微污染水源中的氨氮及其处理技术

目前,我国饮用水水源部分呈现微污染特征.根据中国环保总局颁布的<环境状况公报>的近年来数据,可知水体中污染物之一氨氮已不容忽视.文中介绍了水中氨氮的来源、存在形态以及对水质、水处理工艺和人体健康的影响.对比了国内外饮用水标准中对"三氮"的规定,同时建议我国饮用水标准中宜逐步规定饮用水氨氮浓度的限值.并对目前处理微污染水源水中氨氮的曝气法、折点加氯法、离子交换法及生物预处理法等作了讨论.     

氯化消毒副产物2,2,4-三氯-5-甲氧基-环戊-4-烯-1,3-二酮的合成及结构确认

以七氯丙烷为原料,合成了氯化消毒副产物--2,2,4-三氯-5-甲氧基-环戊-4-烯-1,3-二酮(TCMCD),总收率为13%,产品纯度在98%以上.通过质谱、核磁共振、红外光谱等对TCMCD进行表征,进一步确认了副产物的结构.     

Simultaneous removal of ammonia and N-nitrosamine precursors from high ammonia water by zeolite and powdered activated carbon

When adding sufficient chlorine to achieve breakpoint chlorination to source water containing high concentration of ammonia during drinking water treatment, high concentrations of disinfection by-products(DBPs) may form. If N-nitrosamine precursors are present, highly toxic N-nitrosamines, primarily N-nitrosodimethylamine(NDMA), may also form. Removing their precursors before disinfection should be a more effective way to minimize these DBPs formation. In this study, zeolites and activated carbon were examined for ammonia and N-nitrosamine precursor removal when incorporated into drinking water treatment processes.The test results indicate that Mordenite zeolite can remove ammonia and five of seven N-nitrosamine precursors efficiently by single step adsorption test. The practical applicability was evaluated by simulation of typical drinking water treatment processes using six-gang stirring system. The Mordenite zeolite was applied at the steps of lime softening, alum coagulation, and alum coagulation with powdered activated carbon(PAC) sorption. While the lime softening process resulted in poor zeolite performance, alum coagulation did not impact ammonia and N-nitrosamine precursor removal. During alum coagulation, more than67% ammonia and 70%–100% N-nitrosamine precursors were removed by Mordenite zeolite(except 3-(dimethylaminomethyl)indole(DMAI) and 4-dimethylaminoantipyrine(DMAP)). PAC effectively removed DMAI and DMAP when added during alum coagulation. A combination of the zeolite and PAC selected efficiently removed ammonia and all tested seven N-nitrosamine precursors(dimethylamine(DMA), ethylmethylamine(EMA), diethylamine(DEA), dipropylamine(DPA), trimethylamine(TMA), DMAP, and DMAI) during the alum coagulation process.     

Characteristics of molecular weight distribution of dissolved organic matter in bromide-containing water and disinfection by-product formation properties during treatment processes

The characteristics of dissolved organic matter (DOM) and bromide ion concentration have a significant influence on the formation of disinfection by-products (DBPs). In order to identify the main DBP precursors, DOM was divided into five fractions based on molecular weight (MW), trihalomethane formation potential and haloacetic acid formation potential were determined for fractions, and the change in contents of different fractions and total DBPs during treatment processes (pre-chlorination, coagulation, sand filtration, disinfection) were studied. Moreover, the relationship between bromide concentration and DBP generation characteristics in processes was also analyzed. The results showed that the main DBP precursors were the fraction with MW < 1 kDa and fraction with MW 3−10 kDa, and the DBP''s generation ability of lower molecular weight DOM (< 10 kDa) was higher than that of higher molecular weight DOM. During different processes, pre-chlorination and disinfection had limited effect on removing organics but could alter the MW distribution, and coagulation and filtration could effectively remove organics with higher MW. For DBPs, trihalomethanes (THMs) were mainly generated in pre-chlorination and disinfection, while haloacetic acids (HAAs) were mostly generated during pre-chlorination; coagulation and sand filtration had little effect on THMs but resulted in a slight removal of HAAs. In addition, the results of ANOVA tests suggested that molecular sizes and treatment processes have significant influence on DBP formation. With increasing bromide concentration, the brominated DBPs significantly increased, but the bromine incorporation factor in the processes was basically consistent at each concentration.     

The fate of prazosin and levonorgestrel after electrochemical degradation process: Monitoring by-products using LC-TOF/MS

Prazosin (PRZ) and levonorgestrel (LNG) are widely used as an anti-disease drugs due to their biological activity in the human body. The frequent detection of these compounds in water samples requires alternative technologies for the removal of both compounds. After electrochemical degradation of PRZ and LNG, the parent compounds could be completely removed after treatment, but the identification and characterization of by-products are necessary as well. In this study, the effects of NaCl concentration and applied voltage were investigated during the electrochemical degradation process. The results revealed that the increase of NaCl concentration and applied voltage could promote the generation of hypochlorite OCl? and then enhance the degradation of PRZ and LNG. After initial study, 6 V and 0.2 g NaCl were selected for further experiments (96% and 99% removal of PRZ and LNG after 40 min, respectively). Energy consumption was also evaluated and calculated for PRZ and LNG at 3, 6 and 8 V. Solid phase extraction (SPE) method plays an important role in enhancing the detection limit of by-products. Furthermore, characterization and identification of chlorinated and non-chlorinated by-products were conducted using an accurate liquid chromatography-time of flight/mass spectrometry LC-TOF/MS instrument. The monitoring of products during the electrochemical degradation process was performed at 6 V and 0.2 g NaCl in a 50 mL solution. The results indicated that two chlorinated products were formed during the electrochemical process. The toxicity of by-products toward E. coli bacteria was investigated at 37°C and 20 hr incubation time.     

