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Professor Takeshi Matsuura: An Inspiration to Young Membranologists 松浦武教授:对年轻膜学家的启发
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.116244.1304
N. Hilal
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引用次数: 0
Development of Palladium-Alloy Membranes for Hydrogen Separation and Purification 氢分离纯化用钯合金膜的研究进展
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.110711.1271
Anwu Li, T. Boyd, Jim Lim, J. Grace
This paper summarizes RD 2) preparing and characterizing thin Pd composite membranes; 3) development of Pd-Ru membranes by electroless plating for enhanced stability at higher temperatures; 4) production of palladium membranes for application in hydrogen separation and hydrogen production by fluidized bed membrane reactors.
本文综述了薄钯复合膜的制备和表征;3)通过化学镀法制备Pd-Ru膜,提高其在高温下的稳定性;4)生产用于流化床膜反应器氢气分离和制氢的钯膜。
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引用次数: 5
Gas Separation Properties of Mixed Matrix Membranes based on Polyimide and Graphite Oxide 聚酰亚胺-氧化石墨混合基膜的气体分离性能
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.100069.1244
X. Chen, T. Nguyen, A. Romero, A. Patón, María Sánchez, J. Valverde, S. Kaliaguine, D. Rodrigue
In this work, three different graphene-based materials, namely graphite oxide (GrO), thermally reduced graphite oxide (T-RGrO) and ascorbic acid multi-phase reduced graphene oxide (AMP-RGO), were synthesized and used to produce mixed matrix membranes (MMM) based on Matrimid®5218 for as separation. From the samples produced, a complete set of characterization was performed including XRD, FTIR, TGA and SEM to relate with the gas separation performance using H2, CO2, O2, N2 and CH4. For all the gases studied, the results showed that membrane permeability was inversely proportional to the gas molecular size. This behavior was associated to multi-phase reduced graphite oxide (AMPRGO) being an excellent gas barrier for large gas molecules, especially for CH4. The results showed that the H2/CH4 ideal selectivity increased to 231 which represents a 328% improvement for M/AMP-RGO 0.1 compared to the neat matrix. The CO2/CH4 selectivity was 79.8 for M/AMP-RGO 0.2 wt.% which represents a 344% improvement compared to the neat polymer. These results confirmed that these membranes can be used for methane separation such as in ammonia plants (H2/CH4) or biogas upgrading/natural gas purification (CO2/CH4).
在这项工作中,合成了三种不同的石墨烯基材料,即氧化石墨(GrO),热还原氧化石墨(T-RGrO)和抗坏血酸多相还原氧化石墨烯(AMP-RGO),并用于制备基于Matrimid®5218的混合基质膜(MMM)进行分离。对制备的样品进行了包括XRD、FTIR、TGA和SEM在内的完整表征,并与H2、CO2、O2、N2和CH4的气体分离性能进行了对比。对所研究的所有气体,结果表明,膜渗透率与气体分子大小成反比。这种行为与多相还原氧化石墨(AMPRGO)是一种优秀的气体屏障有关,特别是对于CH4。结果表明,与纯基质相比,M/AMP-RGO 0.1的H2/CH4理想选择性提高到231,提高了328%。M/AMP-RGO的CO2/CH4选择性为79.8,比纯聚合物提高了344%。这些结果证实,这些膜可用于甲烷分离,如氨厂(H2/CH4)或沼气升级/天然气净化(CO2/CH4)。
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引用次数: 9
A Letter for Honoring Prof. Takeshi Matsuura 纪念松浦武教授的信
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.116245.1305
W. Koros
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引用次数: 0
Takeshi Matsuura: A Truly Inspirational Friend and Membrane Scientist 松浦武:一个真正鼓舞人心的朋友和膜科学家
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.116243.1303
A. Ismail
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引用次数: 0
Membrane Condenser for Particulate Abatement from Waste-Gaseous Streams 用于从废气流中去除颗粒的膜冷凝器
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.112686.1282
M. Frappa, A. Brunetti, E. Drioli, Z. Cui, Jun Pan, F. Macedonio
Membrane Condenser (MC) is a novel membrane contactor operation recently investigated for the valorization of industrial waste gaseous streams. In particular, until now, it was applied for water recovery from flue gas, cooling tower plumes, etc. More recently, its effectiveness and flexibility in contaminants (such as, NH3 , HF, SO2 ) removal and control from waste gaseous streams was also proved. In the present work, the application of membrane condenser for water recovery as well as microparticles removal from gaseous streams are presented. Experimental tests showed that microparticles did not affect membrane condenser performance, neither in terms of water recovery nor in term of fouling. Moreover, the carried-out tests revealed also that the complete retention of particles can be achieved only through the proper choice of the membrane, with pore size lower than particles diameter.
