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Challenges in Membrane Process for Gas Separation from Natural Gas 天然气气分离膜工艺面临的挑战
Pub Date : 2021-07-07 DOI: 10.11113/AMST.V25N2.222
K. Farahdila, P. Goh, A. Ismail, N. F. W. M. Wan, H. Mohd, W. K. Soh, S. Y. Yeo
Membrane technology is cost effective solution for CO2 removal from natural gas. However, there is challenges during its application depending on the polymer material characteristic. Understanding on the polymer fundamental and transport properties, will enable proper design of pre-treatment and operating conditions that suits its capability envelope. Diffusivity selective membrane favors high pressure and high temperature conditions and vice versa for solubility selective polymer. On top of that, the robustness and durability of the resultant membrane, need to be evaluated with multicomponent mixture to understand the effect of competitive sorption, plasticization and aging phenomena that will seriously impacting the membrane performance during its application.
膜技术是一种经济有效的天然气脱除二氧化碳的解决方案。然而,由于高分子材料的特性,其在应用过程中存在一些挑战。了解聚合物的基本性质和输运性质,将有助于设计适合其性能范围的预处理和操作条件。扩散性选择性膜有利于高压和高温条件,溶解度选择性聚合物反之亦然。除此之外,还需要用多组分混合物来评估合成膜的坚固性和耐久性,以了解在应用过程中竞争吸附、塑化和老化现象的影响,这些现象将严重影响膜的性能。
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引用次数: 3
Membrane Fouling – The Enemy of Forward Osmosis 膜污染-正向渗透的敌人
Pub Date : 2021-07-07 DOI: 10.11113/amst.v25n2.220
Z. Chang, Y. H. Teow, S. Yeap, J. Y. Sum
Forward osmosis (FO) is an osmotically driven membrane separation process. It is potentially applied in various industries for nutrient recovery and water reclamation. Although FO showed a lesser fouling tendency than other pressure-driven membrane processes, the solutes in the feed solution would still deposit on the membrane surface, forming a fouling layer that resists water permeation. For that reason, fouling mitigation is a trending issue in the FO process. A better understanding of the fouling mechanism is required before opting for the appropriate strategy to mitigate it. This article describes the fouling mechanism based on different foulant presented in the feed, followed by a method in relieving fouling in the FO process.
正向渗透(FO)是一种渗透驱动的膜分离过程。它在各行业的养分回收和水回收中具有潜在的应用前景。尽管与其他压力驱动膜工艺相比,FO工艺的污染倾向较小,但进料液中的溶质仍会沉积在膜表面,形成一层阻碍水渗透的污染层。因此,污垢缓解是FO过程中的一个趋势问题。在选择适当的策略来减轻污染之前,需要更好地了解污染机制。本文介绍了进料中不同杂质的结垢机理,以及FO工艺中消除结垢的方法。
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引用次数: 1
The Potential Role of Membrane Technology in the Removal of Microplastics from Wastewater 膜技术在去除废水中微塑料中的潜在作用
Pub Date : 2021-07-07 DOI: 10.11113/AMST.V25N2.216
A. Adewuyi, Abisola J. Campbell, O. G. Adeyemi
The presence of microplastics in water is a serious environmental problem. Although several approaches have been employed to tackle the problem, the use of membrane technology in addressing this problem remains encouraging but with limitation such as fouling and chemical instability which can be circumvented. This review identifies the presence of microplastics in water and the role of membrane technology in tackling the removal of microplastics in water. The study revealed the presence of microplastics in different water sources as well as the negative impact of microplastics on aquatic animals. Unfortunately, lack of proper management of plastic wastes has led to an increase in the presence of microplastics in the environment. Despite the profound performance by membrane technology towards the removal of microplastics in water, there is need to further improve on the limitations exhibited by this technology. However, there is no doubt that membrane technology remains an outstanding technology for the removal microplastics in water.
