Pub Date : 2025-12-11DOI: 10.1016/j.memsci.2025.125054
Tingting Tang , Wenyi Zhang , Yucheng Liu , Xuewei Li , Kaibo Hu , Yinhua Wan , Jiuyang Lin
Yttrium (Y), the most abundant heavy rare earth element (HREE) in ion-adsorption type rare earth ores (IATREO), is essential for various innovative functional materials. This study employed hollow fiber renewal liquid membrane (HFRLM) technology combined with a novel phosphorus-containing extractant Cextrant322 (C322) to establish a C322-HFRLM system for the selective separation of Y3+ from Y-rich HREEs solution of IATREO. Under the optimized conditions of 0.5 mol L−1 C322, feed phase pH of 3, flow rate of 550 mL min−1, and stripping-to-feed volume ratio (VS/VF) of 1.6, the results demonstrated that the purity of Y3+ in the feed phase increased from 61.90 % to 97.69 % after a single-step simultaneous extraction-stripping process. The maximum separation factor (SF) values between Ho3+-Lu3+ and Y3+ (i.e., SFHo/Y, SFEr/Y, SFTm/Y, SFYb/Y, and SFLu/Y) were 1.32, 2.41, 5.71, 8.60, and 9.80 at 0.25-h operation, respectively. Compared with the traditional hollow fiber supported liquid membrane (HFSLM) system, the C322-HFRLM system achieved 1.29 times increase in Y3+ purity, demonstrating significantly enhanced separation efficiency and stability. Therefore, HFRLM presents substantial potential as an advanced membrane separation technology for the efficient industrial-scale separation and enrichment of Y3+.
{"title":"Highly selective separation of yttrium from heavy rare earth elements by hollow fiber renewal liquid membrane","authors":"Tingting Tang , Wenyi Zhang , Yucheng Liu , Xuewei Li , Kaibo Hu , Yinhua Wan , Jiuyang Lin","doi":"10.1016/j.memsci.2025.125054","DOIUrl":"10.1016/j.memsci.2025.125054","url":null,"abstract":"<div><div>Yttrium (Y), the most abundant heavy rare earth element (HREE) in ion-adsorption type rare earth ores (IATREO), is essential for various innovative functional materials. This study employed hollow fiber renewal liquid membrane (HFRLM) technology combined with a novel phosphorus-containing extractant Cextrant322 (C322) to establish a C322-HFRLM system for the selective separation of Y<sup>3+</sup> from Y-rich HREEs solution of IATREO. Under the optimized conditions of 0.5 mol L<sup>−1</sup> C322, feed phase pH of 3, flow rate of 550 mL min<sup>−1</sup>, and stripping-to-feed volume ratio (<em>V</em><sub>S</sub>/<em>V</em><sub>F</sub>) of 1.6, the results demonstrated that the purity of Y<sup>3+</sup> in the feed phase increased from 61.90 % to 97.69 % after a single-step simultaneous extraction-stripping process. The maximum separation factor (<em>SF</em>) values between Ho<sup>3+</sup>-Lu<sup>3+</sup> and Y<sup>3+</sup> (i.e., <em>SF</em><sub>Ho/Y</sub>, <em>SF</em><sub>Er/Y</sub>, <em>SF</em><sub>Tm/Y</sub>, <em>SF</em><sub>Yb/Y</sub>, and <em>SF</em><sub>Lu/Y</sub>) were 1.32, 2.41, 5.71, 8.60, and 9.80 at 0.25-h operation, respectively. Compared with the traditional hollow fiber supported liquid membrane (HFSLM) system, the C322-HFRLM system achieved 1.29 times increase in Y<sup>3+</sup> purity, demonstrating significantly enhanced separation efficiency and stability. Therefore, HFRLM presents substantial potential as an advanced membrane separation technology for the efficient industrial-scale separation and enrichment of Y<sup>3+</sup>.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125054"},"PeriodicalIF":9.0,"publicationDate":"2025-12-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734430","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-10DOI: 10.1016/j.memsci.2025.125050
Lei Huang , Xueting Zhao , Jinmao Lv , Xinliang Zhang , Zhihong Dong , Anqi Liu , Jiefeng Pan , Xiaocheng Lin
Controllable assembly of covalent organic framework (COF) nanosheets into two-dimensional (2D) layered membranes is crucial to prepare advanced membranes. However, the prevalence of disordered stacking of COF nanosheets often leads to tortuous or overlapped pores and sacrifices membrane permeability. Further, membrane stability is often questioned due to weak interlayer interactions. Herein, a three-dimensional (3D) polyphenol-mediated interlayer engineering strategy was proposed for manipulating the interlayer channels and interactions of COF membranes for simultaneous enhancement of membrane permeability and stability. The COF membranes (TTSBI/TFTA-TG(Cl)) were prepared via vacuum-assisted self-assembly method with TFTA-TG(Cl) COF nanosheets as the building host and 3D polyphenols 5,5′,6,6′-Tetrahydroxy-3,3,3′,3′-tetramethyl-1,1′-spirobiindane (TTSBI) as intercalating guests. The stereoscopic spirocyclic architecture of TTSBI provides rigid interlayer support to expand the 2D nanochannels within the COF membranes, which optimizes the water molecule transport pathway to enhance water permeance. The multiple interactions (e.g., electrostatic and cation-π interactions) between TTSBI and COF nanosheets strengthen the interlayer combination, thereby enhancing the structural stability of the COF membrane. The as-prepared TTSBI/TFTA-TG(Cl) membrane exhibited water permeance of 77.3 L m−2 h−1·bar−1 (approximately 2.5 times that of the pristine TFTA-TG(Cl) membrane) with methylene blue rejection above 91 %. Furthermore, the TTSBI/TFTA-TG(Cl) membrane can effectively reject dye molecules with molecular weight of ≥800 Da, and simultaneously demonstrate superior stability. This polyphenol-mediated interlayer engineering strategy may provide new insights into the construction and manipulation of the channels in COF membranes for high-permeability separation application.
