饮用水中含氮消毒副产物卤代腈(氰)的生成特性与控制研究进展

卤代腈(氰)是水处理过程中产生的一类含氮的氯化消毒副产物。鉴于这种物质有极强的致畸和致突变性,其细胞毒性也远大于三卤甲烷和卤乙酸等常规消毒副产物,因此成为近年来饮用水中颇受关注的含氮消毒副产物种类之一。卤代腈(氰)在水厂出厂水中被大量检出,其质量浓度基本维持在μg/L,而采用氯胺消毒的出厂水中其浓度明显高于自由氯消毒方式。重点对卤代腈(氰)的物质种类、理化特性、遗传毒性、生产机制、检测方法及控制方法进行综述。鉴于多数卤代腈(氰)类消毒副产物均具有含量低、亲水性强等特点,若生成将难以在饮用水处理工艺中有效去除,因此如何有效控制其生成是卤代腈(氰)研究的主要发展方向。     

河流型水源地源水典型氯化消毒副产物及其前体物的强化去除工艺

以长三角某典型河流型水源地源水为研究对象,设计了传统工艺及基于凹凸棒土处理单元的6种强化工艺,对各工艺及其处理单元应用于典型氯化消毒副产物(三卤甲烷和卤乙酸)及其前体物控制的技术和经济可行性进行了系统分析。结果表明,预O3+凹土强化混凝+O3-GAC强化的工艺对上述2种消毒副产物及其前体物的控制效果最佳;在传统工艺中单纯增加O3处理也能在一定程度上提高其对消毒副产物前体物的去除效果;KMnO4控制消毒副产物的效果一般,但KMnO4处理可强化后续单元对消毒副产物前体物的去除效果。各工艺处理出水中三卤甲烷和卤乙酸单项指标均能达标,但传统工艺和经凹土强化混凝+GAC强化的工艺出水三卤甲烷4种化合物的实测浓度与其各自限值的比值之和均大于1.0,不能满足水质要求,必须进行强化处理。凹土强化混凝单元在6种强化工艺条件下对三卤甲烷生成潜能(THMFP)和卤乙酸生成潜能(HAAFP)的去除率较传统混凝单元平均提高15.99%和4.92%;各强化工艺对THMFP和HAAFP的去除率较传统工艺均提高20%以上(除凹土强化混凝+GAC强化的工艺外),消毒副产物产生量降低40%以上,工艺成本降低20%以上。     

水源地生态工程对消毒副产物生成的影响

水源地生态工程可改善饮用水水源水质,但其中的水生生物代谢物可能是消毒副产物(DBPs)前体物的来源。本文构建现场实验装置探究了水源地生态工程对原水水质的影响及原水中主要消毒副产物前体物的来源,考察了氯投量、温度以及pH对香蒲根分泌物、菰根分泌物和鲢鱼排泄物氯化后消毒副产物生成的影响。结果表明,实验装置对NH₄⁺-N、TN和TP的平均总去除率分别为74.93%、53.98%和73.02%,总DOC沿程增加。溶解性有机物(DOM)中分子质量分布在<500 Da的DOC含量总体上呈沿程减少的趋势,>3 000 Da的DOC沿程有所增加。总三卤甲烷生成势(TTHMFP)和总卤乙酸生成势(THAAFP)沿程呈现增加的趋势,分子质量<3000Da的有机物中TTHMFP和THAAFP沿程有所下降,分子质量>3 000 Da的TTHMFP和THAAFP呈沿程增加的趋势。考察了装置中3种水生生物代谢物经氯化后得到的二氯乙酸(DCAA)、三氯乙酸(TCAA)、三氯甲烷(TCM)和二氯乙腈(DCAN)4种消毒副产物生成势,均随着氯投量和温度...     

芳香类有机物氯化生成消毒副产物的特性研究

选择有代表性的芳香类有机物,在含有腐殖酸的水溶液中进行氯化试验.测定三卤甲烷和卤乙酸的生成特性.并分析有机物的化学结构对生成消毒副产物的影响.结果表明.各受试物氯化生成消毒副产物的活性和反应速率排序为间苯二酚>对苯二酚>邻苯二酚>苯酚>苯胺>苯甲酸>硝基苯;芳香类有机物苯环上官能团的性质、数量和位置等影响消毒副产物的生成;间苯二酚的氯化反应可分为快速反应阶段和慢速反应阶段.     

