Anti-fouling and highly permeable thin-film composite forward osmosis membranes based on the reactive polyvinylidene fluoride porous substrates
Currently, thin-film composite (TFC) forward osmosis (FO) membranes are widely developed for wastewater purification, although it is a pressing subject to further improve its permeability, selectivity, and fouling resistance. Here, the polyvinylidene fluoride (PVDF) membranes were modified with dopa...
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Published in | Colloids and surfaces. A, Physicochemical and engineering aspects Vol. 654; p. 130144 |
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Main Authors | , , , , , |
Format | Journal Article |
Language | English |
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Elsevier B.V
05.12.2022
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Abstract | Currently, thin-film composite (TFC) forward osmosis (FO) membranes are widely developed for wastewater purification, although it is a pressing subject to further improve its permeability, selectivity, and fouling resistance. Here, the polyvinylidene fluoride (PVDF) membranes were modified with dopamine (DA) and polyethyleneimine (PEI) via surface segregation during non-solvent induced phase separation (NIPS). And then some residual amine groups on the as-prepared PVDF/DA-PEI membranes participated in the reaction with 1,3,5-benzenetricarboxylic acid chloride (TMC) by interfacial polymerization (IP), forming the TFC FO membranes. Furthermore, they were co-deposited by tannic acid (TA) and taurine, engineering the tTFC FO membranes. The introduction of DA and PEI in the substrate enhances the selectivity of the membrane having a low specific reverse solute flux (Js/Jw), and the TA-taurine layer improves the anti-fouling of the surface. Especially, tTFC6 (6 represents the weight concentration of DA and PEI in the substrate) has an excellent performance has a large Jw of 42.10 ± 0.86 L m−2 h−1, a low Js/Jw of 0.06 ± 0.02 g/L, and a high flux recovery (FRR) of more than 90% using bovine serum albumin (BSA), sodium alginate (SA), and SiO2 nanoparticles as model contaminants. The results provide new insights into the preparation of highly permeable and anti-fouling FO membranes.
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AbstractList | Currently, thin-film composite (TFC) forward osmosis (FO) membranes are widely developed for wastewater purification, although it is a pressing subject to further improve its permeability, selectivity, and fouling resistance. Here, the polyvinylidene fluoride (PVDF) membranes were modified with dopamine (DA) and polyethyleneimine (PEI) via surface segregation during non-solvent induced phase separation (NIPS). And then some residual amine groups on the as-prepared PVDF/DA-PEI membranes participated in the reaction with 1,3,5-benzenetricarboxylic acid chloride (TMC) by interfacial polymerization (IP), forming the TFC FO membranes. Furthermore, they were co-deposited by tannic acid (TA) and taurine, engineering the tTFC FO membranes. The introduction of DA and PEI in the substrate enhances the selectivity of the membrane having a low specific reverse solute flux (Jₛ/Jw), and the TA-taurine layer improves the anti-fouling of the surface. Especially, tTFC6 (6 represents the weight concentration of DA and PEI in the substrate) has an excellent performance has a large Jw of 42.10 ± 0.86 L m⁻² h⁻¹, a low Jₛ/Jw of 0.06 ± 0.02 g/L, and a high flux recovery (FRR) of more than 90% using bovine serum albumin (BSA), sodium alginate (SA), and SiO₂ nanoparticles as model contaminants. The results provide new insights into the preparation of highly permeable and anti-fouling FO membranes. Currently, thin-film composite (TFC) forward osmosis (FO) membranes are widely developed for wastewater purification, although it is a pressing subject to further improve its permeability, selectivity, and fouling resistance. Here, the polyvinylidene fluoride (PVDF) membranes were modified with dopamine (DA) and polyethyleneimine (PEI) via surface segregation during non-solvent induced phase separation (NIPS). And then some residual amine groups on the as-prepared PVDF/DA-PEI membranes participated in the reaction with 1,3,5-benzenetricarboxylic acid chloride (TMC) by interfacial polymerization (IP), forming the TFC FO membranes. Furthermore, they were co-deposited by tannic acid (TA) and taurine, engineering the tTFC FO membranes. The introduction of DA and PEI in the substrate enhances the selectivity of the membrane having a low specific reverse solute flux (Js/Jw), and the TA-taurine layer improves the anti-fouling of the surface. Especially, tTFC6 (6 represents the weight concentration of DA and PEI in the substrate) has an excellent performance has a large Jw of 42.10 ± 0.86 L m−2 h−1, a low Js/Jw of 0.06 ± 0.02 g/L, and a high flux recovery (FRR) of more than 90% using bovine serum albumin (BSA), sodium alginate (SA), and SiO2 nanoparticles as model contaminants. The results provide new insights into the preparation of highly permeable and anti-fouling FO membranes. [Display omitted] |
ArticleNumber | 130144 |
Author | Li, Manman Yang, Yuling Zhu, Lijing Wang, Gang Zeng, Zhixiang Xue, Lixin |
Author_xml | – sequence: 1 givenname: Manman surname: Li fullname: Li, Manman organization: Center for Membrane Separation and Water Science & Technology, College of Chemical Engineering, Zhejiang University of Technology, Hangzhou 310014, Zhejiang, China – sequence: 2 givenname: Yuling surname: Yang fullname: Yang, Yuling organization: Key Laboratory of Marine Materials and Related Technologies, Zhejiang Key Laboratory of Marine Materials and Protective Technologies, Ningbo Institute of Materials Technology and Engineering, Chinese Academy of Sciences, Ningbo 315201, China – sequence: 3 givenname: Lijing surname: Zhu fullname: Zhu, Lijing email: zhulijing@nimte.ac.cn organization: Key Laboratory of Marine Materials and Related Technologies, Zhejiang Key Laboratory of Marine Materials and Protective Technologies, Ningbo Institute of Materials Technology and Engineering, Chinese Academy of Sciences, Ningbo 315201, China – sequence: 4 givenname: Gang surname: Wang fullname: Wang, Gang organization: Key Laboratory of Marine Materials and Related Technologies, Zhejiang Key Laboratory of Marine Materials and Protective Technologies, Ningbo Institute of Materials Technology and Engineering, Chinese Academy of Sciences, Ningbo 315201, China – sequence: 5 givenname: Zhixiang surname: Zeng fullname: Zeng, Zhixiang organization: Key Laboratory of Marine Materials and Related Technologies, Zhejiang Key Laboratory of Marine Materials and Protective Technologies, Ningbo Institute of Materials Technology and Engineering, Chinese Academy of Sciences, Ningbo 315201, China – sequence: 6 givenname: Lixin surname: Xue fullname: Xue, Lixin email: xuelx@zjut.edu.cn organization: Center for Membrane Separation and Water Science & Technology, College of Chemical Engineering, Zhejiang University of Technology, Hangzhou 310014, Zhejiang, China |
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SubjectTerms | Active substrates bovine serum albumin dopamine Forward osmosis Interfacial polymerization Mussel-inspired chemistry nanoparticles osmosis permeability polyethyleneimine polymerization separation sodium alginate solutes tannins Taurine thermoplastics trimesoyl chloride wastewater |
Title | Anti-fouling and highly permeable thin-film composite forward osmosis membranes based on the reactive polyvinylidene fluoride porous substrates |
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