{"title":"3D polyphenol-intercalated covalent organic framework membranes: Toward interlayer manipulation for high-permeability nanofiltration","authors":"Lei Huang , Xueting Zhao , Jinmao Lv , Xinliang Zhang , Zhihong Dong , Anqi Liu , Jiefeng Pan , Xiaocheng Lin","doi":"10.1016/j.memsci.2025.125050","DOIUrl":"10.1016/j.memsci.2025.125050","url":null,"abstract":"<div><div>Controllable assembly of covalent organic framework (COF) nanosheets into two-dimensional (2D) layered membranes is crucial to prepare advanced membranes. However, the prevalence of disordered stacking of COF nanosheets often leads to tortuous or overlapped pores and sacrifices membrane permeability. Further, membrane stability is often questioned due to weak interlayer interactions. Herein, a three-dimensional (3D) polyphenol-mediated interlayer engineering strategy was proposed for manipulating the interlayer channels and interactions of COF membranes for simultaneous enhancement of membrane permeability and stability. The COF membranes (TTSBI/TFTA-TG<sub>(Cl)</sub>) were prepared via vacuum-assisted self-assembly method with TFTA-TG<sub>(Cl)</sub> COF nanosheets as the building host and 3D polyphenols 5,5′,6,6′-Tetrahydroxy-3,3,3′,3′-tetramethyl-1,1′-spirobiindane (TTSBI) as intercalating guests. The stereoscopic spirocyclic architecture of TTSBI provides rigid interlayer support to expand the 2D nanochannels within the COF membranes, which optimizes the water molecule transport pathway to enhance water permeance. The multiple interactions (e.g., electrostatic and cation-π interactions) between TTSBI and COF nanosheets strengthen the interlayer combination, thereby enhancing the structural stability of the COF membrane. The as-prepared TTSBI/TFTA-TG<sub>(Cl)</sub> membrane exhibited water permeance of 77.3 L m<sup>−2</sup> h<sup>−1</sup>·bar<sup>−1</sup> (approximately 2.5 times that of the pristine TFTA-TG<sub>(Cl)</sub> membrane) with methylene blue rejection above 91 %. Furthermore, the TTSBI/TFTA-TG<sub>(Cl)</sub> membrane can effectively reject dye molecules with molecular weight of ≥800 Da, and simultaneously demonstrate superior stability. This polyphenol-mediated interlayer engineering strategy may provide new insights into the construction and manipulation of the channels in COF membranes for high-permeability separation application.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125050"},"PeriodicalIF":9.0,"publicationDate":"2025-12-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734326","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-09DOI: 10.1016/j.memsci.2025.125019
Jinmao Lv , Xueting Zhao , Lei Huang , Xuexi Zhang , Yu Sun , Jiefeng Pan , Xiaocheng Lin
Electrodialysis technology, an energy-efficient membrane separation technique, relies on the performance of its core component—ion exchange membranes (IEMs). However, anion exchange membranes (AEMs) still lag behind cation exchange membranes (CEMs, e.g., Nafion), primarily due to the trade-off between minimizing area resistance and maintaining dimensional stability. To tackle this issue, we leveraged 1-vinylimidazole (1-VIm) as a dual-functional agent by grafting it onto chloromethylated polysulfone (CMPSF) via N-alkylation and subsequently employing its vinyl group for in-situ self-polymerization to form the crosslinked structure. Results demonstrate that the 1-VIm self-crosslinked structure enables the coexistence of a high ion exchange capacity (IEC) for low area resistance and outstanding dimensional stability (suppressed swelling). The optimal VIPSF-3 membrane exhibits a swelling ratio of only 8.0 ± 0.5 % at 60 °C, while significantly enhancing membrane selectivity with an ion transport number () as high as 0.990 ± 0.002. During a 140-min electrodialysis desalination test, the optimized VIPSF-3 membrane outperformed the commercial AMV AEM by achieving a salt removal rate () of 90.5 ± 0.8 %, a current efficiency (η) of 98.3 ± 0.8 %, and an energy consumption (EC) of 4.04 ± 0.13 kWh·kg−1. These values surpass those of AMV ( = 82.4 ± 1.0 %, η = 88.3 ± 1.1 %, EC = 5.20 ± 0.17 kWh·kg−1). This study provides a novel strategy for preparing high-performance AEMs for electrodialysis applications.
