Pub Date : 2026-03-01Epub Date: 2025-10-24DOI: 10.1016/j.advmem.2025.100182
Wei-Long Li , Jiao-Rong Li , Guo-Qiang Li , Xiang Kun Cui , Wen-Long Xue , Ming Hao Li , Zhongfeng Li , Hongliang Dong , Chong-Qing Wan
Metal-Organic Frameworks (MOFs) have been demonstrated to be the perfect candidates of function materials for special specie separation. Although numerous MOFs, nearly 100,000 unique ones, have been explored, only several MOF-based membranes are reported because their lack of processability and grain boundary effects seriously limit their fabrication into thin film. This work discusses a strategy of flux melting, ‘borrowed from inorganic domain’, to prepare a MOF thin film via a simple heat-pressing process by using one meltable MOF and a non-meltable MOF. We observed the flux melting of the non-meltable Zr-MOFs and its meltable derivative modified by the binary ionic liquids, the proportion effect of each part on the melting, processability and film nanofiltration for dye molecules. The melt-quenched glass thin film possesses the network inherited from the pristine MOF via the melt, linker exchange and vitrification mechanism. The interesting pore recovery of MOF upon a solvent stimulation endows the film with pore size control (∼1.2 nm) on the dye molecule separation. A 99.88 % rejection rate and a permeability of 27.7 L/m2·h·bar for Congo red dye solution is observed, which is much better than that of analogous MOF membranes generally obtained through complicate processes.
{"title":"Flux melting of UiO-67 family metal-organic frameworks: the thin film processing and nanofiltration property","authors":"Wei-Long Li , Jiao-Rong Li , Guo-Qiang Li , Xiang Kun Cui , Wen-Long Xue , Ming Hao Li , Zhongfeng Li , Hongliang Dong , Chong-Qing Wan","doi":"10.1016/j.advmem.2025.100182","DOIUrl":"10.1016/j.advmem.2025.100182","url":null,"abstract":"<div><div>Metal-Organic Frameworks (MOFs) have been demonstrated to be the perfect candidates of function materials for special specie separation. Although numerous MOFs, nearly 100,000 unique ones, have been explored, only several MOF-based membranes are reported because their lack of processability and grain boundary effects seriously limit their fabrication into thin film. This work discusses a strategy of flux melting, ‘borrowed from inorganic domain’, to prepare a MOF thin film via a simple heat-pressing process by using one meltable MOF and a non-meltable MOF. We observed the flux melting of the non-meltable Zr-MOFs and its meltable derivative modified by the binary ionic liquids, the proportion effect of each part on the melting, processability and film nanofiltration for dye molecules. The melt-quenched glass thin film possesses the network inherited from the pristine MOF via the melt, linker exchange and vitrification mechanism. The interesting pore recovery of MOF upon a solvent stimulation endows the film with pore size control (∼1.2 nm) on the dye molecule separation. A 99.88 % rejection rate and a permeability of 27.7 L/m<sup>2</sup>·h·bar for Congo red dye solution is observed, which is much better than that of analogous MOF membranes generally obtained through complicate processes.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"6 ","pages":"Article 100182"},"PeriodicalIF":9.5,"publicationDate":"2026-03-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145420549","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-03-01Epub Date: 2025-10-28DOI: 10.1016/j.advmem.2025.100184
Zhihao Huang , Chuanlong Li , Yuanyuan Sheng , Liqiu Yang , Haoli Zhou , Wanqin Jin
Pervaporation (PV) is considered one of the most industrially potential phenol wastewater treatment technologies because of its advantages such as high efficiency and without regeneration. PV membrane performance is a key factor that determines its industrial applicability. Here, polymer-filler-based mixed matrix membranes (MMMs) are proposed to enhance the membrane performance for pervaporation of phenol aqueous solutions. First, three hyper-crosslinked polymer (HCP) fillers were synthesized via the Friedel–Crafts reaction between benzyl alcohol (BA) and a penta-heterocyclic compound, such as furan (Fu), and analyzed by different characterizations. All the fillers exhibited desirable properties such as high phenol adsorption capacity and excellent hydrophobicity. Subsequently, different MMMs were fabricated by incorporating the HCP fillers into poly (ether block amide) (PEBA-2533) for the separation of phenol aqueous solutions. The Fu/BA-HCP@PEBA-2533 MMM was selected for further investigation as it afforded the highest separation factor of 72.2 and a flux of 2.07 kg/(m2·h) at 70 °C for the separation of a 1.5 wt% phenol aqueous solution. The diffusion and solubility coefficients were measured. The effects of different operating conditions on the membrane performance and long-term stability were studied, and the results for the pervaporation of phenol aqueous solutions were compared with previously reported data. Investigating the effects of diverse polymer fillers and their compatibility with polymers on the fabrication and performance of MMMs will be a prospective future research direction.
