scholarly journals An Investigation of the Membrane Fouling Behaviors in Constant Flux Mode

Author(s):  
Shuang Yin ◽  
Peng Song ◽  
Yujie Chen ◽  
Xinpei Du ◽  
Xuguo Liu ◽  
...  
Membranes ◽  
2021 ◽  
Vol 11 (3) ◽  
pp. 203
Author(s):  
Xiawen Yi ◽  
Meng Zhang ◽  
Weilong Song ◽  
Xinhua Wang

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.


1987 ◽  
Vol 34 (2) ◽  
pp. 267-281 ◽  
Author(s):  
M. Turker ◽  
J. Hubble

2002 ◽  
Vol 2002 (7) ◽  
pp. 6-10 ◽  
Author(s):  
S. Ognier ◽  
C. Wisniewski ◽  
A. Grasmick

2016 ◽  
Vol 51 (2) ◽  
pp. 128-140 ◽  
Author(s):  
Dillon A. Waterman ◽  
Steven Walker ◽  
Bingjie Xu ◽  
Roberto M. Narbaitz

Currently, there is no standard bench-scale dead-end ultrafiltration (UF) testing system. The aim of the present study was to design and build a bench-scale hollow fiber UF system to assess the impact of operational parameters on membrane performance and fouling. A bench-scale hollow fiber UF system was built to operate at a constant flux (±2% of the set-point flux) and included automated backwash cycles. The development of the bench-scale system showed that it is very difficult to maintain a constant flux during the first minute of the filtration cycles, that digital flow meters are problematic, and that the volume of the backwash waste lines should be minimized. The system was evaluated with Ottawa River water, which has a relatively high hydrophobic natural organic matter content and is typical of Northern Canadian waters. The testing using different permeate fluxes, filtration cycle duration and backwash cycle duration showed that this system mimics the performance of larger systems and may be used to assess the impact of operating conditions on membrane fouling and alternative pretreatment options. Modeling the first, middle, and last filtration cycles of the six runs using single and dual blocking mechanisms yielded inconsistent results regarding the controlling fouling mechanisms.


2014 ◽  
Vol 454 ◽  
pp. 505-515 ◽  
Author(s):  
Daniel J. Miller ◽  
Sirirat Kasemset ◽  
Donald R. Paul ◽  
Benny D. Freeman

1987 ◽  
Vol 34 (3) ◽  
pp. 267-281 ◽  
Author(s):  
M. Turker ◽  
J. Hubble

2003 ◽  
Author(s):  
Christian Bernard Kuharik
Keyword(s):  

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