{"title":"Preparation of polysulfone-based imidazole-functionalized self-crosslinked anion exchange membranes for electrodialysis","authors":"Jinmao Lv , Xueting Zhao , Lei Huang , Xuexi Zhang , Yu Sun , Jiefeng Pan , Xiaocheng Lin","doi":"10.1016/j.memsci.2025.125019","DOIUrl":"10.1016/j.memsci.2025.125019","url":null,"abstract":"<div><div>Electrodialysis technology, an energy-efficient membrane separation technique, relies on the performance of its core component—ion exchange membranes (IEMs). However, anion exchange membranes (AEMs) still lag behind cation exchange membranes (CEMs, e.g., Nafion), primarily due to the trade-off between minimizing area resistance and maintaining dimensional stability. To tackle this issue, we leveraged 1-vinylimidazole (1-VIm) as a dual-functional agent by grafting it onto chloromethylated polysulfone (CMPSF) via N-alkylation and subsequently employing its vinyl group for in-situ self-polymerization to form the crosslinked structure. Results demonstrate that the 1-VIm self-crosslinked structure enables the coexistence of a high ion exchange capacity (<em>IEC</em>) for low area resistance and outstanding dimensional stability (suppressed swelling). The optimal VIPSF-3 membrane exhibits a swelling ratio of only 8.0 ± 0.5 % at 60 °C, while significantly enhancing membrane selectivity with an ion transport number (<span><math><mrow><msub><mi>t</mi><mi>i</mi></msub></mrow></math></span>) as high as 0.990 ± 0.002. During a 140-min electrodialysis desalination test, the optimized VIPSF-3 membrane outperformed the commercial AMV AEM by achieving a salt removal rate (<span><math><mrow><msub><mi>R</mi><mrow><mi>s</mi><mi>a</mi><mi>l</mi><mi>t</mi></mrow></msub></mrow></math></span>) of 90.5 ± 0.8 %, a current efficiency (<em>η</em>) of 98.3 ± 0.8 %, and an energy consumption (<em>EC</em>) of 4.04 ± 0.13 kWh·kg<sup>−1</sup>. These values surpass those of AMV (<span><math><mrow><msub><mi>R</mi><mrow><mi>s</mi><mi>a</mi><mi>l</mi><mi>t</mi></mrow></msub></mrow></math></span> = 82.4 ± 1.0 %, <em>η</em> = 88.3 ± 1.1 %, <em>EC</em> = 5.20 ± 0.17 kWh·kg<sup>−1</sup>). This study provides a novel strategy for preparing high-performance AEMs for electrodialysis applications.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125019"},"PeriodicalIF":9.0,"publicationDate":"2025-12-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734434","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-09DOI: 10.1016/j.memsci.2025.125039
Daria Syrtsova , Alexandr Zinoviev , Alyona Wozniak , Maxim Bermeshev , Elena Skryleva , Roman Nikiforov , Mikhail Piskarev , Alexander Кuznetsov , Alexandr Alentiev , Alla Gilman , Victoria Ryzhikh
Low-temperature plasma treatment is demonstrated as an effective strategy to enhance the gas separation performance of a vinyl-addition polymer synthesized from the industrially available monomer 5-ethylidene-2-norbornene (APENB). The plasma modification introduces controlled surface and near-surface functionalities without compromising the bulk integrity of the polymer matrix. Structural and physicochemical analyses (XPS, FTIR, AFM) confirmed the incorporation of polar functional groups into the surface layer, resulting in a significantly improved permeability–selectivity balance. A systematic investigation of air plasma treatment conditions revealed the optimal parameters for enhancing gas transport performance. A 30-s plasma exposure was found to be optimal, yielding a more than twofold increase in O2/N2 selectivity and over a 20-fold enhancement in He/CH4 and H2/CH4 selectivity. Aging studies over a one-month period showed that the improved transport properties remained stable, with the H2/CH4 performance of treated polymer exceeding the 2015 Robeson upper bound. This work highlights the potential of plasma-based surface engineering to unlock advanced transport properties in commercially viable membrane materials for industrial gas separation.
