Membrane fouling performance of Fe-based coagulation-ultrafiltration process: Effect of sedimentation time

2021 ◽  
Vol 195 ◽  
pp. 110756
Author(s):  
Yanyan Ding ◽  
Tong Li ◽  
Kaipei Qiu ◽  
Baiwen Ma ◽  
Ruijun Wu
RSC Advances ◽  
2019 ◽  
Vol 9 (27) ◽  
pp. 15277-15287
Author(s):  
Ming Yang ◽  
Jiabin Chen ◽  
Boyu Peng ◽  
Zhenjiang Yu ◽  
Huaqiang Chu ◽  
...  

The removal effect of organics and the feasibility of membrane fouling mitigation with Fe(ii)/PS-PFS coupling technology.


2018 ◽  
Vol 4 (2) ◽  
pp. 315-324 ◽  
Author(s):  
Fangshu Qu ◽  
Zhongsen Yan ◽  
Hao Wang ◽  
Xiaobo Wang ◽  
Heng Liang ◽  
...  

For decentralized drinking water treatment in rural areas, a hybrid process of biological activated carbon (BAC) filtration and ultrafiltration (UF) was applied to obtain potable water.


2013 ◽  
Vol 67 (4) ◽  
Author(s):  
Katarzyna Staszak ◽  
Zofia Karaś ◽  
Karolina Jaworska

AbstractA comparison of polymeric and ceramic membranes in the ultrafiltration process was studied and presented. This study was conducted on the separation of cadmium(II) ions, with particular reference to parameters such as hydrodynamic permeability coefficient, membrane fouling, amount of surfactant in the permeate, efficiency, and effectiveness of the process. The effect of ionic (SDS) and non-ionic (Rofam 10) surfactants or their mixture was investigated. The hydrodynamic permeability coefficient of the ceramic membrane was found to be much lower in comparison to those of the polymeric ones (1.69 × 10−7 m3 h−1 m−2 Pa−1, 5.66 × 10−7 m3 h−1 m−2 Pa−1, and 9.26 × 10−7 m3 h−1 m−2 Pa−1 for ceramic, CA, and PVDF, respectively). However, filtration of the surfactants solutions did not cause permanent blocking of pores and the surface of the ceramic membrane in contrast to the polymeric ones. No significant differences in surfactants permeation through the membranes tested were observed. Concentration of the surfactant in the permeate was lower than 1 CMC for the Rofam 10 solution and exceeded the CMC by about 40 % for the SDS solution. Better separation properties of polymer membranes for the separation of cadmium(II) ions from micellar systems were identified.


RSC Advances ◽  
2016 ◽  
Vol 6 (55) ◽  
pp. 49469-49477 ◽  
Author(s):  
Xin Huang ◽  
Baoyu Gao ◽  
Shuang Zhao ◽  
Shenglei Sun ◽  
Qinyan Yue ◽  
...  

This study focused on the floc characteristics and membrane fouling of Al2(SO4)3 (AS), Fe2(SO4)3 (FS) and Ti(SO4)2 (TS) in a coagulation–ultrafiltration (C–UF) process.


2013 ◽  
Vol 51 (13-15) ◽  
pp. 2718-2725 ◽  
Author(s):  
Mike Dixon ◽  
Christian Staaks ◽  
Rolando Fabris ◽  
Vipasiri Vimonses ◽  
Christopher W.K. Chow ◽  
...  

2013 ◽  
Vol 14 (2) ◽  
pp. 196-204 ◽  
Author(s):  
Ping Xiao ◽  
Weijun Zhang ◽  
Feng Xiao ◽  
Zhe Bi ◽  
Dongsheng Wang

A fouling index (FI) was introduced as a novel approach to investigate natural organic matter (NOM) fouling behavior in a low pressure membrane ultrafiltration process. Humic acid (HA), bovine serum albumin (BSA) and sodium alginate (SA), were used in the experiments. According to FI values, fouling was caused by NOM in two steps: a fast fouling process followed by a slow one. FI of the fast stage (FIF) was much greater than that of the slow one (FIS), showing the initial interaction would play a significant role in the fouling process over a short time. The results of mass balance suggested that a small fraction of DOC was responsible for membrane fouling caused by adsorption. Furthermore, both hydrophobic interaction and electrostatic interaction between NOM and the membrane determined the fouling behavior. Only a portion of foulants was removed after hydraulic washing. The sequence of NOM causing irreversible fouling was BSA > HA > SA, and the sequence of irreversible fouling after alkaline cleaning was SA > BSA > HA. The variations of FI values were consistent with the results of mass balances and flux recovery, which confirmed the FI was a simple and effective tool to describe the membrane fouling process.


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