二氧化氯消毒无机副产物的产生及控制

二氧化氯消毒的副产物(DBPs)主要以无机的亚氯酸根和氯酸根为主,其中亚氯酸根可能对人体健康产生负面影响。本文在国内外大量研究资料的基础上,结合我国应用二氧化氯的实践,分析了二氧化氯消毒无机副产物的产生及可行的去除方法,认为用亚铁还原法控制及去除亚氯酸根是一种经济合理行之有效的方法,同时对硫化物还原法、活性炭吸附法和臭氧氧化法的特点进行了比较,对二氧化氯消毒工艺的正确应用进行了探讨。     

传染病医院污水处理技术

针对传染病医院污水所含病菌的特点,采用“消毒+好氧生物接触氧化法+消毒”二级处理工艺对阳泉市“SARS”病医院污水进行了处理。系统运行结果表明:其出水各项指标均达到国标《污水综合排放标准》一级排放标准,取得了良好的环境和经济效益。     

Modeling the Formation of Chlorination By-Products During Enhanced Coagulation

Because of increasing need to balance health risks for pathogen control and disinfection by-products (DBP) formation in drinking water supplies, water utilities are forced to closely examine and optimize their disinfection practices. This research was designed to investigate the effects of independent variables of dissolved organic carbon (DOC), ferric chloride dosage, chlorine dose, and reaction time on trihalomethanes (THMs) formation in Terkos Lake Water (TLW) of Istanbul City. A statistically-based empirical model was developed for predicting THM formation during enhanced coagulation. The R ² and F value of model were 0.762 and 460, respectively. The model was found to be statistically significant for all four variables, and model predictions appear to be most accurate for this study. A multiple linear model exhibited the best fit of data. It was observed that THM formation depended primarily on DOC removal. Model calibration, testing and validation were accomplished by using independent data set.     

污水深度处理技术研究

通过对污水处理装置外排污水进行深度处理中试研究 ,在净化处理中采用沉淀、过滤 ,同时投加混凝剂、助凝剂 ,并采用二氧化氯消毒 ,处理后的污水达到了所定指标要求 ,可作为工业用水     

城镇污水二级处理和再生水三级处理过程的雌激素活性变化

环境雌激素污染与野生动物性别比例和繁殖密切相关,是人体生殖功能紊乱、发育异常、心血管疾病和癌症发生等的重要因素之一。针对污水处理厂排水造成的环境雌激素污染,采用重组酵母菌方法研究大连、沈阳、哈尔滨和天津的5个典型城市污水厂和再生水厂水处理过程中雌激素活性的变化规律,分析二级处理和再生水厂三级处理对环境雌激素的削减效率。4个采用活性污泥法和紫外消毒工艺的污水厂出水的雌激素当量(EEQ)为0.5～1.5 ng·L~(-1)。再生水厂三级处理工艺的出水雌激素活性低于检测限(0.02 ng·L~(-1))。分级组分测试结果显示,污水雌激素活性主要由强极性组分和弱极性组分引起,紫外消毒后强极性组分雌激素活性升高。4个城市污水处理厂一级处理和活性污泥处理对环境雌激素的削减率为46%～81%,紫外消毒的削减率为5.2%～22%。某再生水厂混凝、微滤和反渗透对环境雌激素的削减率分别为63%、16%和98%。研究表明,活性污泥法二级处理排水回用仍造成一定程度环境雌激素污染,三级处理工艺可有效提高环境雌激素污染物削减率。     

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。     

基于CFD的两种紫外消毒模型的比较研究

为了预测紫外反应器的消毒效率,提高模拟的准确度,对两种紫外光强模型进行了比较分析。利用CFD技术,采用数值模拟的方法,对线源和柱源两种光强模型进行了光强分布以及消毒效率的模拟,并采用生物实验进行了验证。结果表明:与柱源模型相比,线源模型在近灯管处强度高42.3%,在1.2 cm处二者趋于一致;针对同一管式紫外反应器,透光率为95%时,线源模型的模拟结果偏大,柱源结果偏小;透光率为80%时,线源及柱源模型的模拟结果都偏大,流量及模型影响较小,透光率成为主要影响因素。综合比较,柱源模型适用于小型管式紫外灯消毒数值模型的开发。     

