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Fouling control of a ceramic microfiltration membrane for direct sewer mining by backwashing with ozonated water

机译:通过用臭氧水反冲洗来直接下水道开采的陶瓷微滤膜的结垢控制

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Backwashing using ozonated water was investigated to control fouling during direct sewer mining using a ceramic microfiltration (MF) membrane. Primarily treated municipal wastewater was filtered and backwashing was performed using RO filtered tap water in this study. Direct MF filtration in the dead-end filtration mode using the ceramic MF membrane resulted in fouling that could not be fully removed by conventional backwashing. A steady increase in transmembrane pressure (TMP) was observed after each filtration cycle and could be attributed mostly to cake formation. In contrast, backwashing using ozonated water for 2.5 min was effective at removing the fouling cake layer; thus, resulting in a stable TMP value after multiple filtration cycles. The effectiveness of ozonated water backwashing could be enhanced by extending the backwashing time. Indeed, the permeability of a heavily fouled membrane was fully restored after 3.5 min of ozonated water backwashing. Results reported here suggest that backwashing using ozonated water has the ability to remove most foulants deposited on the membrane surface and can be used for sewer mining, where severe cake formation occurs. (C) 2015 Elsevier B.V. All rights reserved.
机译:研究了使用臭氧化水的反冲洗,以控制使用陶瓷微滤(MF)膜直接下水道开采时的结垢。在此研究中,对经过初步处理的市政废水进行了过滤,并使用了RO过滤的自来水进行了反冲洗。使用陶瓷MF膜在死角过滤模式下直接MF过滤会导致结垢,而这种结垢无法通过传统的反冲洗方法完全清除。在每个过滤循环后观察到跨膜压力(TMP)稳定增加,这主要归因于滤饼的形成。相比之下,使用臭氧水反冲洗2.5分钟可有效去除污垢滤饼层。因此,经过多次过滤后,TMP值保持稳定。臭氧水反冲洗的有效性可以通过延长反冲洗时间来提高。实际上,经过3.5分钟的臭氧水反冲洗后,严重污染的膜的渗透性得以完全恢复。此处报道的结果表明,使用臭氧水进行的反冲洗具有去除沉积在膜表面的大部分污垢的能力,并且可用于下水道采矿,其中会形成严重的滤饼。 (C)2015 Elsevier B.V.保留所有权利。

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