{"title":"Advancing gas separation performance: Plasma-treated polymer from 5-ethylidene-2-norbornene beyond the Robeson upper bound","authors":"Daria Syrtsova , Alexandr Zinoviev , Alyona Wozniak , Maxim Bermeshev , Elena Skryleva , Roman Nikiforov , Mikhail Piskarev , Alexander Кuznetsov , Alexandr Alentiev , Alla Gilman , Victoria Ryzhikh","doi":"10.1016/j.memsci.2025.125039","DOIUrl":"10.1016/j.memsci.2025.125039","url":null,"abstract":"<div><div>Low-temperature plasma treatment is demonstrated as an effective strategy to enhance the gas separation performance of a vinyl-addition polymer synthesized from the industrially available monomer 5-ethylidene-2-norbornene (APENB). The plasma modification introduces controlled surface and near-surface functionalities without compromising the bulk integrity of the polymer matrix. Structural and physicochemical analyses (XPS, FTIR, AFM) confirmed the incorporation of polar functional groups into the surface layer, resulting in a significantly improved permeability–selectivity balance. A systematic investigation of air plasma treatment conditions revealed the optimal parameters for enhancing gas transport performance. A 30-s plasma exposure was found to be optimal, yielding a more than twofold increase in O<sub>2</sub>/N<sub>2</sub> selectivity and over a 20-fold enhancement in He/CH<sub>4</sub> and H<sub>2</sub>/CH<sub>4</sub> selectivity. Aging studies over a one-month period showed that the improved transport properties remained stable, with the H<sub>2</sub>/CH<sub>4</sub> performance of treated polymer exceeding the 2015 Robeson upper bound. This work highlights the potential of plasma-based surface engineering to unlock advanced transport properties in commercially viable membrane materials for industrial gas separation.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125039"},"PeriodicalIF":9.0,"publicationDate":"2025-12-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734432","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-09DOI: 10.1016/j.memsci.2025.125045
Zitong Huang , Kai wang , Ruofei Gao , Yi Cheng , Xinxin Li , Jinhua Ji , Xiaomeng Chu , Shaojie Liu , Nanwen Li
Ion-solvating membranes (ISMs) with high ionic conductivity and robust chemical stability are essential for high-performance alkaline water electrolysis (AWE). While naphthalene-based polybenzimidazoles (NPBI) demonstrate promising stability, their OH− conductivity remains limited due to insufficient electrolyte uptake and poorly organized ion transport pathways. To address this limitation, we developed a series of branched NPBI copolymers (NPBI-BM-x) through strategic incorporation of rigid tricarboxylic acid comonomers. This molecular design introduces rigid or articulated branching centers that disrupt chain packing and generate uniformly and continuously distributed ultra-micropores (0.54–0.58 nm), as confirmed by CO2 adsorption, XRD, and simulation. The tailored ultra-microporosity provide large free volume within the membrane, which significantly enhancing KOH absorption and facilitating rapid hydroxide transport. The optimized membrane NPBI-BM2-6 achieves a KOH uptake of 99.8 wt% and an OH− conductivity of 225 mS/cm at 80 °C in 6 M KOH which is 1.9 times higher than that of the linear NPBI. When integrated into an AWE cell with non-noble catalysts, the membrane enables a current density of 2.5 A/cm2 at 2.0 V and 80 °C (even achieved 3.58 A/cm2 90 °C) and voltage remained stable in a 685 h test. This branched ultra-microporous molecularly engineered architecture unlocks durable, high-performance alkaline water electrolysis.
离子溶剂化膜(ISMs)具有高离子电导率和强大的化学稳定性,是高性能碱性电解(AWE)的必要条件。虽然萘基多苯并咪唑(NPBI)表现出良好的稳定性,但由于电解质摄取不足和离子运输途径组织不良,它们的OH -电导率仍然有限。为了解决这一限制,我们通过战略性地加入刚性三羧酸共聚物,开发了一系列支链NPBI共聚物(NPBI- bm -x)。这种分子设计引入了刚性或铰接的分支中心,破坏了链式包装,产生了均匀连续分布的超微孔(0.54-0.58 nm),这一点得到了CO2吸附、XRD和模拟的证实。定制的超微孔提供了大的膜内自由体积,显著增强了KOH的吸收,促进了氢氧化物的快速运输。优化后的NPBI- bm2 -6膜的KOH吸收率为99.8 wt%,在80°C、6 M KOH条件下的OH -电导率为225 mS/cm,是线性NPBI膜的1.9倍。当与非贵金属催化剂集成到AWE电池中时,该膜在2.0 V和80°C时的电流密度为2.5 a /cm2(90°C时甚至达到3.58 a /cm2),并且在685小时的测试中电压保持稳定。这种分支的超微孔分子工程结构开启了持久、高性能的碱性电解。
{"title":"Ultra-microporosity enabled by the branched polybenzimidazole ion-solvating membranes for high performance alkaline water electrolysis","authors":"Zitong Huang , Kai wang , Ruofei Gao , Yi Cheng , Xinxin Li , Jinhua Ji , Xiaomeng Chu , Shaojie Liu , Nanwen Li","doi":"10.1016/j.memsci.2025.125045","DOIUrl":"10.1016/j.memsci.2025.125045","url":null,"abstract":"<div><div>Ion-solvating membranes (ISMs) with high ionic conductivity and robust chemical stability are essential for high-performance alkaline water electrolysis (AWE). While naphthalene-based polybenzimidazoles (NPBI) demonstrate promising stability, their OH<sup>−</sup> conductivity remains limited due to insufficient electrolyte uptake and poorly organized ion transport pathways. To address this limitation, we developed a series of branched NPBI copolymers (NPBI-BM-x) through strategic incorporation of rigid tricarboxylic acid comonomers. This molecular design introduces rigid or articulated branching centers that disrupt chain packing and generate uniformly and continuously distributed ultra-micropores (0.54–0.58 nm), as confirmed by CO<sub>2</sub> adsorption, XRD, and simulation. The tailored ultra-microporosity provide large free volume within the membrane, which significantly enhancing KOH absorption and facilitating rapid hydroxide transport. The optimized membrane NPBI-BM<sub>2</sub>-6 achieves a KOH uptake of 99.8 wt% and an OH<sup>−</sup> conductivity of 225 mS/cm at 80 °C in 6 M KOH which is 1.9 times higher than that of the linear NPBI. When integrated into an AWE cell with non-noble catalysts, the membrane enables a current density of 2.5 A/cm<sup>2</sup> at 2.0 V and 80 °C (even achieved 3.58 A/cm<sup>2</sup> 90 °C) and voltage remained stable in a 685 h test. This branched ultra-microporous molecularly engineered architecture unlocks durable, high-performance alkaline water electrolysis.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125045"},"PeriodicalIF":9.0,"publicationDate":"2025-12-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734436","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Mixed matrix membranes (MMMs) have emerged as a critical platform for molecular separation, especially carbon capture from point-emission sources. In this study, a series of novel MMMs were fabricated by incorporating the bimetallic Ag/Zn-ZIF-8 nanoparticles into the poly (ether-block-amide) (Pebax) matrix for efficient CO2/N2 separation. The SEM, EDS, XRD, FTIR, XPS, TGA, N2 adsorption-desorption measurements were employed to elucidate the microstructures and physicochemical properties of the resultant nanoparticles and membranes. The bimetallic coordination-induced optimization modulated the inherent structure of ZIF-8 framework and enhanced CO2 affinity, thereby forming the CO2-selective transport channels over N2. The incorporation of Ag + promoted the uniform dispersion of Ag/Zn-ZIF-8 nanoparticles in Pebax matrix, indicating the excellent polymer-filler interfacial compatibility. Impressively, the resulting membrane achieved the superior separation performance with a CO2 permeability of 359 Barrer and a CO2/N2 selectivity of 53, which were 2.5 and 1.4 times higher than that of the pristine Pebax membrane. Besides, the introduction of Ag/Zn-ZIF-8 nanoparticles enhanced the thermal and mechanical stability of the membrane, ensuring the potential for long-term operation. These findings herein advance the rational design and preparation of high-performance MMMs for sustainable carbon capture.