水中微塑料的存在是一个严重的环境问题。虽然已经采用了几种方法来解决这个问题,但使用膜技术来解决这个问题仍然令人鼓舞,但也有一些局限性,例如污垢和化学不稳定性,这些都是可以避免的。本文综述了水中微塑料的存在以及膜技术在去除水中微塑料中的作用。该研究揭示了微塑料在不同水源中的存在,以及微塑料对水生动物的负面影响。不幸的是,由于缺乏对塑料废物的适当管理,导致环境中微塑料的存在增加。尽管膜技术在去除水中微塑料方面有着深刻的表现,但该技术所表现出的局限性还需要进一步改进。然而,毫无疑问,膜技术仍然是去除水中微塑料的一种优秀技术。
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引用次数: 6
Electrospun Bi-layered Composite Membrane for the Removal of Metallic Contaminants in Drinking Water 电纺双层复合膜去除饮用水中金属污染物的研究
Pub Date : 2019-10-10 DOI: 10.11113/amst.v23n3.171
N. Sultana, Dennis E. Daniels
Using biodegradable polymer polycaprolactone (PCL) and zeolite, the present experiment was conducted with the aim of using biodegradable PCL and zeolite based composite membrane to remove silver in drinking water. After optimizing the electrospinning parameters, a double-layered PCL and PCL/zeolite electrospun composite membranes were manufactured. The membranes were then characterized using a scanning electron microscope (SEM) and an energy dispersive X-ray (EDX) and the filtration phenomenon was conducted by dispersing silver nanoparticles in water. After comparing the filtration results using an inductively coupled plasma optical emission spectrometry (ICP-OES), it was observed that the bi-layered membrane filtered 90% of silver present in the water. The present work shows that the new PCL/zeolite based double-layered membrane can be promising to remove contaminants in drinking water.
以生物可降解聚合物聚己内酯(PCL)和沸石为材料,研究了生物可降解聚己内酯和沸石基复合膜对饮用水中银的去除效果。通过对静电纺丝工艺参数的优化,制备了双层PCL和PCL/沸石静电纺丝复合膜。然后用扫描电镜(SEM)和能量色散x射线(EDX)对膜进行了表征,并通过将银纳米粒子分散在水中进行了过滤现象的研究。通过电感耦合等离子体发射光谱(ICP-OES)对过滤结果进行比较,发现双层膜过滤了水中90%的银。研究表明,新型聚氯l /沸石双层膜具有去除饮用水中污染物的良好前景。
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引用次数: 0
Book Review: Advanced Nanomaterials for Membrane Synthesis and Its Applications 书评:用于膜合成的先进纳米材料及其应用
Pub Date : 2019-10-10 DOI: 10.11113/amst.v23n3.172
W. Chong
The book compiled some of the most recent knowledge shared by the experts from different countries who specialize in membrane technology. The effort and knowledge sharing by the experts on the recent development of composite membrane fabrication are greatly appreciated. This book provides readers an overview and insight on how nanomaterials affect the membrane formation, enhance the properties of membrane and ultimately lead to different kinds of applications. 
这本书汇集了来自不同国家的膜技术专家分享的一些最新知识。专家们在复合膜制造的最新发展方面所做的努力和知识的分享是非常值得赞赏的。这本书为读者提供了一个概述和洞察纳米材料如何影响膜的形成,增强膜的性能,并最终导致不同种类的应用。
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引用次数: 0
Fabrication and Performance Evaluation of Integrated Solar-Driven Membrane Distillation System with Serpentine-shape of Flat Plate Solar Collector for Seawater Desalination 蛇形平板太阳能集热器集成太阳能驱动膜蒸馏系统的研制及性能评价
Pub Date : 2019-09-15 DOI: 10.11113/AMST.V23N3.163
M. Hanoin, N. Mohammed, M. A. I. Z. Arris, A. Bakar, N. M. Mokhtar, A. A. Razak
Solar-powered membrane distillation (SPMD) system has gained its popularity in desalination application for past decade credit to the system efficiency in producing pure water and the utilization of renewable energy. However, most of the past SPMD works used commercial solar thermal collector (STC) as the thermal energy supply to the feed solution and the study only focused on the performance of the system in terms of flux and salt rejection. In this work, a self-made flat plate solar collector (FPSC) with the serpentine-shape pipe was designed and fabricated to study the effect of the STC towards the membrane performance. Before testing, a simulation work of the fluid flow inside the serpentine-shape pipe of the FPSC was analyzed using NX 10.0 computer-aided design simulation. After that, the efficiency of the self-made FPSC system was tested directly to sunlight in order to identify the maximum irradiance and the temperature of the feed solution. Due to the fluctuation of solar irradiance, the experimental setup of the SPMD system was tested using a solar simulator, and the performance was compared with the membrane distillation (MD) system without integration with FPSC system. Based on the simulation data, it can be concluded that the heat losses across the pipe are due to the slower fluid velocity and sudden pressure drop, which attributed to centripetal force and pressure differences. Meanwhile, the outdoor evaluation data showed that the temperatures of collector and water inside the feed tank could reach up to 84°C and 64°C, respectively when the maximum irradiance of 938 W/m2 was applied. For the performance evaluation between with and without the self-made FPSC system, it can be seen that only marginal difference can be observed for the permeate flux and salt rejection with an average difference of 6.06% and 1.29%, respectively.
