Fouling behavior of poly(vinylidene fluoride) (PVDF) ultrafiltration membrane by polyvinyl alcohol (PVA) and chemical cleaning method
Separation Science and Engineering|Updated:2026-01-06
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Fouling behavior of poly(vinylidene fluoride) (PVDF) ultrafiltration membrane by polyvinyl alcohol (PVA) and chemical cleaning method
Chinese Journal of Chemical EngineeringVol. 28, Issue 12, Pages: 3018-3026(2020)
Affiliations:
State Key Laboratory of Materials-Oriented Chemical Engineering, National Engineering Research Center for Special Separation Membrane, Nanjing Tech University,Nanjing,China,211816
Weijie Ding, Min Chen, Ming Zhou, Zhaoxiang Zhong, Zhaoliang Cui, Weihong Xing. Fouling behavior of poly(vinylidene fluoride) (PVDF) ultrafiltration membrane by polyvinyl alcohol (PVA) and chemical cleaning method[J]. Chinese Journal of Chemical Engineering, 2020, 28(12): 3018-3026.
DOI:
Weijie Ding, Min Chen, Ming Zhou, Zhaoxiang Zhong, Zhaoliang Cui, Weihong Xing. Fouling behavior of poly(vinylidene fluoride) (PVDF) ultrafiltration membrane by polyvinyl alcohol (PVA) and chemical cleaning method[J]. Chinese Journal of Chemical Engineering, 2020, 28(12): 3018-3026.DOI: 10.1016/j.cjche.2020.05.032.
Fouling behavior of poly(vinylidene fluoride) (PVDF) ultrafiltration membrane by polyvinyl alcohol (PVA) and chemical cleaning method
Severe fouling to poly(vinylidene fluoride) (PVDF) membrane is usually caused as filtrating the papermaking wastewater in the ultrafiltration (UF) process. In the paper
fouling behavior and mechanism were investigated
and the low-concentration polyvinyl alcohol (PVA) contained in the sedimentation tank wastewater was found as the main foulant. Consequently
the corresponding cleaning approach was proposed. The experiment and modeling results elaborated that the fouling mode developed from pore blockage to cake layer along with filtration time. Chemical cleaning conditions including the composition and concentration of reagents
cleaning duration and trans-membrane pressure were investigated for their effect on cleaning efficiency. Pure water flux was recovered by over 95% after cleaning the PVDF membrane using the optimal conditions 0.5 wt% NaClO (as oxidant) and 0.1 wt% sodium dodecyl benzene sulfonate (SDBS
as surfactant) at 0.04 MPa for 100 min. In the chemical cleaning method
hypochlorite (ClO
-
) could first chain-scissor PVA macromolecules to small molecules and SDBS could wrap the fragments in micelles
so that the foulants were removed
from the pores and surface of membrane. After eight cycling tests
pure water flux recovery maintained above 95% and the reused membrane was found intact without defects.
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