{"title":"Bimetallic engineering in Ag/Zn-ZIF-8/Pebax mixed matrix membranes for enhanced CO2 separation","authors":"Qian-Qian Li, Yang Li, Heng Mao, Yan-Mei Zhang, Qiu-Ying Zhang, Xin-Ru Chen, Zi-Cong Shan, Xian-Zhe Zhou, Li-Hao Xu, Zhi-Ping Zhao","doi":"10.1016/j.memsci.2025.125046","DOIUrl":"10.1016/j.memsci.2025.125046","url":null,"abstract":"<div><div>Mixed matrix membranes (MMMs) have emerged as a critical platform for molecular separation, especially carbon capture from point-emission sources. In this study, a series of novel MMMs were fabricated by incorporating the bimetallic Ag/Zn-ZIF-8 nanoparticles into the poly (ether-block-amide) (Pebax) matrix for efficient CO<sub>2</sub>/N<sub>2</sub> separation. The SEM, EDS, XRD, FTIR, XPS, TGA, N<sub>2</sub> adsorption-desorption measurements were employed to elucidate the microstructures and physicochemical properties of the resultant nanoparticles and membranes. The bimetallic coordination-induced optimization modulated the inherent structure of ZIF-8 framework and enhanced CO<sub>2</sub> affinity, thereby forming the CO<sub>2</sub>-selective transport channels over N<sub>2</sub>. The incorporation of Ag <sup>+</sup> promoted the uniform dispersion of Ag/Zn-ZIF-8 nanoparticles in Pebax matrix, indicating the excellent polymer-filler interfacial compatibility. Impressively, the resulting membrane achieved the superior separation performance with a CO<sub>2</sub> permeability of 359 Barrer and a CO<sub>2</sub>/N<sub>2</sub> selectivity of 53, which were 2.5 and 1.4 times higher than that of the pristine Pebax membrane. Besides, the introduction of Ag/Zn-ZIF-8 nanoparticles enhanced the thermal and mechanical stability of the membrane, ensuring the potential for long-term operation. These findings herein advance the rational design and preparation of high-performance MMMs for sustainable carbon capture.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125046"},"PeriodicalIF":9.0,"publicationDate":"2025-12-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734324","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-08DOI: 10.1016/j.memsci.2025.125044
Lei Yang , Yuning Feng , Yue Sun
The construction of highly efficient and selective solid-state nanochannels for chiral separation remains a formidable challenge. In this study, we developed a hybrid membrane by incorporating myoglobin (Mb) into the nanochannels of covalent organic frameworks (COFs) through in situ growth and subsequent biofunctionalization. The resulting Mb-COF composite membrane exhibited well-ordered nanochannels with exceptional chiral recognition capability. It achieved outstanding enantioselectivity (ee = 96.4 %) and high permeation flux (367 μmol m−2 h−1) toward S-ibuprofen (S-PRF), significantly surpassing the performance of unmodified COF membrane. The membrane also demonstrated remarkable stability and reproducibility under operational conditions. Furthermore, we provide mechanistic insights into the chiral transport process, highlighting the role of protein-substrate interactions within the confined nanochannels. This work not only offers a novel strategy for designing high-performance chiral separation membranes but also advances our understanding of enantioselective transport mechanisms in biomimetic environments. The Mb-COF platform holds great promise for applications in chiral drug purification and analytical chemistry.
