Biofouling in sugarcane juice refining by nanofiltration membrane: Fouling mechanism and cleaning

2020 ◽  
Vol 612 ◽  
pp. 118432 ◽  
Author(s):  
Yukun Li ◽  
Jianquan Luo ◽  
Yinhua Wan
Desalination ◽  
2005 ◽  
Vol 178 (1-3) ◽  
pp. 171-178 ◽  
Author(s):  
Zhi Wang ◽  
Yuanyuan Zhao ◽  
Jixiao Wang ◽  
Shichang Wang

Membranes ◽  
2019 ◽  
Vol 9 (2) ◽  
pp. 33 ◽  
Author(s):  
Kitae Park ◽  
Pooreum Kim ◽  
Hyoung Gun Kim ◽  
JiHoon Kim

In this paper, we investigated the membrane fouling mechanism according to the coagulant dosage in algal rich water using a ceramic membrane. The algae that were used in this experiment were Microcystis sp. of cyanobacteria, and the fouling mechanism was analyzed through irrigation and filtration resistance through a constant flow operation. The experimental results showed that the filtration resistance decreased as the coagulant dosage increased, but the irreversibility at above optimum coagulant dosage increased. Additionally, as the coagulant dosage increased, the resistance value due to cake and adsorption contamination decreased, and membrane fouling by adsorption was dominant in comparison with cake fouling and adsorption fouling. The specific cake resistance was decreased as the coagulant dosage increased. The characteristics of the cake layer according to the coagulant dosage were found to loosely form the cake layer by increasing micro-size algae as the coagulant dosage increased. The results of this experiment confirmed the membrane fouling mechanism according to coagulant dosage when the ceramic membrane filtered algal rich water.


Desalination ◽  
2014 ◽  
Vol 346 ◽  
pp. 46-53 ◽  
Author(s):  
Haicheng Guo ◽  
Lan Xiao ◽  
Shuili Yu ◽  
Haijun Yang ◽  
Jun Hu ◽  
...  

Author(s):  
Karl J. P. Smith ◽  
Joshua Winans ◽  
James McGrath

Ultrathin membranes will likely see great utility in future membrane-based separations, but key aspects of the performance of these membranes, especially when they are used to filter protein, remain poorly understood. In this work we perform protein filtrations using new nanoporous silicon nitride (NPN) membranes. Several concentrations of protein are filtered using dead end filtration in a benchtop centrifuge, and we track fouling based on the amount of filtrate passed over time. A modification of the classic fouling model that includes the effects of using a centrifuge and allow for the visualization of a transition between pore constriction and cake filtration demonstrate that for a range of protein concentrations, cake filtration supersedes pore constriction after ∼30 seconds at 690 g.


2010 ◽  
Vol 355 (1-2) ◽  
pp. 133-141 ◽  
Author(s):  
M.N. Abu Seman ◽  
M. Khayet ◽  
Z.I. Bin Ali ◽  
N. Hilal

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