饮用水中有机物毒性的生物识别技术研究进展

从技术应用原理、方法、应用现状及发展等角度,综合介绍了国内外常见的细胞与分子水平的水质生物识别与安全评价方法,分析了这些技术的优点与不足,指出了水质生物监测技术研究的发展方向。     

超声技术处理水中有机污染物

超声技术在处理水中有机污染物的应用近年来受到越来越多的关注.与常规处理方法相比,超声处理高效省时.超声技术对众多难处理有机污染物的降解是有效的.本文介绍了超声降解有机污染物原理、影响因素和各种方法,主要包括单独使用超声处理和超声与生物催化剂、化学氧化、吸附等其它技术的联用,综述了近年来利用超声技术处理水中有机污染物的研究进展,对存在问题和发展趋势提出了见解.     

水中有机污染物前处理方法进展

综述了水样中有机污染物前处理方法的进展情况；重点介绍液-液萃取、固相萃取、液相微萃取、膜萃取和顶空处理技术5种前处理方法的一些基本情况及其优缺点。     

水中重金属离子电富集样品处理技术

提出了一种低浓度重金属离子溶液的快速富集净化处理方法。目标金属离子首先络合为负离子,在正电压牵引下,金属络合离子到达离子膜表面,在膜表面阴离子层吸引下通过阳离子交换膜,并在受体溶液中再次络合为阴离子络合物,在电场作用下向阳极区移动。富集电流为1.5mA,汞离子、镉离子的富集时间分别为20,60min,水样中汞离子、镉离子的富集倍数分别为10.5,3.2倍。本方法避免了液膜稳定性缺陷。     

探究铁和铝在浓硫酸和浓硝酸中的电化学行为

铁和铝在冷的浓硫酸和浓硝酸中都因被钝化而阻止其进一步被腐蚀,通过用Fe、Al做原电池的电极材料,考察其在浓硫酸、浓硝酸中的钝化情况：Fe、Al的钝化快慢、钝化后金属表面氧化膜的致密程度、酸液温度等对钝化的影响等均有所不同。     

SPE-UV在线监测技术监测水源水中微量有机物

安全的饮用水是人类发展、健康和福利的基本需求,是构建和谐社会的基础。一旦发生水质污染或水质污染嫌疑,不论其来源于意外事故还是人为造成,立即对可疑或未知污染物进行快速简便的检测以确定其是否存在,对于水质污染危机决策至关重要。因此应用水质在线监测仪器实施快速的水质     

电-Fenton及类电-Fenton技术处理水中有机污染物

传统Fenton技术是一种广泛用于水体里有机污染物降解的高级氧化技术(advanced oxidation technologies, AOTs)。它利用Fenton试剂Fe²⁺与H₂O₂反应生成具有强氧化性的羟基自由基(^·OH),从而降解有机污染物。基于相似的机理,过渡金属离子(Fe²⁺、Co²⁺和Ag⁺等)也可与过硫酸盐反应生成氧化能力较强的硫酸根自由基(SO₄^·-),而被称之为类Fenton技术。传统Fenton技术存在Fe²⁺投加量多,产生的铁污泥多等缺点,因此,有学者将Fenton技术与电化学技术结合,使Fe²⁺在阴极得以持续再生,这就是广为关注的电-Fenton技术。同样地,类Fenton技术也遇到与传统Fenton技术相似的问题。借鉴电-Fenton技术的成功应用,基于硫酸根自由基的类电-Fenton技术应运而生。本文在介绍电-Fenton和类电-Fenton技术原理的基础上,概括了电-Fenton和类电-Fenton技术的主要类型及其改进方法,并就值得深入研究的问题和热点趋势进行了展望。     

