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Thin-layer nanofiltration membranes using engineered biopolymers for seawater desalination pre-treatment processes

机译:使用工程生物聚合物的薄层纳滤膜,用于海水淡化预处理工艺

摘要

Nowadays water demand already exceeds supply and water scarcity is a global problem. So it isnecessary to develop novel technologies to be able to use poorer quality source waters for drinkingwater production. Once considered as an expensive, ultimate solution for water supply, desalination isbecoming affordable. The two most commonly used seawater desalination methods are Multi-stageFlash Distillation (MSF) and Seawater Reverse Osmosis (SWRO). SWRO is less energy demandingcompared to MSF, which makes it economically attractive. However there is no backpulsing of theexpensive and delicate reverse osmosis (RO) membranes with air or water, so they are susceptible tofouling, causing the loss of their performance. Therefore cleaning the feed water to the highest levelpossible by nanofiltration, before it reaches the RO membranes would highly increase the efficiency ofthe process.Nanofiltration (NF) as a feed pre-treatment step is a pressure driven membrane separation process thattakes place on a selective layer formed by a semipermeable membrane with properties between ROand ultrafiltration. The objective of this project is the developement of highly efficient thin-film composite(TFC) membranes for SWRO pre-treatment processes based on low-fouling cyanobacterial extracellularpolymeric substances (EPS). TFC membranes combine high flux and mechanical strenght, and they areexpected to be the key components of any water purification technology in the future.Cyanobacterial EPS are complex heteropolysaccharides with putative antimicrobial and antiviralproperties and a particular affinity to bind metal ions [1,2].Within this work, the unicellular N2-fixingmarine cyanobacterium Cyanothece sp. CCY 0110 was chosen for RPS production, since it is amongthe most efficient released polysaccharide (RPS) producers and the polymer has been previouslyextensively characterised [3]. RPS was produced by growing Cyanothece CCY 0110 in 10L bioreactors,in conditions previously defined and the polymer was isolated following the standard methodology [3].A polyvinyl alcohol (PVA) / cyanobacterial EPS blend nanofibrous membranes were fabricated byelectrospinning using polyvinylidene fluoride (PVDF) as a basal membrane, in order to obtain thin-layercomposite nanofiltration membranes. The production of the nanofibers using EPS and PVA asplasticizer in different ratios was produced in a NF-103 MECC Nanon electrospinning equipment with anapplied electric field between 15 and 25 kV and a flow of 0,2 mL/h.Morphological, mechanical, chemical and thermal characterization of the electrospun fibers depositedon the basal membranes, were evaluated by atomic force microscopy (AFM), scanning electronmicroscopy (SEM) and energy dispersive spectroscopy (EDS), dynamical and mechanical analysis(DMA), thermogravimetry (TGA) and differential scanning calorimetry (DSC).The AFM and SEM results show the presence of fibers with dimensions between 54 and 121 nm withlow bead formation. In the EDS analysis presence of sulfur elements was observed confirming theinclusion of EPS in the nanofibers. The morphology and diameter of the nanofibers were mainly affectedby the concentration of the blend solution and the weight ratio of the blend, respectively. The bestPVA/EPS nanofibers were achieved in a ratio of 12 % PVA and 0.4 % EPS. The solution conductivitywas ranging 1500 to 3500 μS/cm with a viscosity of about 100 to 500 cP. The DMA results confirmedthe miscibility of PVA/EPS blends. The elastic modulus of the nanocomposite mats increasedsignificantly as a consequence of the reinforcing effect of EPS. Thermal and mechanical analysisdemonstrated that there were strong intermolecular hydrogen bonds between the molecules EPS-PVAin the blends. The heat-treated electrospun blended membranes showed better tensile mechanicalproperties when compared with PVA alone, and resisted more against disintegration. A lab-scalenanofiltration was performed in a bench stainless steel Sterlitech tangential flow stirred cell (200 mL)connected to an air pressure system that allow pressure driven filtration up to 10 BAR.Bactericidal activity and biofilm formation were tested using Escherichia coli and Sthaphylococcusaureus as pathogenic microorganisms.
机译:如今,水的需求已经超过供应,而水的短缺是一个全球性的问题。因此,有必要开发新技术以能够使用质量较差的原水来生产饮用水。海水淡化曾经被认为是昂贵的供水最终解决方案,现在正变得可以承受。两种最常用的海水淡化方法是多级闪蒸蒸馏(MSF)和海水反渗透(SWRO)。与MSF相比,SWRO的能源需求更少,这使其在经济上更具吸引力。但是,昂贵,细腻的反渗透(RO)膜不会因空气或水而产生反冲,因此它们容易结垢,从而导致其性能下降。因此,在纳滤到达RO膜之前,通过纳滤将进料水清洗到最高水平将极大地提高工艺效率。纳滤(NF)作为进料预处理步骤是压力驱动的膜分离工艺,发生在选择性层上由具有RO和超滤性能的半透膜形成。该项目的目的是开发基于低污染蓝藻胞外聚合物(EPS)的SWRO预处理工艺的高效薄膜复合(TFC)膜。 TFC膜结合了高通量和机械强度,有望成为未来任何水净化技术的关键组成部分。蓝细菌EPS是复杂的杂多糖,具有公认的抗微生物和抗病毒特性,并具有与金属离子结合的特殊亲和力[1,2]。在这项工作中,单细胞N2固定海洋蓝藻蓝藻sp.。选择CCY 0110进行RPS生产,因为它是最有效的释放多糖(RPS)生产商之一,并且该聚合物先前已得到广泛表征[3]。 RPS是通过在预先定义的条件下在10升生物反应器中生长Cyanothece CCY 0110而制备的,并按照标准方法[3]分离出聚合物。通过使用聚偏二氟乙烯(PVDF)进行电纺丝来制备聚乙烯醇(PVA)/蓝细菌EPS共混物纳米纤维膜。作为基底膜,以得到复合的薄层纳滤膜。使用NF-103 MECC Nanon静电纺丝设备在15至25 kV的施加电场和0.2 mL / h的流量下使用EPS和PVA增塑剂以不同比例生产纳米纤维。通过原子力显微镜(AFM),扫描电子显微镜(SEM)和能量色散谱(EDS),动态和机械分析(DMA),热重分析(TGA)和差示扫描量热法评估沉积在基膜上的电纺纤维的热特性(DSC).AFM和SEM结果表明存在尺寸在54至121 nm之间的纤维,且珠粒形成率较低。在EDS分析中观察到硫元素的存在,证实了纳米纤维中包含EPS。纳米纤维的形态和直径分别主要受共混物溶液的浓度和共混物的重量比的影响。最佳的PVA / EPS纳米纤维的比例为12%PVA和0.4%EPS。溶液的电导率在1500至3500μS/ cm的范围内,粘度约为100至500 cP。 DMA结果证实了PVA / EPS混合物的混溶性。纳米复合材料垫的弹性模量由于EPS的增强作用而显着增加。热和机械分析表明,共混物中EPS-PVA分子之间存在强大的分子间氢键。与单独的PVA相比,经热处理的静电纺丝共混膜表现出更好的拉伸机械性能,并且抗崩解性更高。在连接至气压系统的台式不锈钢Sterlitech切向流搅拌池(200 mL)中进行实验室规模的纳滤,可进行高达10 BAR的压力驱动过滤。使用大肠杆菌和Sthaphylococcusaureus作为致病菌测试杀菌活性和生物膜形成微生物。

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