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Banik A, Biswal SK, Bandyopadhyay TK. Predicting the optimum operating parameters and hydrodynamic behavior of rectangular sheet membrane using response surface methodology coupled with computational fluid dynamics. CHEMICAL PAPERS 2020. [DOI: 10.1007/s11696-020-01136-y] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 02/02/2023]
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Kim HY, Cho Y, Kang SW. Porous cellulose acetate membranes prepared by water pressure-assisted process for water-treatment. J IND ENG CHEM 2019. [DOI: 10.1016/j.jiec.2019.05.027] [Citation(s) in RCA: 15] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/26/2022]
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Jung KW, Kang SW. Effect of functional group ratio in PEBAX copolymer on propylene/propane separation for facilitated olefin transport membranes. Sci Rep 2019; 9:11454. [PMID: 31391519 PMCID: PMC6686014 DOI: 10.1038/s41598-019-47996-7] [Citation(s) in RCA: 8] [Impact Index Per Article: 1.6] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 01/07/2019] [Accepted: 07/25/2019] [Indexed: 11/21/2022] Open
Abstract
PEBAX-5513/AgBF4/Al(NO3)3 membranes were fabricated for mixed olefin/paraffin separation. In order to improve the selectivity of the membranes utilizing PEBAX-1657, PEBAX-5513, which increased the ratio of amide groups from 40% to 60% in the copolymer, was used. The selectivity and permeance of the membranes were 7.7 and 11.1 GPU, respectively. Furthermore, the PEBAX–5513/AgBF4/Al(NO3)3 membranes had long-term stability because of Al(NO3) to have the stabilizing effect on Ag+ ions acting as an olefin carrier. Unexpectedly, the performance of the membrane selectivity was not improved, and the permeance became rather lower. Generally, when Ag+ ions was added to the polymer containing amide groups, the selectivity increased with the content of the amide groups. However, Al(NO3)3 was added for the stability of Ag+ ions and there was no increase in selectivity. Since the ratio of amide was high, Ag+ ions were favorably in coordination with the oxygen of the carbonyl group, but the NO3− ions in Al(NO3)3 had the enhanced interaction with Ag+ ions as obstacles for olefin complexation. Therefore, the composition ratio of amide/ether in the polymer matrix was negligible for olefin separation.
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Affiliation(s)
- Kyoung Won Jung
- Department of Chemistry, Sangmyung University, Seoul, 03016, Republic of Korea
| | - Sang Wook Kang
- Department of Chemistry, Sangmyung University, Seoul, 03016, Republic of Korea. .,Department of Chemistry and Energy Engineering, Sangmyung University, Seoul, 03016, Republic of Korea.
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Sun Z, Wu Q, Ye C, Wang W, Zheng L, Dong F, Yi Z, Xue L, Gao C. Nanovoid Membranes Embedded with Hollow Zwitterionic Nanocapsules for a Superior Desalination Performance. NANO LETTERS 2019; 19:2953-2959. [PMID: 30969778 DOI: 10.1021/acs.nanolett.9b00060] [Citation(s) in RCA: 22] [Impact Index Per Article: 4.4] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/05/2023]
Abstract
In order to lower the capital and operational cost of desalination and wastewater treatment processes, nanofiltration (NF) membranes need to have a high water permeation and ionic rejection, while also maintaining a stable performance through antifouling resistance. Recently, Turing-type reaction conditions [ Science 2018, 360, 518-521] and sacrificed metal organic frame (MOF) nanoparticles [ Nat. Commun. 2018, 9, 2004] have been reported to introduce nanovoids into thin-film composite (TFC) polyamide (PA) NF membranes for an improved performance. Herein, we report a one-step fabrication of thin-film nanocomposite membranes (TFNM) with controllable nanovoids in the polyamide layer by introducing hollow zwitterionic nanocapsules (HZNCs) during interfacial polymerization. It was found that embedding HZNCs increases the membrane internal free volume, external surface area, and hydrophilicity, thus enhancing the water permeation and antifouling resistance without trading off the rejection of multivalent ions. For example, water permeation of the NF membranes embedded with about 19.0 wt % of HZNCs (73 L m-2 h-1) increased by 70% relative to the value of the control TFC NF membrane without HZNCs (43 L m-2 h-1). This increase comes while also maintaining 95% rejection of Na2SO4. Further, we also determined the effect of the mass loading of HZNCs on the top surface of the TFC NF membranes on the membrane performance. This work provided a direct and simple route to fabricate advanced desalination membranes with a superior separation performance.
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Affiliation(s)
- Zhijuan Sun
- Center for Membrane Separation and Water Science & Technology, Ocean College , Zhejiang University of Technology , Hangzhou , Zhejiang 310014 , China
| | - Qian Wu
- Center for Membrane Separation and Water Science & Technology, Ocean College , Zhejiang University of Technology , Hangzhou , Zhejiang 310014 , China
| | - Changhuai Ye
- College of Materials Science and Engineering , Donghua University , Shanghai 201620 , China
| | - Wei Wang
- Center for Membrane Separation and Water Science & Technology, Ocean College , Zhejiang University of Technology , Hangzhou , Zhejiang 310014 , China
| | - Liuchun Zheng
- Key Laboratory of Engineering Plastics , Institute of Chemistry, Chinese Academy of Sciences (ICCAS) , Beijing 100190 , China
| | - Fengkai Dong
- Center for Membrane Separation and Water Science & Technology, Ocean College , Zhejiang University of Technology , Hangzhou , Zhejiang 310014 , China
| | - Zhuan Yi
- Center for Membrane Separation and Water Science & Technology, Ocean College , Zhejiang University of Technology , Hangzhou , Zhejiang 310014 , China
| | - Lixin Xue
- Center for Membrane Separation and Water Science & Technology, Ocean College , Zhejiang University of Technology , Hangzhou , Zhejiang 310014 , China
| | - Congjie Gao
- Center for Membrane Separation and Water Science & Technology, Ocean College , Zhejiang University of Technology , Hangzhou , Zhejiang 310014 , China
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