水中挥发性有机物分析前处理技术研究进展

环境水体中挥发性有机物(VOCs)的种类繁多,含量在(ng/L～μg/L)范围内。本文总结了2003年以来测定水样中VOCs的8种前处理技术,包括顶空单液滴微萃取(HS-SDME)、中空纤维液相微萃取(HF-LPME)、分散液液微萃取(DLLME)、顶空固相微萃取(HS-SPME)、搅拌棒吸附萃取(SBSE)、静态顶空(HS)、吹扫捕集法(P&T)和针式毛细管吸附阱(INCAT)的进展情况。比较了它们的优缺点,并展望了VOCs的分析方法。     

缺陷金属有机骨架的制备及其去除水中污染物的研究进展

在避免母体结构坍塌的前提下,通过缺陷工程对金属有机骨架(MOFs)进行处理可有效提升其去除水体污染物的性能。目前,通过调整合成条件(温度、金属/配体比例等)、添加调制剂、热处理和金属节点取代等方式可制备缺陷MOFs。粉末X射线衍射(PXRD)、比表面积分析、热重-差热分析(TGA-DSC)、电子顺磁共振(EPR)、X射线光电子能谱(XPS)、高分辨率透射电子显微镜(HR-TEM)、球差校正透射电镜(AC-TEM)和X射线吸收光谱(XAS)表征技术可证实MOFs中缺陷的特征。相比原始MOFs,从光催化等高级氧化的角度来看,构造缺陷型MOFs可促进电子转移、减小带隙以提升其高级氧化降解去除污染物的性能。此外,缺陷型MOFs还可为污染物提供更多吸附位点,进一步提升吸附剂的吸附容量和吸附速率。本文系统总结缺陷MOFs的制备方法、现有常见表征技术及其在水处理领域中的应用。同时,本文还根据缺陷MOFs用于去除水中污染物的研究现状对其今后发展予以展望。     

反渗透系统的经济运行与维护

广东中山发电A厂两套设计出力50T/h的反渗透系统(RO)自1997年12月投产以来已运行6年多时间,其间进行了多次清洗,清洗后系统投入运行所测数据达到系统正常运行标准,其清洗后的出力达到50T/h左右。根据国内外理论介绍,反渗透系统中反渗透膜随运行时间增加,系统产水量年递减10%,显然该厂的反渗透系统在经济运行方面取得了很好的成绩。     

Aroma Profile and Chemical Composition of Reverse Osmosis and Nanofiltration Concentrates of Red Wine Cabernet Sauvignon

Wine aroma represents one of the main properties that determines the consumer acceptance of the wine. It is different for each wine variety and depends on a large number of various chemical compounds. The aim of this study was to prepare red wine concentrates with enriched aroma compounds and chemical composition. For that purpose, Cabernet Sauvignon red wine variety was concentrated by reverse osmosis (RO) and nanofiltration (NF) processes under different operating conditions. Different pressures (2.5, 3.5, 4.5 and 5.5 MPa) and temperature regimes (with and without cooling) were applied on Alfa Laval LabUnit M20 equipped with six composite polyamide RO98pHt M20 or NF M20 membranes. Higher pressure increased the retention of sugars, SO₂, total and volatile acids and ethanol, but the temperature increment had opposite effect. Both membranes were permeable for water, ethanol, acetic acid, 4-ethylphenol and 4-ethylguaiacol and their concentration decreased after wine filtration. RO98pHt membranes retained higher concentrations of total aroma compounds than NF membranes, but both processes, reverse osmosis and nanofiltration, resulted in retentates with different aroma profiles comparing to the initial wine. The retention of individual compounds depended on several factors (chemical structure, stability, polarity, applied processing parameters, etc.).     

Influence of Substitutional Defects in ZIF-8 Membranes on Reverse Osmosis Desalination: A Molecular Dynamics Study