预氯化及常规工艺对消毒副产物的影响

以天津市某给水厂的水源水为实验对象,通过在实验室规模上模拟的给水处理厂工艺流程,比较了3种不同工艺流程中各单元出水的三卤甲烷(THMs)、卤乙酸(HAAs)和总有机物(TOC)浓度变化,分析了水处理单元工艺和TOC浓度对消毒副产物的影响。结果表明,预氯化生成的三卤甲烷和卤乙酸分别占最终出水中三卤甲烷和卤乙酸浓度的55.7%和66.7%,说明预氯化对出厂水中消毒副产物的产生有显著影响;混凝沉淀和过滤对三卤甲烷的去除率分别为17.2%和19.6%,而卤乙酸在水处理过程中变化不大,仅在过滤之后降低了3.32μg/L,说明过滤对三卤甲烷和卤乙酸均有一定的去除作用,而混凝沉淀仅对三卤甲烷有一定的去除作用;TOC浓度经过水处理工艺后整体呈下降趋势,但分析表明,其浓度对三卤甲烷和卤乙酸的生成影响很小,而氯则是三卤甲烷和卤乙酸生成的重要限制因素。     

活性炭对天然有机物氯化过程消毒副产物生成的影响及作用机制

活性炭(AC)与氯均为水处理过程中广泛使用的药剂,在实际使用过程中二者的接触不可避免,因此,深入研究AC对于氯化过程中消毒副产物(DBPs)生成的影响对于饮用水安全有重要意义。本研究对比了AC对于溶解性天然有机物(DOM)氯化过程中已知DBPs(包括三卤甲烷(THMs)和卤乙酸(HAAs))生成释放的影响,并采用傅立叶变换离子回旋共振质谱(FTICR-MS)技术检测分析其滤后水的未知氯化副产物及有机物变化规律。结果表明,在DOM氯化过程中,AC存在时释放的THMs和HAAs浓度较低,但氯的衰减速率更快,这是由于AC本身的强还原性及其他氯代副产物生成导致的。进一步通过FTICR-MS分析未知氯代产物及DOM的变化发现,在2种条件下有163种相同的氯化产物,与不存在AC时对比,AC存在时生成了不同的氯化产物中有57种。此外,AC存在时CHOCl、CHONCl和CHONSCl分子式的数量减少,而CHOSCl分子式的数量增加,并且具有芳香结构的DOM更容易被转化。通过电子自旋共振谱仪(ESR)分析发现AC表面的持久性自由基激发次氯酸钠反应生成的氯自由基(Cl·)是导致氯化产物变化的主要原因。本...     

臭氧对饮用水管网中溶解性有机物的影响

利用生物膜环状反应器模拟配水管网系统,将水厂砂滤池出水经过臭氧氧化后投加氯然后进入该模拟管网,另外把水厂砂滤池出水加氯后通入另一模拟管网作为对照实验。通过对两管网出水余氯、总铁、浊度、溶解性有机物(DOC)、以及消毒副产物三卤甲烷(THMs)、卤乙酸(HAAs)生成情况的测定,研究了饮用水臭氧处理对管网出水水质的影响。单因素方差分析结果表明,两管网出水的余氯、总铁、浊度以及THMs、HAAs含量相差不大,但DOC在臭氧氯管网中消耗较多。同时通过高效凝胶色谱(HPSEC),红外光谱(FTIR)和三维荧光光谱(EEM)表征了不同管网进出水DOC变化,结果表明,臭氧氧化后的管网出水中溶解性有机物荧光光谱中三区富里酸和五区腐植酸荧光峰值(ФⅢ+Ⅴ,n)减小较多,管网出水消毒副产物稍有增加。     

饮用水氯化消毒副产物的分析检测方法

氯化消毒饮用水中普遍存在消毒副产物 (DBPs) ,其中主要的是三卤甲烷和卤乙酸。文章在大量国内外文献调研的基础上 ,综述了饮用水氯化消毒 DBPs的种类及副作用 ,并对主要 DBPs的预处理技术和检测方法进行了系统的介绍和比较 ,为在不同实验条件下选择 DBPs的分析检测方法提供了指导。     