近十年来,太阳能膜蒸馏(SPMD)系统因其生产纯净水的效率和可再生能源的利用而在海水淡化领域得到了广泛的应用。然而,过去的SPMD工程大多采用商用太阳能集热器(STC)作为进料液的热能供应,研究只关注系统在通量和盐的抑制方面的性能。本文设计并制作了一种自制的带有蛇形管的平板太阳能集热器(FPSC),研究了STC对膜性能的影响。试验前,利用NX 10.0计算机辅助设计仿真软件对FPSC蛇形管内流体流动进行了仿真分析。然后,直接在阳光下测试自制FPSC系统的效率,以确定最大辐照度和进料溶液的温度。由于太阳辐照度的波动,利用太阳模拟器对SPMD系统的实验装置进行了测试,并与未与FPSC系统集成的膜蒸馏(MD)系统进行了性能比较。根据模拟数据可以得出,管道上的热损失是由于流体速度变慢和压力下降突然造成的,这是由于向心力和压力差造成的。同时,室外评价数据显示,在最大辐照度为938 W/m2时,集热器温度可达84℃,进料槽内水温可达64℃。通过对自制FPSC系统的性能评价,可以看出,在渗透通量和除盐率方面,两者的平均差异仅为6.06%和1.29%。
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引用次数: 2
Synthesis of GMA/EDMA Uniform Pores Monolith Using Melt blown Polypropylene Nanofibers Templates 熔融吹塑聚丙烯纳米纤维模板合成GMA/EDMA均匀孔整体材料
Pub Date : 2019-09-15 DOI: 10.11113/AMST.V23N3.165
Z. Kamin, N. Ramon, M. Misson, C. C. Ken, R. Sarbatly, D. Krishnaiah, A. Bono
Glycidyl methacrylate / ethyl dimethacrylate (GMA/ EDMA) monoliths consisting of pores induced by polypropylene nanofibers (PPNF) were developed. For creating these pores, templating technique was used where the PPNF act as a template. The PPNF were fabricated using a melt blowing technique at various process operations of polymer flowrate, air pressure and die-to-collector distance at ranges of 15 to 30 Hz, 0.15 to 0.3 MPa and 0.20 to 0.6 m respectively designed using a response surface methodology (RSM). Subsequently, a monolith solution was synthesis using the polymerization of GMA and EDMA, with azobisisobutyronitrile (AIBN) as initiator and cyclohexanol as porogen. The PPNF and GMA/ EDMA monoliths were characterized using SEM and melting point instrument. The findings show, PPNF fiber diameter and melting points were in the range of 5 to 14 x 103 nm and 120 to 130 °C respectively. RSM analysis suggests that air pressure and die-to-collector distance could be an important factor for  PPNF final diameter. Morphology studies demonstrate that GMA/ EDMA monolith have been successfully acquired mesoporous structure and creating uniform pores by PPNF template produce at 22.5 Hz, 0.22 MPa and 0.40 m. As a conclusion, the PPNF can be proposed as a template to prepare monolith having uniform pores.