In this study, molecular dynamics simulation is used to investigate the effects of water-based substitutional defects in zeolitic imidazolate frameworks (ZIF)-8 membranes on their reverse osmosis (RO) desalination performance. ZIF-8 unit cells containing up to three defect sites are used to construct the membranes. These substitutional defects can either be Zn defects or linker defects. The RO desalination performance of the membranes is assessed in terms of the water flux and ion rejection rate. The effects of defects on the interactions between the ZIF-8 membranes and NaCl are investigated and explained with respect to the radial distribution function (RDF) and ion density distribution. The results show that ion adsorption on the membranes occurs at either the nitrogen atoms or the defect sites. Complete NaCl rejection can be achieved by introducing defects to change the size of the pores. It has also been discovered that the presence of linker defects increases membrane hydrophilicity. Overall, molecular dynamics simulations have been used in this study to show that water-based substitutional defects in a ZIF-8 structure reduce the water flux and influence its hydrophilicity and ion adsorption performance, which is useful in predicting the type and number of defect sites per unit cell required for RO applications. Of the seven ZIF-8 structures tested, pristine ZIF-8 exhibits the best RO desalination performance.     

高浓度含酚废水中酚类的转化回收及脱除

以含量30 g/L的苯酚水溶液为模型,提出氯化联合氧化工艺,实现对高浓度含酚废水中苯酚的转化回收及残余酚类的氧化脱除。 首先以pH值作为指示,向溶液中引入足够量的氯离子和氢离子,通过加入氯酸钠与之反应定量产生氯气;在所控制的实验条件下,氯气与溶液中的苯酚选择性反应转化为低溶解度的三氯苯酚沉淀,经气相色谱-质谱（GC-MS）面积归一法测得其含量可达97.76%;过滤所得滤液化学需氧量（COD）降低至1125 mg/L,苯酚回收率约98.7%。 采用Fenton氧化技术对该滤液进行氧化降解,结果表明,在优化的实验条件pH=3、Fe2+浓度为1 mmol/L下,H2O2用量为15 mL/L时,残余的氯酚类即可以被有效降解,降解后的水样经调碱性将铁或亚铁离子沉淀后为无色透明的溶液;联合处理后,水样COD减小到52 mg/L,该值满足国家工业污水排放标准。     

添加共试剂改善聚酰胺复合反渗透膜的性能

将N,N′-二甲基乙酰胺(DMAc)作为共试剂添加在间苯二胺水溶液中参与界面聚合反应, 以改善聚酰胺复合反渗透膜(PA-RO-x, x代表添加DMAc的质量分数)的性能. X射线光电子能谱(XPS)和衰减全反射傅里叶红外光谱(ATR-FTIR)分析表明, 随着DMAc含量的增加, 复合膜结构中交联聚酰胺含量相对于线性羧基部分有所增加; 场发射扫描电子显微镜(FE-SEM)和原子力显微镜(AFM)表征结果显示, 随着DMAc含量的增加, 膜表面的粗糙程度逐渐增大; 静态水接触角测试结果表明, 添加DMAc后, 膜的亲水性增强. 结合上述测试结果发现, 添加DMAc可以有效降低水油两相的不相溶性, 提高水相中间苯二胺向正己烷中扩散的速率, 这有助于加快间苯二胺与均苯三甲酰氯反应; 同时, 聚酰胺结构中交联酰胺含量的增加可以提供更多的氢键位点, 有助于水分子快速渗透通过复合膜而不损失截盐率; 膜表面的粗糙程度变大, 有助于提高水通量. 在2 g/L的氯化钠溶液和1.6 MPa测试压力条件下, PA-RO-5.2(DMAc添加质量分数为5.2%)的渗透通量和截盐率分别为66.1 L/(m²·h)和98.7%, 与未添加DMAc的聚酰胺复合反渗透膜相比, 通量增加115%, 截盐率仅下降0.9%.     

铁基金属-有机骨架及其复合物高级氧化降解水中新兴有机污染物

新兴有机污染物(Emerging organic contaminants,EOCs)是对人体健康及生态环境具有潜在或实质威胁的新型化学污染物.由于其被频繁使用且能在水生生态系统中持久性存在而对水生生物健康和安全造成严重威胁,故引起大众越来越多的关注.以活性污泥法为代表的传统水处理工艺通常不足以消除这些新兴有机污染物....     