{"title":"Integrating protein into covalent organic framework nanochannel membranes for highly enantioselective transport","authors":"Lei Yang , Yuning Feng , Yue Sun","doi":"10.1016/j.memsci.2025.125044","DOIUrl":"10.1016/j.memsci.2025.125044","url":null,"abstract":"<div><div>The construction of highly efficient and selective solid-state nanochannels for chiral separation remains a formidable challenge. In this study, we developed a hybrid membrane by incorporating myoglobin (Mb) into the nanochannels of covalent organic frameworks (COFs) through in situ growth and subsequent biofunctionalization. The resulting Mb-COF composite membrane exhibited well-ordered nanochannels with exceptional chiral recognition capability. It achieved outstanding enantioselectivity (ee = 96.4 %) and high permeation flux (367 μmol m<sup>−2</sup> h<sup>−1</sup>) toward S-ibuprofen (S-PRF), significantly surpassing the performance of unmodified COF membrane. The membrane also demonstrated remarkable stability and reproducibility under operational conditions. Furthermore, we provide mechanistic insights into the chiral transport process, highlighting the role of protein-substrate interactions within the confined nanochannels. This work not only offers a novel strategy for designing high-performance chiral separation membranes but also advances our understanding of enantioselective transport mechanisms in biomimetic environments. The Mb-COF platform holds great promise for applications in chiral drug purification and analytical chemistry.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125044"},"PeriodicalIF":9.0,"publicationDate":"2025-12-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734435","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-08DOI: 10.1016/j.memsci.2025.125047
Haleh Nourizadeh Kazerouni, Gabriel Toshiaki Tayama, Julie Fréchette, Younès Messaddeq
We present a novel freeform fabrication strategy for polymer membranes via 3D printing, in which porosity is generated through a polymerization-induced phase separation mechanism. The approach employs a vat-photopolymerization compatible formulation to produce a macroporous network with coexisting mesoporosity. Hydrophilic flat-sheet membranes (400 μm thick) were fabricated and subjected to post-treatments involving CO2 supercritical drying and solvent exchange. The resulting membranes exhibited permeance of up to 36 and 29 LMH.bar−1, respectively, under a transmembrane pressure of 2 bar. An in-depth evaluation was conducted on membranes produced from photocurable formulations containing methacrylic acid (MA, 30 vol%) and polyethylene glycol diacrylate (PEGDA, 20 vol%), with varying ratios of 1-butanol and 2-phenoxyethanol as porogens. SEM analysis revealed a porous morphology throughout the membrane cross-section. The top-performing sample exhibited the highest specific surface area of 12.8 m2/g and the smallest mean pore diameters of 45 nm and 42 nm, as determined by adsorption branches of Brunauer-Emmett-Teller (BET) and Barrett-Joyner-Halenda (BJH) analyses, respectively. Pore size distribution was compared with liquid-liquid displacement method, which revealed mean pore size of 8.8 nm, with a small quantity of pores of approximately 121 nm, which were in better agreement with pure water flux values. The influence of post-polymerization porogen removal methods—solvent exchange and supercritical drying—was also assessed. Post-treated membranes demonstrated lower compaction factors and more stable flux over time and under increasing pressure. This technique offers a promising route for the customized design of membrane geometries and architectures tailored to specific separation challenges. We further demonstrate such concept by printing textured membranes with wavy and rugged surface profiles.
{"title":"New approach to 3D-print methacrylic acid/polyethylene glycol diacrylate-based membranes based on polymerization induced phase separation","authors":"Haleh Nourizadeh Kazerouni, Gabriel Toshiaki Tayama, Julie Fréchette, Younès Messaddeq","doi":"10.1016/j.memsci.2025.125047","DOIUrl":"10.1016/j.memsci.2025.125047","url":null,"abstract":"<div><div>We present a novel freeform fabrication strategy for polymer membranes via 3D printing, in which porosity is generated through a polymerization-induced phase separation mechanism. The approach employs a vat-photopolymerization compatible formulation to produce a macroporous network with coexisting mesoporosity. Hydrophilic flat-sheet membranes (400 μm thick) were fabricated and subjected to post-treatments involving CO<sub>2</sub> supercritical drying and solvent exchange. The resulting membranes exhibited permeance of up to 36 and 29 LMH.bar<sup>−1</sup>, respectively, under a transmembrane pressure of 2 bar. An in-depth evaluation was conducted on membranes produced from photocurable formulations containing methacrylic acid (MA, 30 vol%) and polyethylene glycol diacrylate (PEGDA, 20 vol%), with varying ratios of 1-butanol and 2-phenoxyethanol as porogens. SEM analysis revealed a porous morphology throughout the membrane cross-section. The top-performing sample exhibited the highest specific surface area of 12.8 m<sup>2</sup>/g and the smallest mean pore diameters of 45 nm and 42 nm, as determined by adsorption branches of Brunauer-Emmett-Teller (BET) and Barrett-Joyner-Halenda (BJH) analyses, respectively. Pore size distribution was compared with liquid-liquid displacement method, which revealed mean pore size of 8.8 nm, with a small quantity of pores of approximately 121 nm, which were in better agreement with pure water flux values. The influence of post-polymerization porogen removal methods—solvent exchange and supercritical drying—was also assessed. Post-treated membranes demonstrated lower compaction factors and more stable flux over time and under increasing pressure. This technique offers a promising route for the customized design of membrane geometries and architectures tailored to specific separation challenges. We further demonstrate such concept by printing textured membranes with wavy and rugged surface profiles.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125047"},"PeriodicalIF":9.0,"publicationDate":"2025-12-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734503","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-08DOI: 10.1016/j.memsci.2025.125030