膜冷凝器(MC)是近年来研究的一种用于工业废气处理的新型膜接触器。特别是,到目前为止,它被应用于烟气、冷却塔羽流等水的回收。最近,它在污染物(如NH3, HF, SO2)去除和控制废气流中的有效性和灵活性也得到了证明。本文介绍了膜冷凝器在水回收和气体中微粒去除方面的应用。实验结果表明,微颗粒不影响膜冷凝器的性能,无论是在水回收方面还是在污染方面。此外,所进行的试验还表明,只有适当选择孔径小于颗粒直径的膜,才能实现颗粒的完全保留。
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引用次数: 4
Activator Generated Electron Transfer Combined Atom Transfer Radical Polymerization (AGET-ATRP) for Controlled Grafting Location of Glycidyl Methacrylate on Regenerated Cellulose Ultrafiltration Membranes 活化剂生成的电子转移结合原子转移自由基聚合(AGET-ATRP)用于甲基丙烯酸缩水甘油酯在再生纤维素超滤膜上的接枝
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.109047.1266
A. Sengupta, Ranil Wickramasinghe
This investigation indicates the ability to selectively graft glycidyl methacrylate (GMA) only from the external surface of regenerated cellulose (RC) ultrafiltration (UF) membranes using activator generated electron transfer (AGET) atom transfer radical polymerization (ATRP). This controlled polymerization resulted in epoxy functionalized polymer brush ends. Further reaction of the terminal epoxy groups provides a flexible platform to introduce desired functionalities either by electrophilic or nucleophilic epoxy ring opening. Selective grafting from the external membrane surface was achieved by using an appropriate pore filling solvent prior to modification. A high viscosity pore filling solvent that is immiscible with the reactive monomer solution used during surface modification was the most effective in supressing grafting from the internal pore surface. The effects of grafting on membrane performance were evaluated by determining water permeability and protein rejection.
本研究表明,利用激活剂生成的电子转移(AGET)原子转移自由基聚合(ATRP)技术,仅从再生纤维素(RC)超滤(UF)膜的外表面选择性接枝甲基丙烯酸甘油酯(GMA)的能力。这种控制聚合产生了环氧功能化聚合物刷端。末端环氧基团的进一步反应提供了一个灵活的平台,通过亲电或亲核环氧环开口引入所需的功能。通过在修饰前使用合适的孔填充溶剂,实现了外膜表面的选择性接枝。高粘度的孔隙填充溶剂与表面改性过程中使用的反应性单体溶液不混溶,在抑制内部孔隙表面接枝方面最有效。通过测定膜的透水性和蛋白质排斥反应来评价接枝对膜性能的影响。
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引用次数: 3
Membrane Science and Research: A Tribute to Professor Takeshi Matsuura 膜科学与研究:致敬松浦武教授
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.117578.1308
D. Rana
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引用次数: 0
Seawater Desalination by Using Nanofiltration (NF) and Brackish Water Reverse Osmosis (BWRO) Membranes in Sequential Mode of Operation 纳滤(NF)和微咸水反渗透(BWRO)膜顺序操作的海水淡化
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.107844.1264
C. Kaya, Y. A. Jarma, Enver Guler, N. Kabay, M. Arda, Mithat Yükse
In this study, the applicability of nanofiltration (NF) membranes as a pretreatment prior to reverse osmosis (RO) in seawater desalination was investigated. The membranes used wereNF270 and NF90 as the NF membranes, while the brackish water (BW) RO membrane BW30 was used as the RO membrane. In desalination tests, permeates of the NF membraneswere collected and used as the feed to the BW30 membrane. The calculated permeate fluxes were 6.7 L/h.m2, 11.3 L/h.m2, 24.3 L/h.m2, and 36.6 L/h.m2 for single BW30-35 bar,NF270-30 bar + BW30-35 bar, NF90-30 bar + BW30-25 bar and NF90-30 BW30-35 bar, respectively. The calculated water recovery and rejected salt values were 51.6%, 41.4%,24.8%, 15.4% and 98.2%, 98.2%, 96.0%, 91.0% for NF90-30 bar + BW30-35 bar, NF90-30 bar + BW30-25 bar, NF270-30 bar + BW30-35 bar and single BW30-35 bar, respectively.The qualities of the product waters of integrated systems (NF+BWRO) and the single BWRO system were also investigated. Boron rejection was fairly well with average boronrejections of 59.3% and 60.2% by NF90-30 bar + BW30-25 bar and NF90-30 bar + BW30-35 bar combinations, respectively while single BW30-35 bar gave an average rejection of49.6%. The results obtained showed that the quality of product water obtained using single BWRO did not comply with the irrigation standards, while the integrated systems providedtotal compliance to irrigation standards with the exception of boron.