O3/ H2O2法对生化出水中不同种类有机物的去除效果研究

采用XAD-8/XAD-4吸附树脂联用技术将城市污水生化出水中有机物分为疏水酸、非酸疏水物质、弱疏水物质及亲水物质4类有机物,研究了O3/H2O2法对这4类有机物的去除效果.结果表明:(1)O3/H2O2法对生化出水中有机物的去除效果明显好于O3法、H2O2法.反应60 min时,O3/H2O2法对溶解有机碳(DOC)和254 nm波长处的单位比色皿光程下的紫外吸光度(UV254)的去除率分别达到49%和82%.(2)生化出水经O3/H2O2处理后,一部分疏水性有机物(疏水酸和非酸疏水物质)在反应过程中转化为亲水性有机物(弱疏水物质和亲水物质).(3)生化出水中71%的三卤甲烷生成势(THMFP)由疏水酸和亲水物质产生,特别是疏水酸,其产生的THMFP占总量的48%.反应60 min时,O3/H2O2法对疏水酸、非酸疏水物质、弱疏水物质和亲水物质产生的THMFP的去除率分别为64%、100%、88%和18%.     

经氯胺消毒的高溴碘水体中极性卤代消毒副产物的生成及鉴定

本研究以中国南方某沿海地区易受海水入侵影响的自来水厂和污水处理厂出水为研究对象,通过建立基于液液萃取与超高效液相色谱/电喷雾电离-三重四级杆质谱的分析方法,快速选择性地检测这类含高质量浓度溴离子、碘离子的水体在氯胺消毒过程中生成的极性卤代消毒副产物。结果表明,通过设置子离子m/z79/81和m/z 127,对母离子进行扫描,在氯胺消毒后的2种水样中检测出了10种极性溴代消毒副产物和19种极性碘代消毒副产物。通过对同位素丰度比和子离子碎片的分析,首次提出了2种溴代消毒副产物和4种碘代消毒副产物的分子结构。此外,对比自来水厂和污水厂出水的总离子强度可以发现,污水厂出水中生成的极性卤代消毒副产物,特别是卤代含氮消毒副产物的种类和数量显著高于自来水厂出水。     

A fingerprint analysis method for characterization of dissolved organic matter in secondary effluents of municipal wastewater treatment plant

Dissolved organic matter (DOM) in wastewater and reclaimed water is related to water quality, safety, and treatability. In this study, DOM was characterized through a fingerprint analysis method for DOM characterization using resin fractionation followed by size exclusion chromatography (SEC). Resin fractionation was used in the first step to divide the DOM in water samples into six resin fractions, namely, hydrophobic acids (HOA), hydrophobic bases (HOB), hydrophobic neutrals (HON), hydrophilic acids (HIA), hydrophilic bases (HIB), and hydrophilic neutrals (HIN). SEC analysis was then performed to separate each resin fraction into several (n) subfractions with different molecular weights (MW). Thus, the total DOM in the water sample was fractionated into 6n subfractions. After quantification of each subfraction by dissolved organic carbon (DOC), a fingerprint graph was constructed to express the distribution of DOM in the subfractions. The fingerprint analysis method was applied to a secondary effluent sample during ozonation. Ozonation (dose of 10 mg L^?1) removed the DOC only by 8 % and reduced UV₂₅₄ of the sample by 36 %. Fingerprint graphs also revealed that the resin fractions changed quite limitedly but transformation of subfractions occurred notably.     

Disinfection by-products in Finnish drinking waters

Disinfection by-products (DBPs) were measured in plant effluents of 35 Finnish waterworks, which utilized different treatment processes and raw water sources. DBPs were measured also from the distribution systems of three waterworks. Di- and trichloroacetic acids, and chloroform were the major DBPs found in treated water samples. The concentration of six haloacetic acids (HAA6) exceeded the concentrations of trihalomethanes (THMs). Chlorinated drinking waters (DWs) originating from surface waters contained the highest concentration of HAA6 and THMs: 108 and 26 microg/l, respectively. The lowest concentrations of DBPs were measured from ozonated and/or activated carbon filtrated and chloraminated DWs. Higher concentrations of HAA6, THMs, and adsorbable organic halogens were measured in summer compared to winter. The levels of chlorinated acetic acids, chloroform, and bromodichloromethane correlated positively with mutagenicity. Past mutagenicity levels of DWs were examined. A major reduction in the use of prechlorination, increased use of chloramine disinfection, and better removal of organic carbon were the most important reasons for the 69% decrease in mutagenicity from 1985 to 1994.     