静电纺丝复合反渗透膜的改性制备与脱盐性能

利用静电纺丝技术在无纺布上制备PET纳米纤维膜, 并用交联壳聚糖对其进行改性得到壳聚糖改性纳米纤维复合膜. 以间苯二胺(MPD)和均苯三甲酰氯(TMC)为单体, 采用界面聚合法在壳聚糖改性纳米纤维复合膜的表面制备聚酰胺分离层, 得到新型静电纺丝纳米纤维基复合反渗透膜. 新型复合反渗透膜具有典型的聚酰胺复合反渗透膜的表面脊-谷结构. 从膜的表面形貌、 亲水性、 分离性能等3个方面对水相MPD溶液中阴离子表面活性剂十二烷基苯磺酸钠(SDBS)的含量对膜结构和性能的影响进行了系统研究. 结果表明, SDBS的含量对膜形态结构的均匀性和亲水性有一定影响, 且随着SDBS含量的增加, 膜的脱盐率先增大后减小, 而通量小幅度上升后, 先减小后增大, 呈现规律性变化.     

苦咸水反渗透淡化中膜面结垢预测及防垢进展

苦咸水反渗透（BWRO）中的防垢过程,首先取决于给水水质,而根据水质条件和垢在膜面的形成机理采取相应的防垢措施是非常重要的。 显然,有效地管控膜面无机结垢及抑制膜面污染需要开展无机结垢趋势的预测、防垢措施和非破坏性无机垢监控等方面的技术研究。 一系列传统和新兴的分析技术,包括摩尔比率法、直接目测法和光谱法等已应用于BWRO过程中膜面防垢研究。 本文详细综述了该过程中无机结垢趋势的预测、防垢方法和非破坏性无机垢监控技术等方面的研究进展。 此外,针对目前的研究方向提出了建议。     

Removal of Natural Organic Matter by Forward Osmosis Membrane: Flux Behaviour and Foulant Characterization

Fouling of cellulose triacetate(CTA) forward osmosis(FO) membranes by natural organic matter(NOM) was studied by means of a cross-flow flat-sheet forward osmosis membrane system. The NOM solution was employed as the feed solution(FS), and a sodium chloride solution(3 mol/L) was used for the draw solution(DS). The process was conducted at various temperatures and cross-flow velocities. The flux decline was investigated with 3 h forward osmosis operation. The substances absorbed on the membranes were cleaned by ultrasonic oscillation of the fouled membranes and were characterized by methodologies including fluorescence excitation-emission matrices (EEMs) and liquid chromatography with an organic carbon detector(LC-OCD), and the variations of membrane properties were also investigated by Fourier transform infrared spectrometer(FTIR) and a contact angle meter. It was noted that the rejection efficiency of NOM is remarkable and that ultrasonic oscillation is an effective method to extract the NOM fouled on the CTA membranes after FO process. A higher cross-flow velocity and lower temperature benefit the anti-fouling capacity of the membrane significantly. Although humic substances accounted for the majo- rity of the NOM, aromatic proteins and amino acids were the main fouling components on the membranes, with symbolic FTIR peaks at 2355, 1408 and 873 cm^-1. The present surface foulant made the membranes becoming more hydrophilic, as demonstrated by a significant decrease in contact angle(ranging from 20% to 46%) under all the operation conditions.     

Removal of Flotation Collector O-Isopropyl-N-ethylthionocarbamate from Wastewater

Flotation collector O-isopropyl N-ethylthionocarbamate (IPETC) is widely used for separation of sulfide ores. Its removal from water by several oxidation processes was studied. Photocatalytic oxidation with air in the presence of iron salts, utilizing solar irradiation or artificial UV-A light is very efficient. Oxidation leads through the formation of O-isopropyl N-ethylcarbamate and several other reaction intermediates to total decomposition of organic compound in the final stage in 1 day. Similar results were obtained with a Fenton type oxidation with hydrogen peroxide and iron salts. Treatment with sodium hypochlorite yields mainly O-isopropyl N-ethylcarbamate. The formation of this compound in wastewaters can be of concern, since simple alkyl carbamates are cancer suspect agents.