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A Novel Approach using Reverse Osmosis/Electrodialysis (RO/ED) to Concentrate and Isolate Organic Carbon from Water Samples

机译:一种使用反渗透/电渗析(RO / ED)富集和分离水样品中有机碳的新方法

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The objective of this study was to develop, optimize, and apply a novel approach toconcentrate and isolate organic carbon using reverse osmosis (RO) followed byelectrodialysis (ED). Electrodialysis is a membrane separation process employing ionexchangemembranes which allows separating charged from neutral constituents. Due toan electric potential and a concentration gradient as the driving forces of separation,organic molecules can be isolated from inorganic salts without altering characteristics ofdissolved organic carbon (DOC). Issues associated with ED separation are related topotential migration of charged low-molecular weight organics through the membrane orlosses due to adsorption onto the membrane surface. A 1-stage lab-scale RO-unit, an EDmembrane test unit, and an ED-stack (Electrosynthesis, Inc.) were employed to performexperiments with single organic compound solutions varying in molecular weight,surface water samples, and treated wastewater samples. Five different ion-selectivemembrane pairs were investigated in the membrane test unit to determine the best-suitedED membrane for laboratory-scale operation. To investigate the fate of bulk organics andspecific target compounds, cations, anions, dissolved organic carbon (DOC) and UVabsorbance were measured. Conductivity, pH, and current were measured online duringeach ED-experiment.Lessons learned from this study are that RO separation to concentrate organicsfrom NOM and EfOM samples can achieve DOC recoveries larger than 90 percent.Losses of DOC into the RO permeate varied for NOM samples between 7 and 8 percentand for EfOM samples between 1 and 2 percent, respectively. During the ED-membraneselection process, a monovalent-selective membrane combination (Asahi Glass, Inc.)showed the best DOC rejection of all membranes investigated. The DOC rejection ofNOM and EfOM concentrates during ED-treatment varied between 96 and 97 percent. Itwas found that charged low-molecular weight compounds (molecular weight less than200 Dalton) can only be partly rejected during ED and therefore contributed to the DOCloss. Fouling of humic substances onto the ED membrane was reversible during asubsequent rinsing procedure with 0.1 N HCl-solution. With overall DOC rejection ratesof more than 90 percent the RO/ED-approach can be a valuable alternative to theconventional XAD-8/-4 resin approach to concentrate and isolate organics from watersamples. This approach recovers more and different fractions as compared to XAD-resinmethods and avoids sample contamination and DOC alteration. The approach is fasterand capable of processing higher volumes of samples low in initial DOC (such asgroundwater samples).
机译:这项研究的目的是开发,优化并将一种新颖的方法应用于 通过反渗透(RO)浓缩和分离有机碳 电渗析(ED)。电渗析是采用离子交换的膜分离工艺 允许分离电荷与中性成分的膜。由于 电位和浓度梯度作为分离的驱动力, 可以从无机盐中分离出有机分子,而不会改变 溶解的有机碳(DOC)。与ED分离有关的问题与 带电的低分子量有机物通过膜的潜在迁移或 由于吸附到膜表面而造成的损失。 1级实验室规模的RO单元ED 膜测试装置和ED-stack(Electrosynthesis,Inc.)进行 用分子量不同的单一有机化合物溶液进行的实验, 地表水样品和处理过的废水样品。五种不同的离子选择性 在膜测试装置中对膜对进行了研究,以确定最适合的膜对 ED膜,用于实验室规模的操作。调查散装有机物的命运和 特定的目标化合物,阳离子,阴离子,溶解的有机碳(DOC)和紫外线 测量吸光度。在线测量电导率,pH和电流 每个ED实验。 从这项研究中学到的经验是,RO分离可浓缩有机物 从NOM和EfOM样品中获得的DOC回收率可达到90%以上。 对于NOM样品,DOC进入RO渗透液的损失在7%到8%之间变化 对于EfOM样本,分别为1-2%。在ED膜中 选择过程,单价选择性膜组合(旭硝子株式会社) 在所有研究的膜中均显示出最佳的DOC拒绝率DOC拒绝 ED处理期间的NOM和EfOM浓度在96%至97%之间。它 发现带电的低分子量化合物(分子量小于 200道尔顿)只能在ED期间被部分拒绝,因此促成了DOC 失利。腐殖质在ED膜上的结垢是可逆的 随后用0.1 N HCl溶液冲洗。总体DOC拒绝率 超过90%的RO / ED方法可以替代 传统XAD-8 / -4树脂方法可从水中浓缩和分离有机物 样品。与XAD树脂相比,此方法可回收更多不同的馏分 方法,并避免样品污染和DOC改变。该方法更快 并能够处理大量初始DOC较低的样品(例如 地下水样品)。

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