The formation and control of disinfection by-products using chlorine dioxide

In this study, chlorine dioxide (ClO2) was used as an alternative disinfectant with vanillic acid, p-hydroxybenzoic acid, and humic acid as the organic precursors in a natural aquatic environment. The primary disinfection by-products (DBPs) formed were trihalomethanes (THMs) and haloacetic acids (HAAs). Under neutral conditions (pH = 7) for vanillic acid, more total haloacetic acids (THAAs) than total trihalomethanes (TTHMs) were found, with a substantial increase during the later stages of the reaction. In the case of p-hydroxybenzoic acid, the amount of THAAs produced was minimal. Raising the concentration of ClO2 was not favorable for the control of THAAs in low concentrations of vanillic acid. ClO2 could reduce the total amount of TTHMs and THAAs for higher concentration of vanillic acid. It was found that the humic acid treatment dosage was not significant. Under alkaline conditions (pH = 9), the control of TTHMs and THAAs for the treatment of vanillic acid was better and more economical, however, an appreciable amount of inorganic by-products were observed. Under the same alkaline condition, the control of THAA for the treatment of p-hydroxybenzoic acid was not beneficial and for the treatment of humic acid was not significant.     

Minimization of the formation of disinfection by-products

The drinking water industry is required to minimize DBPs levels while ensuring adequate disinfection. In this study, efficient and appropriate treatment scheme for the reduction of disinfection by-product (DBPs) formation in drinking water containing natural organic matter has been established. This was carried out by the investigation of different treatment schemes consisting of enhanced coagulation, sedimentation, disinfection by using chlorine dioxide/ozone, filtration by sand filter, or granular activated carbon (GAC). Bench scale treatment schemes were applied on actual samples from different selected sites to identify the best conditions for the treatment of water. Samples were collected from effluent of each step in the treatment train in order to analyze pH, UV absorbance at 254 nm (UVA₂₅₄), specific UV absorbance at 254 nm (SUVA₂₅₄), dissolved organic carbon (DOC), haloacetic acids (HAAs) and trihalomethanes (THMs). The obtained results indicated that using pre-ozonation/enhanced coagulation/activated carbon filtration treatment train appears to be the most effective method for reducing DBPs precursors in drinking water treatment.     

The fate and importance of organics in drinking water treatment: a review

In the pioneer days, the main driving forces for research of organics in drinking water treatment (DWT) were human health risks and optimisation of technology. The focus was on natural organic matter (NOM) structure, disinfection by-products (DBPs) formation, NOM removal by means of coagulation, adsorption, and oxidation, and development of the most efficient water treatment trains. Surprisingly, after decades of research, rapid development of analytical techniques and progress in risk assessment, the same driving forces are still in the limelight — although the topics have changed slightly. The attention switched from trihalomethanes to a new generation of DBPs. The definition of hydrophilic/hydrophobic NOM depends on the technique used for characterisation. It has become evident that numerous organic compounds can threaten water supply sources. Some of them had been ignored or overlooked in the past, but have recently been detected by advanced analytical tools even in drinking water. Prioritisation becomes priority per se. As far as processes are concerned, mainstream research has been following three lines: fouling mechanisms, application of hybrid processes and interactions between synthetic organic chemicals, other water constituents and materials used in DWT. Significant development has been made in membrane technology. This paper presents a broad overview of the recent organics research. Although the state-of-the-art technologies seem to have an answer to each and every question raised, it is still necessary to deal with specific problems on a case-by-case basis mainly due to the unique nature of NOM and different xenobiotics that may appear in various types of waters. In the end, human health risk, which derives from the presence/absence of organics, is only the tip of the iceberg — underneath lies a whole new universe — the socio-economic aspect of water treatment and quality that deserves much more attention.     

