Yi Xiawen, Zhang Meng, Song Weilong, Wang Xinhua
Jiangsu Key Laboratory of Anaerobic Biotechnology, School of Environmental and Civil Engineering, Jiangnan University, Wuxi 214122, China.
Membranes (Basel). 2021 Mar 13;11(3):203. doi: 10.3390/membranes11030203.
Anaerobic membrane bioreactors (AnMBRs) have aroused growing interest in wastewater treatment and energy recovery. However, serious membrane fouling remains a critical hindrance to AnMBRs. Here, a novel membrane fouling mitigation via optimizing initial water flux is proposed, and its feasibility was evaluated by comparing the membrane performance in AnMBRs between constant flux and varying flux modes. Results indicated that, compared with the constant flux mode, varying flux mode significantly prolonged the membrane operating time by mitigating membrane fouling. Through the analyses of fouled membranes under two operating modes, the mechanism of membrane fouling mitigation was revealed as follows: A low water flux was applied in stage 1 which slowed down the interaction between foulants and membrane surface, especially reduced the deposition of proteins on the membrane surface and formed a thin and loose fouling layer. Correspondingly, the interaction between foulants was weakened in the following stage 2 with a high water flux and, subsequently, the foulants absorbed on the membrane surface was further reduced. In addition, flux operating mode had no impact on the contaminant removal in an AnMBR. This study provides a new way of improving membrane performance in AnMBRs via a varying flux operating mode.
厌氧膜生物反应器(AnMBRs)在废水处理和能源回收方面引起了越来越多的关注。然而,严重的膜污染仍然是AnMBRs的关键障碍。在此,提出了一种通过优化初始水通量来减轻膜污染的新方法,并通过比较恒通量和变通量模式下AnMBRs的膜性能来评估其可行性。结果表明,与恒通量模式相比,变通量模式通过减轻膜污染显著延长了膜的运行时间。通过对两种运行模式下污染膜的分析,揭示了减轻膜污染的机制如下:在第一阶段采用低水通量,减缓了污染物与膜表面之间的相互作用,特别是减少了蛋白质在膜表面的沉积,并形成了一层薄而松散的污染层。相应地,在随后的第二阶段采用高水通量时,污染物之间的相互作用减弱,随后,吸附在膜表面的污染物进一步减少。此外,通量运行模式对AnMBR中的污染物去除没有影响。本研究提供了一种通过变通量运行模式提高AnMBRs膜性能的新方法。