{"title":"Poly (ether block amide) membranes with hyper-crosslinked polymer fillers for enhanced pervaporation of phenol aqueous solutions","authors":"Zhihao Huang , Chuanlong Li , Yuanyuan Sheng , Liqiu Yang , Haoli Zhou , Wanqin Jin","doi":"10.1016/j.advmem.2025.100184","DOIUrl":"10.1016/j.advmem.2025.100184","url":null,"abstract":"<div><div>Pervaporation (PV) is considered one of the most industrially potential phenol wastewater treatment technologies because of its advantages such as high efficiency and without regeneration. PV membrane performance is a key factor that determines its industrial applicability. Here, polymer-filler-based mixed matrix membranes (MMMs) are proposed to enhance the membrane performance for pervaporation of phenol aqueous solutions. First, three hyper-crosslinked polymer (HCP) fillers were synthesized via the Friedel–Crafts reaction between benzyl alcohol (BA) and a penta-heterocyclic compound, such as furan (Fu), and analyzed by different characterizations. All the fillers exhibited desirable properties such as high phenol adsorption capacity and excellent hydrophobicity. Subsequently, different MMMs were fabricated by incorporating the HCP fillers into poly (ether block amide) (PEBA-2533) for the separation of phenol aqueous solutions. The Fu/BA-HCP@PEBA-2533 MMM was selected for further investigation as it afforded the highest separation factor of 72.2 and a flux of 2.07 kg/(m<sup>2</sup>·h) at 70 °C for the separation of a 1.5 wt% phenol aqueous solution. The diffusion and solubility coefficients were measured. The effects of different operating conditions on the membrane performance and long-term stability were studied, and the results for the pervaporation of phenol aqueous solutions were compared with previously reported data. Investigating the effects of diverse polymer fillers and their compatibility with polymers on the fabrication and performance of MMMs will be a prospective future research direction.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"6 ","pages":"Article 100184"},"PeriodicalIF":9.5,"publicationDate":"2026-03-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145475892","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-03-01Epub Date: 2025-11-03DOI: 10.1016/j.advmem.2025.100186
Yi Gao , Tengpeng Wang , Fangsheng Liu , Dongjie Fan , Xiaoyu Xie , Zhengmao Ye , Dehua Dong , Huanting Wang , Zongping Shao
Ceramic oxygen separation membranes have advantages over cryogenic distillation and pressure swing adsorption in terms of oxygen production. However, the application of ceramic membranes is restricted by membrane stability issues at high operation temperatures. This study develops ultra-stable oxygen separation membranes through the over-doping of Ni into yttrium-doped zirconia (NYSZ). The Ni doping amount reaches 18.1 mol%, and Ni dissolution substantially increases the electronic conductivity of the yttrium-doped zirconia membranes under both oxidizing and reducing atmospheres, which is as high as 0.96 S cm−1. Accordingly, high oxygen permeation rates of up to 1.68 mL min−1 cm−2 at 800 °C were achieved, which are comparable with those of conventional perovskite membranes (3.53 mL min−1 cm−2). The ultra-stable NYSZ membranes were confirmed with stable electrochemical reforming of methane for 310 h. Therefore, the robust NYSZ membranes demonstrate great potential in practical applications.