Jie Liu , Yingqing Zhan , Xinyue Duan , Jing Yang , Yuxing Han , Yajie Lei , Sihan Li , Hongyi Zhang
The polymeric membrane encounters huge challenge in dealing with high-viscosity oil pollutants and complicated membrane fouling issues. Herein, the multi-functional polymeric composite membrane (ZCP) is fabricated via anchoring bio-adhesive dopamine bridged gear-like CuS–ZnIn2S4 heterostructure onto PAN nanofiber support, which hits three birds with one stone. Firstly, the unique three-dimensional gear-like structure confers the ultra-low oil adhesion and high permeability to membrane by constructing underwater superoleophobicity (UWCA: up to 157.1° ± 1.6°) and providing efficient mass transfer channels, as confirmed by Molecular dynamics simulation and Hermia equation-fitted blocking models. The ZCP membrane demonstrates superior separation flux (3921.44 ± 196.1 L m−2 h−1) and separation efficiency (up to 99.53 %) for diverse oil-in-water emulsions. Besides, the ZCP membrane shows remarkable durability in harsh conditions and cyclic separation stability. Secondly, dopamine bridged CuS–ZnIn2S4 heterostructure mitigates charge recombination, strengthens electron transfer, and extends light absorption, which results in favorable photocatalytic self-cleaning via peroxymonosulfate (PMS) activation. Under simulated sunlight and low PMS input, the ZCP membrane exhibits high-efficiency catalytic degradation of organic pollutants within 60 min (97.9 % tetracycline and 100 % dye degradation rates) and effective self-cleaning for membrane regeneration (98.51 ± 2.4 % flux recovery rate). Moreover, the band structure, charge transfer, and mechanism of photocatalytic PMS activation are elucidated. Thirdly, owing to the photothermal conversion function of CuS–ZnIn2S4 heterostructure, the membrane surface temperature reaches 61.7 °C within 15 s, thus efficiently reducing oil viscosity and achieving 102.04 % enhancement in permeation flux during the simulated O/W separation application. This work opens a new avenue for treatment of complex emulsified oily wastewater and membrane fouling control.
{"title":"Dopamine-bridged CuS–ZnIn2S4/PAN nanofibrous membrane for purification of viscous emulsified oil pollutants with integrated oil resistance, photocatalytic self-cleaning, and photothermal conversion","authors":"Jie Liu , Yingqing Zhan , Xinyue Duan , Jing Yang , Yuxing Han , Yajie Lei , Sihan Li , Hongyi Zhang","doi":"10.1016/j.memsci.2025.125030","DOIUrl":"10.1016/j.memsci.2025.125030","url":null,"abstract":"<div><div>The polymeric membrane encounters huge challenge in dealing with high-viscosity oil pollutants and complicated membrane fouling issues. Herein, the multi-functional polymeric composite membrane (ZCP) is fabricated via anchoring bio-adhesive dopamine bridged gear-like CuS–ZnIn<sub>2</sub>S<sub>4</sub> heterostructure onto PAN nanofiber support, which hits three birds with one stone. Firstly, the unique three-dimensional gear-like structure confers the ultra-low oil adhesion and high permeability to membrane by constructing underwater superoleophobicity (UWCA: up to 157.1° ± 1.6°) and providing efficient mass transfer channels, as confirmed by Molecular dynamics simulation and Hermia equation-fitted blocking models. The ZCP membrane demonstrates superior separation flux (3921.44 ± 196.1 L m<sup>−2</sup> h<sup>−1</sup>) and separation efficiency (up to 99.53 %) for diverse oil-in-water emulsions. Besides, the ZCP membrane shows remarkable durability in harsh conditions and cyclic separation stability. Secondly, dopamine bridged CuS–ZnIn<sub>2</sub>S<sub>4</sub> heterostructure mitigates charge recombination, strengthens electron transfer, and extends light absorption, which results in favorable photocatalytic self-cleaning via peroxymonosulfate (PMS) activation. Under simulated sunlight and low PMS input, the ZCP membrane exhibits high-efficiency catalytic degradation of organic pollutants within 60 min (97.9 % tetracycline and 100 % dye degradation rates) and effective self-cleaning for membrane regeneration (98.51 ± 2.4 % flux recovery rate). Moreover, the band structure, charge transfer, and mechanism of photocatalytic PMS activation are elucidated. Thirdly, owing to the photothermal conversion function of CuS–ZnIn<sub>2</sub>S<sub>4</sub> heterostructure, the membrane surface temperature reaches 61.7 °C within 15 s, thus efficiently reducing oil viscosity and achieving 102.04 % enhancement in permeation flux during the simulated O/W separation application. This work opens a new avenue for treatment of complex emulsified oily wastewater and membrane fouling control.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125030"},"PeriodicalIF":9.0,"publicationDate":"2025-12-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734506","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-08DOI: 10.1016/j.memsci.2025.125043
Yangbo Qiu , Yidong Gao , Jingxiang Rockson Liu , Yuantian Cai , Ying Mei , Lei Xia , How Yong Ng , Yan Zhao , Bart Van der Bruggen , Chuyang Tang
Electro-driven membranes with monovalent ion selectivity represent a promising technology for sustainable lithium (Li) recovery from spent lithium-ion battery (LIB) leachate. However, existing membranes suffer from limited Li+ selectivity and low ion permeation rates. In this study, a zeolitic imidazolate framework (ZIF)-embedded hydrogel electro-driven membrane was developed for selective Li+ extraction via electrodialysis (ED). A poly(dimethyl diallyl ammonium chloride) (PDDA) network-threaded ZIF (QZIF) layer was in-situ constructed within the hydrogel matrix of Kevlar aramid nanofibers (KANFs), forming a stable composite layer on a sulfonated polysulfone (SPSF) substrate. Benefiting from the synergistic effects of size sieving and electrostatic repulsion, the resulting QZIF@KANF#SPSF membrane exhibited rapid Li+ transport while effectively rejecting larger divalent ions (Ni2+, Co2+, and Mn2+). During ED at 5 mA cm−2, the QZIF@KANF#SPSF membrane achieved a Li+ permeation rate of 0.45 mol m−2 h−1 in a 25 mM Li+, Ni2+, Co2+, and Mn2+ mixed solution, with high permselectivities of 13.8, 12.2, and 10.5 for Li+/Ni2+, Li+/Co2+, and Li+/Mn2+, respectively. This strategy of embedding charged ZIFs within a hydrogel matrix provides a robust and scalable pathway for enhancing Li+ selectivity and transport efficiency in advanced separation processes for spent LIB recycling.