硫自养反硝化过程中含硫副产物产生规律及微生物群落结构的空间分布

为探究硫自养反硝化过程中含硫副产物的产生规律,建立了上流式硫自养固定床生物反应器,考察HRT（水力停留时间）对水中NO₃--N去除的影响,运用零级和1/2级反应动力学模型对NO₃--N还原过程进行拟合,通过测定与理论计算分析含硫副产物的产生趋势及规律,利用高通量测序技术（high-throughput sequencing）测定微生物群落结构空间分布特征.结果表明:①当进水NO₃--N浓度为（30.45±0.38）mg/L,HRT为4和1 h时,NO₃--N去除率达到98%以上.硫自养反硝化过程符合1/2级反应动力学模型,1/2K_1/2V（1/2级反应动力学速率常数）为5.69 mg1/2/（L1/2·h）.②出水SO₄2-的产生量接近理论值,S2-在反应器中部出现微量的积累,在出水口处浓度进一步降低（< 0.5 mg/L）.③HRT的缩短改变了反应器内部微生物群落α多样性的变化规律;Proteobacteria成为了最主要的优势菌群,各阶段所占比例均大于59%,Sulfurimonas为最常见的反硝化菌,在HRT为1 h时,反应器中部其丰度达到36%,成为反应器中的优势菌属;Desulfurella为SRB（硫酸盐还原菌）,其丰度的增加与反应器内部S2-的积累一致.研究显示,硫自养反硝化过程中产生的SO₄2-与理论值接近,S2-产生量沿反应器高度方向呈现先增加后降低的趋势,微生物群落结构分布情况与反应器高度有关.      

加氯消毒过程中纯细菌物质生成消毒副产物研究

按照UFC方法对水体中3种常见细菌Acinetobacter junii、Staphylococcussciuri和Escherichia coli进行纯细菌加氯消毒处理,同时考察水中溴离子对纯细菌物质生成DBPs的影响.结果表明,3种细菌均为DBPs前体物,加氯消毒生成的DBPs除水合三氯乙醛(CHD)外,生成的三卤甲烷(THMs)物质主要为氯仿(TCM),卤乙腈(HANs)物质主要为二氯乙腈(DCAN).氯仿的生成量与细菌物质TOC浓度无明显关系,但HANs和CHD生成量均随细菌TOC浓度增大而增加.其中革兰氏阳性细菌Staphylococcus sciuri生成的DCAN和CHD比革兰氏阴性细菌Acinetobacter junii和Escherichia coli生成的要高,说明细胞壁的化学组分可能是DCAN和CHD生成的影响因素之一.Escherichia coli细菌反应液中溴离子(Br-)存在时,除生成CHD、TCM及DCAN外,THMs和HANs中的溴代种类CHBr3随Br-增多而持续增加,相反TCM持续减少.当Br-浓度为4mg.L-1时,TBM浓度增至最高127.9μg.L-1;HANs和CHD生成量随Br-浓度增加先有所增加,随后持续降低至低于检测限;Br离子存在时THMs为主要DBPs种类.     

饮用水氯消毒副产物控制技术研究进展

依据新颁布的《生活饮用水卫生标准》对饮用水氯消毒副产物控制技术进行了具体的论述,介绍了替代消毒剂、前体物去除和副产物去除等控制技术的应用效果和局限性,分析了安全高效的多级屏障组合消毒工艺在控制消毒副产物中的应用前景。     

快速混合法氯化消毒及其效果研究

本文提出了以固定混合器作为促进混合效果装置的快速混合法,并以E.Coli作为指示微生物、液氯作为消毒剂进行了研究。结果表明,均匀快速而剧烈的初始混合作用,可大大改善灭菌效果。在短至5秒的接触时间内即可达到99.99％以上的灭活效率。投氯量和接触时间对E.Coli灭活率的影响随混合程度的提高而减弱。与传统法相比,灭活率可提高100倍以上,投氯量可下降4—8倍,接触时间可大大缩短。     

腐植酸氯化过程中氯仿生成的基础研究

为了研究用氯消毒饮用水过程中产生氯仿等致癌性副产物,进行了采用低分子量腐植酸与次氯酸钠反应生成氯仿的实验,结果表明,在次氯钠浓度,ｐＨ和温度一定的条件,氯仿产量随腐植酸浓度的增大而增加,ｐＨ在７．３－９内,氯仿生成速度最快,ｐＨ大于９时,氯仿生成速率随ｐＨ的升高而下降,氯仿生成量与温度呈正相关关系,腐植酸氯化成氯仿的反应活化能国５１．８ＫＪ,因此设法降低原水中腐植酸含量量降低氯仿含量的有效方法。