在制氧方面,陶瓷氧分离膜具有低温蒸馏和变压吸附的优点。然而,陶瓷膜的应用受到高温下膜稳定性问题的限制。本研究通过在掺钇氧化锆(NYSZ)中过量掺杂Ni来制备超稳定的氧分离膜。Ni掺杂量达到18.1 mol%,在氧化和还原气氛下,Ni的溶解均显著提高了钇掺杂氧化锆膜的电导率,最高可达0.96 S cm−1。因此,在800°C下实现了高达1.68 mL min - 1 cm - 2的高氧渗透率,这与传统钙钛矿膜(3.53 mL min - 1 cm - 2)相当。通过稳定的甲烷电化学重整310 h,证实了NYSZ膜的超稳定性。因此,坚固耐用的NYSZ膜在实际应用中显示出巨大的潜力。
{"title":"Ultra-stable Ni-overdoped yttria-stabilized zirconia oxygen separation membranes for methane partial oxidation","authors":"Yi Gao , Tengpeng Wang , Fangsheng Liu , Dongjie Fan , Xiaoyu Xie , Zhengmao Ye , Dehua Dong , Huanting Wang , Zongping Shao","doi":"10.1016/j.advmem.2025.100186","DOIUrl":"10.1016/j.advmem.2025.100186","url":null,"abstract":"<div><div>Ceramic oxygen separation membranes have advantages over cryogenic distillation and pressure swing adsorption in terms of oxygen production. However, the application of ceramic membranes is restricted by membrane stability issues at high operation temperatures. This study develops ultra-stable oxygen separation membranes through the over-doping of Ni into yttrium-doped zirconia (NYSZ). The Ni doping amount reaches 18.1 mol%, and Ni dissolution substantially increases the electronic conductivity of the yttrium-doped zirconia membranes under both oxidizing and reducing atmospheres, which is as high as 0.96 S cm<sup>−1</sup>. Accordingly, high oxygen permeation rates of up to 1.68 mL min<sup>−1</sup> cm<sup>−2</sup> at 800 °C were achieved, which are comparable with those of conventional perovskite membranes (3.53 mL min<sup>−1</sup> cm<sup>−2</sup>). The ultra-stable NYSZ membranes were confirmed with stable electrochemical reforming of methane for 310 h. Therefore, the robust NYSZ membranes demonstrate great potential in practical applications.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"6 ","pages":"Article 100186"},"PeriodicalIF":9.5,"publicationDate":"2026-03-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145529064","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-03-01Epub Date: 2025-10-30DOI: 10.1016/j.advmem.2025.100174
Jing Wang , Guoke Zhao , Bo Chen , Gongqing Tang , Yiqun Liu , Pei Li
Two series of soluble polyimides based on pyromellitic dianhydride (PMDA) were synthesized and investigated for gas separation applications. The first series was prepared by reacting PMDA with 5(6)-1-(4-aminophenyl)-1,3,3′-trimethylindane (5(6)-DAPI). Two commercially available DAPI mixtures, designated as DAPI-1 and DAPI-2, containing 5-DAPI to 6-DAPI isomer ratios of 36:64 and 44:56, respectively, were employed. The results indicated that the higher structural distortion associated with 6-DAPI in PMDA-DAPI-1 demonstrated greater gas permeability but lower selectivity compared to PMDA-DAPI-2. The second series of polyimides utilized diethyl toluene diamine (DETDA). Particular emphasis was placed on polyimides obtained through the copolymerization of DETDA with either 2,4,6-trimethyl-1,3-diaminobenzene (DAM) or 1,5-diaminonaphthalene (NDA), at a diamino monomer ratio of 3:1. The PMDA-DETDA polyimide exhibited higher gas permeability but lower selectivity compared to copolyimide counterparts. Notably, DETDA-based polyimides exhibited CO2/CH4 separation performances approaching the 1991 Robeson upper bound under mixed gas conditions. Furthermore, two series of polyimides showed high glass transition temperatures (Tg) ranging from 461 °C to 534 °C, suggesting their suitability for high-temperature gas separation applications.
{"title":"Gas separation performance of soluble PMDA-polyimides controlled by diamine isomerism and copolymerization","authors":"Jing Wang , Guoke Zhao , Bo Chen , Gongqing Tang , Yiqun Liu , Pei Li","doi":"10.1016/j.advmem.2025.100174","DOIUrl":"10.1016/j.advmem.2025.100174","url":null,"abstract":"<div><div>Two series of soluble polyimides based on pyromellitic dianhydride (PMDA) were synthesized and investigated for gas separation applications. The first series was prepared by reacting PMDA with 5(6)-1-(4-aminophenyl)-1,3,3′-trimethylindane (5(6)-DAPI). Two commercially available DAPI mixtures, designated as DAPI-1 and DAPI-2, containing 5-DAPI to 6-DAPI isomer ratios of 36:64 and 44:56, respectively, were employed. The results indicated that the higher structural distortion associated with 6-DAPI in PMDA-DAPI-1 demonstrated greater gas permeability but lower selectivity compared to PMDA-DAPI-2. The second series of polyimides utilized diethyl toluene diamine (DETDA). Particular emphasis was placed on polyimides obtained through the copolymerization of DETDA with either 2,4,6-trimethyl-1,3-diaminobenzene (DAM) or 1,5-diaminonaphthalene (NDA), at a diamino monomer ratio of 3:1. The PMDA-DETDA polyimide exhibited higher gas permeability but lower selectivity compared to copolyimide counterparts. Notably, DETDA-based polyimides exhibited CO<sub>2</sub>/CH<sub>4</sub> separation performances approaching the 1991 Robeson upper bound under mixed gas conditions. Furthermore, two series of polyimides showed high glass transition temperatures (Tg) ranging from 461 °C to 534 °C, suggesting their suitability for high-temperature gas separation applications.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"6 ","pages":"Article 100174"},"PeriodicalIF":9.5,"publicationDate":"2026-03-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145475891","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-03-01Epub Date: 2025-10-10DOI: 10.1016/j.advmem.2025.100175
Yuling Yang , Yingxin Zhang , Ping Zhu , Lei Tang , Zhixiang Zeng , Lijing Zhu