具有单价离子选择性的电驱动膜是一种很有前途的从废锂离子电池(LIB)渗滤液中可持续回收锂(Li)的技术。然而,现有的膜存在Li+选择性有限和离子渗透率低的问题。在这项研究中,开发了一种沸石咪唑盐框架(ZIF)包埋的水凝胶电驱动膜,用于电渗析(ED)选择性提取Li+。在凯夫拉芳纶纳米纤维(KANFs)的水凝胶基质中原位构建了聚二甲基二烯丙基氯化铵(PDDA)网络螺纹ZIF (QZIF)层,在磺化聚砜(SPSF)衬底上形成了稳定的复合层。得益于粒径筛分和静电斥力的协同作用,所得QZIF@KANF#SPSF膜具有快速的Li+传输,同时有效地排斥较大的二价离子(Ni2+, Co2+和Mn2+)。在5 mA cm−2的放电条件下,QZIF@KANF#SPSF膜在25 mM Li+、Ni2+、Co2+和Mn2+混合溶液中Li+的渗透率为0.45 mol m−2 h−1,Li+/Ni2+、Li+/Co2+和Li+/Mn2+的渗透率分别为13.8、12.2和10.5。这种将带电荷的zif嵌入水凝胶基质的策略,为在废LIB回收的高级分离过程中提高Li+的选择性和传输效率提供了一种强大且可扩展的途径。
{"title":"In-situ construction of ZIF-embedded hydrogel electro-driven membranes for lithium selectivity","authors":"Yangbo Qiu , Yidong Gao , Jingxiang Rockson Liu , Yuantian Cai , Ying Mei , Lei Xia , How Yong Ng , Yan Zhao , Bart Van der Bruggen , Chuyang Tang","doi":"10.1016/j.memsci.2025.125043","DOIUrl":"10.1016/j.memsci.2025.125043","url":null,"abstract":"<div><div>Electro-driven membranes with monovalent ion selectivity represent a promising technology for sustainable lithium (Li) recovery from spent lithium-ion battery (LIB) leachate. However, existing membranes suffer from limited Li<sup>+</sup> selectivity and low ion permeation rates. In this study, a zeolitic imidazolate framework (ZIF)-embedded hydrogel electro-driven membrane was developed for selective Li<sup>+</sup> extraction via electrodialysis (ED). A poly(dimethyl diallyl ammonium chloride) (PDDA) network-threaded ZIF (QZIF) layer was <em>in-situ</em> constructed within the hydrogel matrix of Kevlar aramid nanofibers (KANFs), forming a stable composite layer on a sulfonated polysulfone (SPSF) substrate. Benefiting from the synergistic effects of size sieving and electrostatic repulsion, the resulting QZIF@KANF#SPSF membrane exhibited rapid Li<sup>+</sup> transport while effectively rejecting larger divalent ions (Ni<sup>2+</sup>, Co<sup>2+</sup>, and Mn<sup>2+</sup>). During ED at 5 mA cm<sup>−2</sup>, the QZIF@KANF#SPSF membrane achieved a Li<sup>+</sup> permeation rate of 0.45 mol m<sup>−2</sup> h<sup>−1</sup> in a 25 mM Li<sup>+</sup>, Ni<sup>2+</sup>, Co<sup>2+</sup>, and Mn<sup>2+</sup> mixed solution, with high permselectivities of 13.8, 12.2, and 10.5 for Li<sup>+</sup>/Ni<sup>2+</sup>, Li<sup>+</sup>/Co<sup>2+</sup>, and Li<sup>+</sup>/Mn<sup>2+</sup>, respectively. This strategy of embedding charged ZIFs within a hydrogel matrix provides a robust and scalable pathway for enhancing Li<sup>+</sup> selectivity and transport efficiency in advanced separation processes for spent LIB recycling.</div></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"741 ","pages":"Article 125043"},"PeriodicalIF":9.0,"publicationDate":"2025-12-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145734512","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}