制备了由聚丙烯纳米纤维(PPNF)诱导孔隙组成的甲基丙烯酸缩水甘油酯/二甲基丙烯酸乙酯(GMA/ EDMA)单体材料。为了创建这些孔,使用了模板技术,其中PPNF作为模板。利用响应面法(RSM)设计不同的工艺操作,分别在15 ~ 30 Hz、0.15 ~ 0.3 MPa和0.20 ~ 0.6 m范围内,采用熔体吹制技术制备PPNF。随后,以偶氮二异丁腈(AIBN)为引发剂,环己醇为破孔剂,采用GMA和EDMA聚合制备了单体溶液。采用SEM和熔点仪对PPNF和GMA/ EDMA单体进行了表征。结果表明,PPNF纤维直径范围为5 ~ 14 × 103 nm,熔点范围为120 ~ 130℃;RSM分析表明,空气压力和模具到收集器的距离可能是影响PPNF最终直径的重要因素。形态学研究表明,在22.5 Hz、0.22 MPa、0.40 m的条件下,PPNF模板制备的GMA/ EDMA单体材料成功获得了介孔结构,并形成了均匀的孔隙。结果表明,PPNF可作为模板制备具有均匀孔隙的整体块体。
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引用次数: 0
Preparation of Blend Hydrophilic Polyetherimide-Cellulose Acetate Hollow Fiber Membrane for Oily Wastewater Treatment 含油废水处理用亲水性聚醚酰亚胺-醋酸纤维素共混中空纤维膜的制备
Pub Date : 2019-09-12 DOI: 10.11113/AMST.V23N3.159
Moslem Nazarian, A. Mansourizadeh, Mehran Abbasi
Membrane separation is known as an efficient technique for oily wastewater treatment. In the present study, cellulose acetate (CA) was introduced into the polyetherimide (PEI) solution in order to enhance hydrophilicity and the membrane structure for oil–water separation. The hollow fiber membranes were prepared via a phase-inversion process. The membranes were characterized by N2 permeation test, water contact angle, pure water flux and field emission scanning electron microscopy (FESEM). The blend PEI-CA membrane presented larger finger-likes morphology with a thicker outer skin layer. From N2 permeation test, the blend membrane showed effective surface porosity of 697 m-1 and mean pore size of 4.5 nm. The higher water flux and lower resistance of the blend PEI-CA membrane were related to the higher hydrophilicity and the open structure. Due to small pore sizes and enhanced hydrophilicity, the blend membrane showed a stable oil rejection of over 98% and water flux of 18 L/m2 h after 100 min of the separation operation. The developed PEI-CA membrane can potentially be applied in petrochemical and refinery industries for oily wastewater treatment.
膜分离是一种高效的含油废水处理技术。本研究将醋酸纤维素(CA)引入聚醚酰亚胺(PEI)溶液中,以增强聚醚酰亚胺(PEI)溶液的亲水性和油水分离膜结构。采用相变法制备中空纤维膜。通过N2渗透试验、水接触角、纯水通量和场发射扫描电镜(FESEM)对膜进行了表征。共混PEI-CA膜呈较大的指状形态,外表皮层较厚。N2渗透测试表明,共混膜的有效表面孔隙率为697 m-1,平均孔径为4.5 nm。共混PEI-CA膜具有较高的水通量和较低的阻力,这与膜具有较高的亲水性和开放结构有关。由于该共混膜孔径小,亲水性增强,在分离操作100 min后,其排油率稳定在98%以上,水通量为18 L/m2 h。所研制的PEI-CA膜在石油化工、炼油等行业的含油废水处理中具有潜在的应用前景。
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引用次数: 2
Computational Modeling of Coupled Free and Porous Media Flow for Membrane-based Filtration Systems: A Review 膜基过滤系统中自由介质与多孔介质耦合流动的计算模型研究进展
Pub Date : 2019-09-12 DOI: 10.11113/AMST.V23N3.158
Antonios Parasyris, Christopher Brady, D. Das, M. Discacciati
We review different mathematical models proposed in literature to describe fluid-dynamic aspects in membrane-based water filtration systems. Firstly, we discuss the societal impact of water filtration, especially in the context of developing countries under emergency situations, and then review the basic concepts of membrane science that are necessary for a mathematical description of a filtration system. Secondly, we categorize the mathematical models available in the literature as (a) microscopic, if the pore-scale geometry of the membrane is accounted for; (b) reduced, if the membrane is treated as a geometrically lower-dimensional entity due to its small thickness compared to the free flow domain; (c) mesoscopic, if the characteristic geometrical dimension of the free flow domain and the porous domain is the same, and a multi-physics problem involving both incompressible fluid flow and porous media flow is considered. Implementation aspects of mesoscopic models in CFD software are also discussed with the help of relevant examples.
