两点短时游离氯后转氯胺的顺序氯化消毒工艺研究

基于顺序氯化消毒工艺的原理,采用两点短时游离氯后转氯胺的两点顺序氯化消毒工艺,即在过滤和清水池前的两点分别加氯,并在清水池加氯后立即加氨转化为氯胺消毒的工艺,该工艺在常规处理工艺的给水厂进行了消毒试验.结果表明,加氯点的适当提前,不仅有利于控制消毒副产物的生成量,而且有效抑制了滤池中的生物膜滋生.两点顺序氯化消毒工艺中生成的卤代消毒副产物比相同条件下一次性加入等量的氯消毒剂的消毒方法产生的三卤甲烷(THMs)平均减少了51.6％,卤乙酸(HAAs)平均减少了46.7％.细菌学指标HPC的结果也显示出了该工艺在保障水质的微生物安全方面的优势.     

污水处理中紫外消毒效果的研究

紫外消毒技术相对于氯化法消毒,能够快速、有效地去除污水中粪大肠杆菌,操作简单方面,无副产物生成,对周围环境和人员安全可靠,在中国许多污水处理厂都已取代氯化法消毒并广泛应用。阐述了紫外消毒和微生物光复活现象的原理,并通过大量试验来研究紫外消毒技术去除粪大肠杆菌的效果,及经紫外消毒后出水中粪大肠杆菌光复活现象对紫外消毒效果的影响,提出可采用出水避光排放、增加紫外照射剂量、延长照射时间等方法来控制微生物光复活现象。     

电化学消毒法对水中大肠杆菌的灭活特性

本研究通过电化学消毒小试装置,系统考察了电极板材料、极板间距、p H、水温、Na Cl浓度等因素对水中大肠杆菌CGMCC 1.3373灭活效果的影响,并进一步考察了电化学消毒对抗生素抗性大肠杆菌CGMCC 1.1595的灭活效果及其抗性变化.结果发现,在相同的电化学消毒条件下,阳极采用钌铱涂层的钛电极板的灭活效果显著优于铅涂层和铱钽涂层电极板,并且极板间距为50 mm时灭活率最高.进一步研究表明,电化学消毒法对大肠杆菌的灭活率随水的p H升高而降低,随水温和Na Cl浓度升高而升高.在相同消毒条件下,电化学法对四环素抗性大肠杆菌的灭活率显著低于普通大肠杆菌.消毒后存活的抗性菌对四环素、青霉素、氯霉素的抗性,随消毒时间延长呈现先下降后上升的规律.     

碘代乙酸体外暴露诱导斑马鱼(Danio rerio)淋巴细胞内源性凋亡可能机理研究

以斑马鱼(Danio rerio)为试验生物,经淋巴细胞体外暴露试验,从细胞内源性凋亡角度,研究了饮用水消毒副产物—碘代乙酸诱导斑马鱼淋巴细胞损伤的致毒机理.结果表明,在碘代乙酸的环境浓度1μg·L-1下暴露24、36、48和96 h后,细胞凋亡率从对照组的3.52%分别增加到15.89%、22.47%、40.76%和52.13%,与对照组差异均为极显著(p0.01);线粒体膜电位分别较对照组下降了32.9%、50.1%、68.6%和81.5%,与对照组差异均为极显著(p0.01);细胞色素C的相对释放量分别增加了0.85、1.37、1.86和2.66倍,与对照组差异均为极显著(p0.01).暴露36、48和96 h后,Caspase-3酶活性分别增加了0.49、0.86和1.43倍,与对照组差异均为极显著(p0.01);Caspase-9酶活性分别增加了0.73、1.41和1.88倍,与对照组差异均为极显著(p0.01);抑制凋亡Bcl-2基因的相对表达量分别下降27.0%、35.3%和52.3%,与对照组差异均为极显著(p0.01);而促进凋亡的Bax基因相对表达量分别增加1.1、2.3和3.2倍,与对照组差异均为极显著(p0.01).碘代乙酸体外诱导斑马鱼淋巴细胞凋亡的可能机制是,线粒体膜电位的崩溃导致细胞色素C持续从线粒体中释放,进而引起细胞凋亡下游通路的变化;Bcl-2基因和Bax基因明显参与了对凋亡的调控.此外,Caspase-9酶的活化导致Caspase-3酶活化,最终引起细胞凋亡.     