The occurrence of disinfection by-products in the drinking water of Athens,Greece

Application of chlorination for the disinfection of drinking water results in the formation of a wide range of organic compounds, called disinfection by-products (DBPs), which occur due to the reaction of chlorine with natural organic materials. The occurrence of DBPs was studied in samples from four drinking-water treatment plants (WTPs) and from the distribution network of Athens, Greece. Twenty-four compounds, which belong to different categories of DBPs, were monitored, including trihalomethanes (THMs), haloacetic acids (HAAs), haloacetonitriles (HANs), haloketones (HAKs), chloral hydrate (CH) and chloropicrin (CP). Sampling was performed monthly for a period of two years, from three different points at each WTP and from eight points atthe distribution network. Samples were analyzed by GC-ECD methods, which included pretreatment with liquid-liquid extraction for volatile DBPs and acidic methanol esterification for HAAs. The results of the analyses have shown the presence of disinfection by-products belonging to all categories studied in all water samples collected after prechlorination. The major categories of DBPs detected were THMs and HAAs, while the other volatile DBPs occurred at lower concentrations. The concentrations of DBPs did not in any case exceed the maximum contaminant levels (MCL) set by USEPA and WHO. However, monitoring these compounds needs to be continued, because their levels could increase due to changes in the quality of water entering the water treatment plants. Reduction of the concentrations of DBPs could be achieved by optimization of the chlorination conditions, taking into account the effect of time. Moreover, research on alternative disinfection methods (e.g. ozone, chlorine dioxide, chloramines) and their by-products should be conducted to evaluate their applicability in the case of the drinking water of Greece.     

Particles in swimming pool filters--does pH determine the DBP formation?

The formation was investigated for different groups of disinfection byproducts (DBPs) during chlorination of filter particles from swimming pools at different pH-values and the toxicity was estimated. Specifically, the formation of the DBP group trihalomethanes (THMs), which is regulated in many countries, and the non-regulated haloacetic acids (HAAs) and haloacetonitriles (HANs) were investigated at 6.0≤pH≤8.0, under controlled chlorination conditions. The investigated particles were collected from a hot tub with a drum micro filter. In two series of experiments with either constant initial active or initial free chlorine concentrations the particles were chlorinated at different pH-values in the relevant range for swimming pools. THM and HAA formations were reduced by decreasing pH while HAN formation increased with decreasing pH. Based on the organic content the relative DBP formation from the particles was higher than previously reported for body fluid analogue and filling water. The genotoxicity and cytotoxicity estimated from formation of DBPs from the treated particle suspension increased with decreasing pH. Among the quantified DBP groups the HANs were responsible for the majority of the toxicity from the measured DBPs.     

Influence of pH and ozone dose on the content and structure of haloacetic acid precursors in groundwater

This study investigated the effects of pH (6-10) and ozone dose [0.4-3.0?mg O(3)/mg dissolved organic carbon (DOC)] on the content and structure of haloacetic acid (HAA) precursors in groundwater rich in natural organic matter (NOM; DOC 9.85?±?0.18?mg/L) during drinking water treatment. The raw water was ozonated in a 2 L glass column. NOM fractionation was carried out using XAD resins. HAA formation potential (HAAFP) was determined according to standard EPA Method 552. NOM characterization revealed it is mostly hydrophobic (65?% fulvic and 14?% humic acids). Hydrophobic NOM significantly influences HAA formation, as confirmed by the high HAAFP (309?±?15?μg/L). Ozonation at pH?6-10 led to changes in NOM structure, i.e. complete humic acid oxidation, and increased the hydrophilic NOM fraction content (65-90?% achieved using 3.0?mg O(3)/mg DOC). The highest degree of NOM oxidation and HAA precursor removal was achieved at pH?10 (up to 68?% HAAFP). Ozonation pH influenced the distribution of HAA precursor content, as increasing the pH from 6 to 10 increased the reactivity of the hydrophilic fraction, with the HAAFP increasing from 19.1?±?6.0?μg/mg DOC in raw water to 152?±?8?μg/mg DOC in ozonated water. The degree of HAA precursor removal depends on the dominant oxidation mechanism, which is related to the applied ozone dose and the pH of the oxidation process. Ozonation at pH?10 favours the mechanism of radical NOM oxidation and was the most effective for HAAFP reduction, with the efficacy of the process improving with increasing ozone dose.