在本研究中,研究了纳滤(NF)膜作为反渗透(RO)前预处理在海水淡化中的适用性。采用enf270和NF90作为滤膜,微淡水反渗透膜BW30作为反渗透膜。在脱盐试验中,收集了纳滤膜的渗透液,作为BW30膜的进料。计算的渗透通量为6.7 L/h。m2, 11.3 L/h。m2, 24.3 L/h。m2, 36.6 L/h。单个BW30-35 bar、NF270-30 bar + BW30-35 bar、NF90-30 bar + BW30-25 bar和NF90-30 BW30-35 bar分别为m2。NF90-30 bar + BW30-35 bar、NF90-30 bar + BW30-25 bar、NF270-30 bar + BW30-35 bar和单一BW30-35 bar的计算含水率和废盐值分别为51.6%、41.4%、24.8%、15.4%和98.2%、98.0%、96.0%、91.0%。研究了综合系统(NF+BWRO)和单一BWRO系统的产水水质。NF90-30 bar + BW30-25 bar和NF90-30 bar + BW30-35 bar组合对硼的平均去除率分别为59.3%和60.2%,而单个BW30-35 bar的平均去除率为49.6%。结果表明,采用单一BWRO获得的产品水水质不符合灌溉标准,而采用综合系统获得的产品水除硼外均符合灌溉标准。
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引用次数: 15
Membrane Distillation for Water Recovery and Its Fouling Phenomena 膜蒸馏水回收及其污染现象
Q2 Materials Science Pub Date : 2020-01-01 DOI: 10.22079/JMSR.2019.111501.1277
Changyong Shi, Lyly Leow Hui Ting, O. B. Seng
The total volume of water on Earth is circa 300 million cubic miles, with close to 98.0% being salt water and the remaining 2.0% fresh water. It has been increasingly more challenging to harvest fresh water from surface water, seawater and even from wastewater due to the combination of factors, viz. burgeoning population growth, rapid industrialization and climate change. Recently, membrane distillation (MD) emerges as a promising cost-effective thermal driven sustainable water recovery technology when integrated with renewable energy sources. However, one of the major challenges for MD is the membrane fouling, which has been gaining popularity in the recent literature, as well. The membrane fouling propensity for MD is very much depends on the type of feed water, suitability of membrane and the operating conditions. The objective of this review is to investigate the fouling phenomena of membrane distillation in wastewater treatment and desalination. The design of membrane and its system from the perspective of material and process design were discussed to provide an insight on the current and future advancement in MD technology for water recovery. Finally, the future trend of MD is projected based on the state of the art development of MD process.
地球上的水总量约为3亿立方英里,其中接近98.0%是盐水,剩下的2.0%是淡水。由于人口快速增长、工业化快速发展和气候变化等因素的综合作用,从地表水、海水甚至废水中获取淡水的难度越来越大。近年来,膜蒸馏(MD)作为一种极具成本效益的热驱动可持续水回收技术,与可再生能源相结合。然而,在最近的文献中,膜污染也越来越受欢迎,这是MD面临的主要挑战之一。膜污染倾向在很大程度上取决于进水类型、膜的适宜性和操作条件。本文综述了膜蒸馏在污水处理和海水淡化中的污染现象。从材料和工艺设计的角度对膜及其系统的设计进行了探讨,并对水回收的MD技术的现状和未来发展进行了展望。最后,在分析了当前MD工艺发展现状的基础上,展望了MD的未来发展趋势。
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引用次数: 33
期刊
Journal of Membrane Science and Research
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