我们回顾了文献中提出的描述膜基水过滤系统流体动力学方面的不同数学模型。首先,我们讨论了水过滤的社会影响,特别是在紧急情况下的发展中国家的背景下,然后回顾了过滤系统数学描述所必需的膜科学的基本概念。其次,我们将文献中可用的数学模型分类为:(a)微观的,如果考虑到膜的孔隙尺度几何形状;(b)减少,如果膜被视为几何上较低维的实体,因为它的厚度比自由流域小;(c) mesoscopic,如果自由流域和多孔域的特征几何尺寸相同,并且考虑了不可压缩流体流动和多孔介质流动的多物理场问题。结合相关实例,讨论了CFD软件中介观模型的实现问题。
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引用次数: 2
Effect of Solvent Evaporation Time and Casting Thickness on the Separation Performance of Cellulose Acetate Butyrate Blend Membrane 溶剂蒸发时间和浇铸厚度对醋酸丁酸纤维素共混膜分离性能的影响
Pub Date : 2019-07-15 DOI: 10.11113/AMST.V23N2.151
D. Manimaran, Z. Jawad, C. Leng
Global warming and climate change due to greenhouse gases (GHGs) emission, mostly carbon dioxide (CO2), have induced global efforts to minimize the concentration of atmospheric CO2. To reduce the effects of this problem, membrane technology is selected for the separation of CO2 due to the energy efficiency and economic advantages exhibited. In this study, the chosen polymeric material, cellulose acetate butyrate (CAB) is optimized using a wet phase inversion method with various molecular weight and different casting conditions due to its outstanding film-forming specifications and capabilities of fabricating a defect-free layer of neat membrane. The membrane was synthesized by blending three different molecular weights (Mn) of 12,000, 30,000 and 70,000 at different casting thickness, 150 µm to 300 µm and solvent evaporation time of 3.5 to 5 min. The results of these predominant parameters were then utilized to determine a high performance CAB membrane suitable for an enhanced CO2/Nitrogen (N2) separation. Eventually, a high separation performance CAB membrane was successfully synthesized with a CO2/N2 selectivity of 1.5819 ± 0.0775 when the solvent evaporation time and casting thickness was optimized at 4.5 min and 300 µm, respectively. Through this study, an improved understanding between membrane casting conditions and membrane performance has been achieved, for future development and progress.
由于温室气体(ghg)排放,主要是二氧化碳(CO2),导致全球变暖和气候变化,促使全球努力尽量减少大气中二氧化碳的浓度。为了减少这一问题的影响,由于膜技术具有能效和经济优势,因此选择膜技术进行CO2分离。在本研究中,选用的聚合物材料醋酸丁酸纤维素(CAB)由于其优异的成膜性能和制造无缺陷的整齐膜层的能力,采用湿相转化法对其进行了优化,该材料具有不同分子量和不同铸造条件。在铸造厚度为150µm ~ 300µm,溶剂蒸发时间为3.5 ~ 5 min的条件下,将分子量为12000、30000和70000的三种不同分子量(Mn)混合,合成了一种适合于CO2/氮气(N2)强化分离的高性能CAB膜。最终,在溶剂蒸发时间为4.5 min、浇铸厚度为300µm的条件下,成功合成了CO2/N2选择性为1.5819±0.0775的高分离性能CAB膜。通过本研究,提高了对膜铸造工艺条件与膜性能之间关系的认识,为今后的发展和进步奠定了基础。
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引用次数: 1
期刊
Journal of Applied Membrane Science & Technology
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