Underwater superoleophobic characteristics of the membranes have been developed to defeat fouling caused by organic solvents and oils with low viscosity and high volatility in oily wastewater treatment. However, the classic strategy is lacking in fighting for worse membranes caused by viscous/nonvolatile oils and soluble materials such as dyes and antibiotics in wastewater. Hence, a synergistic antifouling mechanism, combining hydrophilicity/low oil adhesive underwater superoleophobicity and advanced oxidation processes (AOPs), is proposed and implemented by CoFe2O4/Fe2O3 nanoparticles anchored on polyvinylidene fluoride/polyacrylic acid (PVDF/PAA) blend membranes against various foulants in wastewater. Briefly, the as-prepared composite membrane not only repels the oils and hydrophobic groups in dyes/antibiotics from adhering to the surface due to its low oil adhesive underwater superoleophobicity and hydrophilicity, but also it can effectively degrade the foulants on the surface and within the pore walls because of its excellent AOPs performances. Specially, after the separation of complex oil-in-water emulsion including soybean oil, methylene blue (MB), and levofloxacin (LEVO), the composite membrane bearing hydrophilicity/underwater superoleophobicity and excellent AOPs has a high flux recovery ratio of 95.4 ± 0.3 % and a low fouling resistance of 0.1 × 1011 m−1. This innovative synergistic antifouling mechanism offers an outstanding anti-fouling membrane for the purification of complex wastewater containing various foulants.
{"title":"Synergizing peroxymonosulfate-activated advanced oxidation processes with underwater superoleophobicity in composite membranes for enhanced anti-fouling in oily wastewater purification","authors":"Yuling Yang , Yingxin Zhang , Ping Zhu , Lei Tang , Zhixiang Zeng , Lijing Zhu","doi":"10.1016/j.advmem.2025.100175","DOIUrl":"10.1016/j.advmem.2025.100175","url":null,"abstract":"<div><div>Underwater superoleophobic characteristics of the membranes have been developed to defeat fouling caused by organic solvents and oils with low viscosity and high volatility in oily wastewater treatment. However, the classic strategy is lacking in fighting for worse membranes caused by viscous/nonvolatile oils and soluble materials such as dyes and antibiotics in wastewater. Hence, a synergistic antifouling mechanism, combining hydrophilicity/low oil adhesive underwater superoleophobicity and advanced oxidation processes (AOPs), is proposed and implemented by CoFe<sub>2</sub>O<sub>4</sub>/Fe<sub>2</sub>O<sub>3</sub> nanoparticles anchored on polyvinylidene fluoride/polyacrylic acid (PVDF/PAA) blend membranes against various foulants in wastewater. Briefly, the as-prepared composite membrane not only repels the oils and hydrophobic groups in dyes/antibiotics from adhering to the surface due to its low oil adhesive underwater superoleophobicity and hydrophilicity, but also it can effectively degrade the foulants on the surface and within the pore walls because of its excellent AOPs performances. Specially, after the separation of complex oil-in-water emulsion including soybean oil, methylene blue (MB), and levofloxacin (LEVO), the composite membrane bearing hydrophilicity/underwater superoleophobicity and excellent AOPs has a high flux recovery ratio of 95.4 ± 0.3 % and a low fouling resistance of 0.1 × 10<sup>11</sup> m<sup>−1</sup>. This innovative synergistic antifouling mechanism offers an outstanding anti-fouling membrane for the purification of complex wastewater containing various foulants.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"6 ","pages":"Article 100175"},"PeriodicalIF":9.5,"publicationDate":"2026-03-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145398633","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2026-03-01Epub Date: 2025-10-31DOI: 10.1016/j.advmem.2025.100183
Chen-Jie Wei , Xun Li , Xing-Yu Chen , Ya-Wei Lin , Dong Yu , He-Lin Zhu , Xue-Li Cao , Bai-Long Xu , Li-Fen Liu
High temperature resistant thin-film composite polyamide (TFC PA) membranes are notable across various applications. However, the pursuit of efficient separation at elevated temperatures was hindered by the thick and unstable active layer. In this work, based on covalent organic frameworks (COFs) decorated with exceptional porosity, remarkably large specific surface areas, and outstanding thermal stability, a TFC PA reverse osmosis (RO) membrane featuring a slimmer selective layer and enhanced thermal stability was achieved through interfacial polymerization mediated by COF nanoparticles as aqueous-phase modifier. Firstly, a novel COFTpDATB nanoparticles with high free volume and rigidity were designed and synthesized based on 3,3′-diamine-Trögers base (DATB) with V-shaped rigid structure and 1,3,5-Triformylphloroglucinol (Tp). The introduction of COFTpDATB nanoparticles retards the penetration of the aqueous phase into the organic phase, facilitating the formation of a thinner and more uniform PA selective layer. The resultant COFTpDATB modified TFC RO membrane exhibited a water permeance of 35.8 L/(m2·h) and high salt rejection rate of 99.6 %. Notably, the hydrogen bond crosslinking density might be increased owing to hydrogen bond formation between carboxyl groups of PA separation layer and a tertiary amine group of COFTpDATB, which further guarantee the high salt rejection under high temperature. The membrane showed a high water permeance of 83.7 L/(m2·h) and rejection rate of 99.1 % even at 70 °C. Overall, enhanced by incorporation of COFTpDATB nanoparticles, TFC PA RO membrane exhibited excellent thermal stability and separation efficiency. The current work is envisaged to supply direction for the high-performance TFC PA RO membrane for high temperature resistance.