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。     

臭氧法在城市污水消毒中的应用

介绍了臭氧在水中的化学特性和消毒的基本原理,通过试验研究了臭氧在城市污水深度处理消毒中的反应过程,认为臭氧在城市污水处理二级出水中的消毒是可行的。     

再生水消毒副产物的检测、生成与控制

在水资源紧缺的当下,污水再生利用是一项重要的环保战略更是资源战略.消毒能有效杀灭病菌和阻断介水疾病的传播,是保障再生水用水安全的重要手段.然而,消毒剂会不可避免地与水中有机物发生反应形成具有毒害效应的消毒副产物.围绕污水在再生消毒过程中所产生的消毒副产物,针对其检测识别方法、生成条件（前体物、消毒工艺及水质条件对消毒副产物生成的影响）以及控制方法（源头控制、过程控制及末端控制）进行综述.在此基础上,对再生水消毒副产物的未来研究动态进行了探讨,可为保障再生水的安全利用提供依据.     

循环冷却水处理中臭氧的杀菌作用

臭氧作为强氧化剂可以用于循环冷却水的处理中.试验研究了影响臭氧杀菌的基本因素,冷却水的pH和水温对处理效果基本没有影响.臭氧的杀菌能力取决于水中的剩余臭氧浓度,臭氧的消耗量与系统中的微生物数量有关.当水中剩余臭氧浓度为0.05mg/L和接触时间为14min时,可以使臭氧的灭菌力达99%.即在循环冷却水系统中,投加0.05mg/L臭氧,就可以控制系统中微生物的生长.由此确定了循环水处理过程中为控制系统中微生物的生长所需维持的最低臭氧浓度.     

A photolysis coefficient for characterizing the response of aqueous constituents to photolysis

UV photolysis and UV based advanced oxidation processes (AOPs) are gaining more and more attention for drinking water treatment. Quantum yield (ø) and molar absorption coefficient (ε) are the two critical parameters measuring the effectiveness of photolysis of a compound. The product of the two was proposed as a fundamental measure of a constituent’s amenability to transformation by photolysis. It was shown that this product, named the photolysis coefficient, k _p , can be determined using standard bench tests and captures the properties that govern a constituent’s transformation when exposed to light. The development showed the photolysis coefficient to be equally useful for microbiological, inorganic and organic constituents. Values of k _p calculated by the authors based on quantum yield and molar absorption coefficient data from the literature were summarized. Photolysis coefficients among microorganisms ranged from 8500 to more than 600000 and are far higher than for inorganic and organic compounds, which varied over a range of approximately 10 to 1000 and are much less sensitive to UV photolysis than the microorganisms.     

Removal of organic matter and disinfection by-products precursors in a hybrid process combining ozonation with ceramic membrane ultrafiltration

The performance of an integrated process including coagulation, ozonation, ceramic ultrafiltration (UF) and biologic activated carbon (BAC) filtration was investigated for the removal of organic matter and disinfection by-products (DBPs) precursors from micro-polluted surface water. A pilot scale plant with the capacity of 120 m³ per day was set up and operated for the treatment of drinking water. Ceramic membranes were used with the filtration area of 50 m² and a pore size of 60 nm. Dissolved organic matter was divided into five fractions including hydrophobic acid (HoA), base (HoB) and neutral (HoN), weakly hydrophobic acid (WHoA) and hydrophilic matter (HiM) by DAX-8 and XAD-4 resins. The experiment results showed that the removal of organic matter was significantly improved with ozonation in advance. In sum, the integrated process removed 73% of dissolved organic carbon (DOC), 87% of UV₂₅₄, 77% of trihalomethane (THMs) precursors, 76% of haloacetic acid (HAAs) precursors, 83%of trichloracetic aldehyde (CH) precursor, 77% of dichloroacetonitrile (DCAN) precursor, 51% of trichloroacetonitrile (TCAN) precursor, 96% of 1,1,1-trichloroacetone (TCP) precursor and 63% of trichloronitromethane (TCNM) precursor. Hydrophobic organic matter was converted into hydrophilic organic matter during ozonation/UF, while the organic matter with molecular weight of 1000–3000 Da was remarkably decreased and converted into lower molecular weight organic matter ranged from 200–500 Da. DOC had a close linear relationship with the formation potential of DBPs.