不会中断整个规模的MBR操作。

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