耐高温薄膜复合聚酰胺(TFC PA)膜在各种应用中都是值得注意的。然而,在高温下追求有效的分离受到厚厚的和不稳定的活性层的阻碍。在这项工作中,基于共价有机框架(COFs)具有优异的孔隙率,显着的大比表面积和出色的热稳定性,通过COF纳米颗粒作为水相改性剂介导的界面聚合,获得了具有更薄选择层和增强热稳定性的TFC PA反渗透(RO)膜。首先,以具有v型刚性结构的3,3 ' -diamine-Trögers碱(DATB)和1,3,5-三甲酰间苯三酚(Tp)为基材,设计并合成了具有高自由体积和高刚性的新型COFTpDATB纳米颗粒。COFTpDATB纳米颗粒的引入延缓了水相向有机相的渗透,有利于形成更薄、更均匀的PA选择层。所得COFTpDATB改性TFC反渗透膜的渗透率为35.8 L/(m2·h),盐去除率高达99.6%。值得注意的是,由于PA分离层的羧基与COFTpDATB的叔胺基之间形成氢键,可能会增加氢键交联密度,从而进一步保证了高温下的高阻盐性。在70℃条件下,膜的透水率为83.7 L/(m2·h),截留率为99.1%。总的来说,COFTpDATB纳米颗粒的加入增强了TFC PA RO膜的热稳定性和分离效率。本研究为高性能TFC PA RO耐高温膜的研究提供了方向。
{"title":"High temperature resistant thin film composite polyamide membrane constructed via 3,3′-diamine-Tröger base COFs for enhancing reverse osmosis separation performances","authors":"Chen-Jie Wei , Xun Li , Xing-Yu Chen , Ya-Wei Lin , Dong Yu , He-Lin Zhu , Xue-Li Cao , Bai-Long Xu , Li-Fen Liu","doi":"10.1016/j.advmem.2025.100183","DOIUrl":"10.1016/j.advmem.2025.100183","url":null,"abstract":"<div><div>High temperature resistant thin-film composite polyamide (TFC PA) membranes are notable across various applications. However, the pursuit of efficient separation at elevated temperatures was hindered by the thick and unstable active layer. In this work, based on covalent organic frameworks (COFs) decorated with exceptional porosity, remarkably large specific surface areas, and outstanding thermal stability, a TFC PA reverse osmosis (RO) membrane featuring a slimmer selective layer and enhanced thermal stability was achieved through interfacial polymerization mediated by COF nanoparticles as aqueous-phase modifier. Firstly, a novel COF<sub>TpDATB</sub> nanoparticles with high free volume and rigidity were designed and synthesized based on 3,3′-diamine-Trögers base (DATB) with V-shaped rigid structure and 1,3,5-Triformylphloroglucinol (Tp). The introduction of COF<sub>TpDATB</sub> nanoparticles retards the penetration of the aqueous phase into the organic phase, facilitating the formation of a thinner and more uniform PA selective layer. The resultant COF<sub>TpDATB</sub> modified TFC RO membrane exhibited a water permeance of 35.8 L/(m<sup>2</sup>·h) and high salt rejection rate of 99.6 %. Notably, the hydrogen bond crosslinking density might be increased owing to hydrogen bond formation between carboxyl groups of PA separation layer and a tertiary amine group of COF<sub>TpDATB</sub>, which further guarantee the high salt rejection under high temperature. The membrane showed a high water permeance of 83.7 L/(m<sup>2</sup>·h) and rejection rate of 99.1 % even at 70 °C. Overall, enhanced by incorporation of COF<sub>TpDATB</sub> nanoparticles, TFC PA RO membrane exhibited excellent thermal stability and separation efficiency. The current work is envisaged to supply direction for the high-performance TFC PA RO membrane for high temperature resistance.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"6 ","pages":"Article 100183"},"PeriodicalIF":9.5,"publicationDate":"2026-03-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145623779","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-01-01Epub Date: 2025-03-18DOI: 10.1016/j.advmem.2025.100141
Muhammad Inam Bari, Bende Merve Kayhan, Bengü Bozkaya, Aykut Argönül
Reverse osmosis (RO) polyamide membranes are widely used for water treatment applications. However, certain processes such as wastewater reuse require regular membrane cleaning and disinfection with oxidants, which can lead to early membrane degradation. Furthermore, some metal ions present in the water can act as a catalyst for further accelerating the degradation. This early degradation of RO membranes poses significant challenges, resulting in operational inefficiencies, early disposal of membranes, and elevated operational costs. Fortunately, there is the possibility of recovering some part of this performance loss by means of chemical treatment through rejuvenating agents. This study aims to investigate the effectiveness of a commercially available rejuvenating agent containing tannic acid for restoring salt rejection and permeability parameters on degraded thin-film polyamide membranes. The membranes were first degraded using 250 ppm sodium hypochlorite (NaOCl) and 0.05 ppm ferric chloride (FeCl3) at various pH levels (pH = 4, 7 and 9). After applying the rejuvenation treatment to the degraded membranes, the efficiency of the rejuvenating agent was determined based on the improvement achieved for performance testing with respect to salt rejection and permeability. Analytical characterization of the membranes was carried out with Fourier Transform Infrared Spectroscopy-Attenuated Total Reflection (FTIR-ATR). It was found that the chlorine degradation of membranes was accelerated in the presence of FeCl3 at all studied pH levels but more prominently in the acidic region. This acceleration effect was attributed to the formation of (, ) radicals. Under the conditions studied in this work, rejuvenating agent treatment effectively enhanced the salt rejection capability of the degraded membranes but was unable to restore the permeate flux.
{"title":"Rejuvenation of reverse osmosis polyamide membranes degraded by chlorine in the presence of ferric chloride","authors":"Muhammad Inam Bari, Bende Merve Kayhan, Bengü Bozkaya, Aykut Argönül","doi":"10.1016/j.advmem.2025.100141","DOIUrl":"10.1016/j.advmem.2025.100141","url":null,"abstract":"<div><div>Reverse osmosis (RO) polyamide membranes are widely used for water treatment applications. However, certain processes such as wastewater reuse require regular membrane cleaning and disinfection with oxidants, which can lead to early membrane degradation. Furthermore, some metal ions present in the water can act as a catalyst for further accelerating the degradation. This early degradation of RO membranes poses significant challenges, resulting in operational inefficiencies, early disposal of membranes, and elevated operational costs. Fortunately, there is the possibility of recovering some part of this performance loss by means of chemical treatment through rejuvenating agents. This study aims to investigate the effectiveness of a commercially available rejuvenating agent containing tannic acid for restoring salt rejection and permeability parameters on degraded thin-film polyamide membranes. The membranes were first degraded using 250 ppm sodium hypochlorite (NaOCl) and 0.05 ppm ferric chloride (FeCl<sub>3</sub>) at various pH levels (pH = 4, 7 and 9). After applying the rejuvenation treatment to the degraded membranes, the efficiency of the rejuvenating agent was determined based on the improvement achieved for performance testing with respect to salt rejection and permeability. Analytical characterization of the membranes was carried out with Fourier Transform Infrared Spectroscopy-Attenuated Total Reflection (FTIR-ATR). It was found that the chlorine degradation of membranes was accelerated in the presence of FeCl<sub>3</sub> at all studied pH levels but more prominently in the acidic region. This acceleration effect was attributed to the formation of (<span><math><mrow><mo>·</mo><mtext>OH</mtext></mrow></math></span>, <span><math><mrow><mo>·</mo><mtext>OCl</mtext></mrow></math></span>) radicals. Under the conditions studied in this work, rejuvenating agent treatment effectively enhanced the salt rejection capability of the degraded membranes but was unable to restore the permeate flux.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"5 ","pages":"Article 100141"},"PeriodicalIF":0.0,"publicationDate":"2025-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"143678398","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-01-01Epub Date: 2025-06-09DOI: 10.1016/j.advmem.2025.100156
Yuting Wang , Bin Yan , Jiaying Liu , Runkai Wang , Pinhua Rao , Yang Liu
Metal-organic framework (MOF) membranes have emerged as a promising solution for lithium extraction from salt lake brines due to their tunable pore structures and high specific surface areas. Their exceptional selectivity for Li+, combined with efficient extraction and robust performance in complex ionic environments, positions MOF membranes as a key technology for low-concentration lithium extraction. However, meeting industrial-scale demands requires not only enhancing membrane selectivity and permeability, but also addressing long-term stability and reusability under harsh conditions. This review provides a comprehensive overview of recent advances in MOF-based membrane materials for Li+ extraction, focusing on both inorganic and organic substrate-supported configurations. Strategic approaches in structural design such as the selection of metal nodes, ligand modification, and encapsulation of active molecules, and growth control techniques to achieve precise pore architectures are discussed. Furthermore, methods for enhancing membrane robustness through multilayer and composite structures to improve antifouling properties and durability are outlined. Finally, the challenges and emerging trends are also proposed for sustainable and high-efficiency lithium extraction. This work offers valuable insights and theoretical support for the ongoing technical innovation and industrial application of MOF membranes in lithium extraction.
{"title":"Advances in MOF membrane strategies for selective lithium extraction from salt lake brine","authors":"Yuting Wang , Bin Yan , Jiaying Liu , Runkai Wang , Pinhua Rao , Yang Liu","doi":"10.1016/j.advmem.2025.100156","DOIUrl":"10.1016/j.advmem.2025.100156","url":null,"abstract":"<div><div>Metal-organic framework (MOF) membranes have emerged as a promising solution for lithium extraction from salt lake brines due to their tunable pore structures and high specific surface areas. Their exceptional selectivity for Li<sup>+</sup>, combined with efficient extraction and robust performance in complex ionic environments, positions MOF membranes as a key technology for low-concentration lithium extraction. However, meeting industrial-scale demands requires not only enhancing membrane selectivity and permeability, but also addressing long-term stability and reusability under harsh conditions. This review provides a comprehensive overview of recent advances in MOF-based membrane materials for Li<sup>+</sup> extraction, focusing on both inorganic and organic substrate-supported configurations. Strategic approaches in structural design such as the selection of metal nodes, ligand modification, and encapsulation of active molecules, and growth control techniques to achieve precise pore architectures are discussed. Furthermore, methods for enhancing membrane robustness through multilayer and composite structures to improve antifouling properties and durability are outlined. Finally, the challenges and emerging trends are also proposed for sustainable and high-efficiency lithium extraction. This work offers valuable insights and theoretical support for the ongoing technical innovation and industrial application of MOF membranes in lithium extraction.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"5 ","pages":"Article 100156"},"PeriodicalIF":0.0,"publicationDate":"2025-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144312869","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-01-01Epub Date: 2025-06-28DOI: 10.1016/j.advmem.2025.100163
Yan Zhu, Danwei Huang, Hongbo Xie, Zheyuan Liu, Fei-Fei Chen, Yan Yu
Polyamide (PA) nanofiltration membranes have raised considerable interest in the realm of water purification. However, balancing permeability and rejection remains a critical challenge in membrane science and technology. Herein, we report that weak non-covalent hydrogen bonds and strong coordination bonds between ultrathin calcium silicate (UCS) interlayers and piperazine (PIP) powerfully control its diffusion. Theoretical calculations reveal that coordination bonds dominate PIP binding on UCS with an adsorption energy of −443.83 kJ mol−1, thereby impeding its movement. The diffusion coefficient of PIP diminishes by 14 % upon the incorporation of UCS, as evidenced by molecular dynamics simulations. As a consequence, a superhydrophilic, smooth, loose, and ultrathin (∼18.9 nm) PA separation layer is created. The as-obtained UCS-interlayered PA possesses a remarkable water permeance of 31.7 L m−2 h−1 bar−1 that is 2.2-fold higher than that of UCS-free PA, while dye rejection rates keep a high level. Furthermore, the UCS-interlayered PA demonstrates exceptional antifouling performance with a 95 % flux recovery ratio and long-term stability during 16-h filtration. The study highlights the pivotal role of mineral interlayers in tailoring amine monomer diffusion via multiple interfacial interactions for advanced water treatment applications.
{"title":"Ultrathin mineral interlayers regulate interfacial polymerization of polyamide nanofiltration membranes via multiple non-covalent and coordination bonding for rapid molecular separation","authors":"Yan Zhu, Danwei Huang, Hongbo Xie, Zheyuan Liu, Fei-Fei Chen, Yan Yu","doi":"10.1016/j.advmem.2025.100163","DOIUrl":"10.1016/j.advmem.2025.100163","url":null,"abstract":"<div><div>Polyamide (PA) nanofiltration membranes have raised considerable interest in the realm of water purification. However, balancing permeability and rejection remains a critical challenge in membrane science and technology. Herein, we report that weak non-covalent hydrogen bonds and strong coordination bonds between ultrathin calcium silicate (UCS) interlayers and piperazine (PIP) powerfully control its diffusion. Theoretical calculations reveal that coordination bonds dominate PIP binding on UCS with an adsorption energy of −443.83 kJ mol<sup>−1</sup>, thereby impeding its movement. The diffusion coefficient of PIP diminishes by 14 % upon the incorporation of UCS, as evidenced by molecular dynamics simulations. As a consequence, a superhydrophilic, smooth, loose, and ultrathin (∼18.9 nm) PA separation layer is created. The as-obtained UCS-interlayered PA possesses a remarkable water permeance of 31.7 L m<sup>−2</sup> h<sup>−1</sup> bar<sup>−1</sup> that is 2.2-fold higher than that of UCS-free PA, while dye rejection rates keep a high level. Furthermore, the UCS-interlayered PA demonstrates exceptional antifouling performance with a 95 % flux recovery ratio and long-term stability during 16-h filtration. The study highlights the pivotal role of mineral interlayers in tailoring amine monomer diffusion via multiple interfacial interactions for advanced water treatment applications.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"5 ","pages":"Article 100163"},"PeriodicalIF":0.0,"publicationDate":"2025-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144557142","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-01-01Epub Date: 2025-06-27DOI: 10.1016/j.advmem.2025.100161
Xinchen Xiang , Zheng Cao , Yukun Qian , Dan Lu , Jiancong Lu , Jinyan Wang , Shiyu Zhou , Lijun Liang , Zhikan Yao , Lin Zhang
Nanofiltration (NF) is a rapidly growing field, resulting in a surge of publications with diverse focuses. It's challenging for researchers to quickly find key information from the vast amount of publications. Large language models (LLMs) have shown promise in analyzing article and reasoning about knowledge in some scientific fields, but their effectiveness in membrane research is unclear. Here, we introduced the first benchmark specifically designed for membrane studies and used it to systematically evaluate six general-purpose LLMs (i.e., Claude-3.5, Deepseek-R1, Gemini-2.0, GPT-4o-mini, Llama-3.2, and Mistral-small-3.1). Our findings revealed that the complexity and depth of NF knowledge pose a significant challenge for these LLMs, leading to poor performance, particularly in tasks involving membrane mechanisms. To enhance LLMs' using in this field, we developed a specialized NF database and integrated it with the LLMs using Retrieval-Augmented Generation (RAG). RAG significantly improved performance across all models, with average gains of 18.5 % on Question type tasks and 10.8 % on Reasoning type tasks. Moreover, in areas such as membrane fabrication and characterization, several models with RAG demonstrated performance exceeding that of human experts. These results suggested that RAG is a promising strategy for leveraging LLMs in NF research. This study introduced a new path for applying LLMs to membrane research and proposes a professional benchmark to ensure the reliable and effective use of LLMs.
{"title":"Evaluating and advancing large language models for nanofiltration membrane knowledge tasks","authors":"Xinchen Xiang , Zheng Cao , Yukun Qian , Dan Lu , Jiancong Lu , Jinyan Wang , Shiyu Zhou , Lijun Liang , Zhikan Yao , Lin Zhang","doi":"10.1016/j.advmem.2025.100161","DOIUrl":"10.1016/j.advmem.2025.100161","url":null,"abstract":"<div><div>Nanofiltration (NF) is a rapidly growing field, resulting in a surge of publications with diverse focuses. It's challenging for researchers to quickly find key information from the vast amount of publications. Large language models (LLMs) have shown promise in analyzing article and reasoning about knowledge in some scientific fields, but their effectiveness in membrane research is unclear. Here, we introduced the first benchmark specifically designed for membrane studies and used it to systematically evaluate six general-purpose LLMs (i.e., Claude-3.5, Deepseek-R1, Gemini-2.0, GPT-4o-mini, Llama-3.2, and Mistral-small-3.1). Our findings revealed that the complexity and depth of NF knowledge pose a significant challenge for these LLMs, leading to poor performance, particularly in tasks involving membrane mechanisms. To enhance LLMs' using in this field, we developed a specialized NF database and integrated it with the LLMs using Retrieval-Augmented Generation (RAG). RAG significantly improved performance across all models, with average gains of 18.5 % on Question type tasks and 10.8 % on Reasoning type tasks. Moreover, in areas such as membrane fabrication and characterization, several models with RAG demonstrated performance exceeding that of human experts. These results suggested that RAG is a promising strategy for leveraging LLMs in NF research. This study introduced a new path for applying LLMs to membrane research and proposes a professional benchmark to ensure the reliable and effective use of LLMs.</div></div>","PeriodicalId":100033,"journal":{"name":"Advanced Membranes","volume":"5 ","pages":"Article 100161"},"PeriodicalIF":0.0,"publicationDate":"2025-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144588192","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}