二氧化氯应用于二次供水安全消毒的静态研究

采用二氧化氯（ClO2）作为二次供水的消毒剂进行静态实验研究,考察了ClO2投加量、氨氮与CODMn浓度及pH对ClO2衰减及消毒副产物氯酸盐（ClO3^-）和亚氯酸盐（ClO2）的生成影响,并建立了ClO3-和ClO2生成浓度的经验预测模型。结果表明：前4h内,随着消毒剂初始投加浓度提高,ClO2的衰减速率增加,4h后降解则较缓慢。ClO2加入水中,立即有ClO3^-与ClO2^-生成,4h后基本达到稳定,且随着药剂投加量的增加,ClO3^-和ClO2-的生成量逐渐增大。氨氮、CODMn及pH的升高,可加速ClO2的衰减,同时可促进ClO3^-和ClO2-的生成。其中,氨氮浓度从0．085mg／L升高到0．585mg／LClO3^-与ClO2-的生成浓度分别增加了6．49μg／L和8．32μg／L;CODMn从1．13mg／L升高到3．13mg／L,ClO3^-与ClO2-的生成浓度分别增加了13．75μg／L和9．23μg／L;pH从6．49升高到8．45,ClO3^-与ClO2-的生成浓度分别增加了13．28μg／L和10．01μg／L。     

氨氮浓度对次氯酸钠消毒中水的影响

研究了氨氮浓度对次氯酸钠消毒中水的影响,讨论了中水氨氮浓度、氯胺浓度、总余氯浓度、消毒接触时间和总大肠菌群指标的变化关系。结果表明,氨氮随消毒接触时间呈先降低再升高的趋势,中水氨氮浓度越高,其变化幅度越小,反之,则变化幅度较大;氯胺浓度随消毒接触时间的延长先升高再降低,而总余氯量则逐渐降低,并有一定的持续消毒作用;此外,总余氯随次氯酸钠投加量的增加呈先升高后降低再逐渐升高的趋势,整个反应过程符合折点加氯消毒理论;当次氯酸钠投加量与氨氮的比值（以后简称C1／N）为25／1时,氨氮消耗掉的次氯酸钠量最多,生成的总余氯量最少;当C1／N比大于25／1时,消毒后中水氨氮浓度为零,反之,则随C1／N比升高逐渐降低;而当氨氮浓度相同时,中水消毒达标的主要影响因素是水中总大肠菌群的数量。     

Inactivation and injury assessment of Escherichia coli during solar and photocatalytic disinfection in LDPE bags

Solar disinfection (SODIS) of Escherichia coli suspensions in low-density polyethylene bag reactors was investigated as a low-cost disinfection method suitable for application in developing countries. The efficiency of a range of SODIS reactor configurations was examined (single skin (SS), double skin, black-backed single skin, silver-backed single skin (SBSS) and composite-backed single skin) using E. coli suspended in model and real surface water. Titanium dioxide was added to the reactors to improve the efficiency of the SODIS process. The effect of turbidity was also assessed. In addition to viable counts, E. coli injury was characterised through spread-plate analysis using selective and non-selective media. The optimal reactor configuration was determined to be the SBSS bag (t₅₀ = 9.0 min) demonstrating the importance of UVA photons, as opposed to infrared in the SODIS disinfection mechanism. Complete inactivation (6.5-log) was achieved in the presence of turbidity (50 NTU) using the SBSS bag within 180 min simulated solar exposure. The addition of titanium dioxide (0.025 g L⁻¹) significantly enhanced E. coli inactivation in the SS reactor, with 6-log inactivation observed within 90 min simulated solar exposure. During the early stages of both SODIS and photocatalytic disinfection, injured E. coli were detected; however, irreversible injury was caused and re-growth was not observed. Experiments under solar conditions were undertaken with total inactivation (6.5-log) observed in the SS reactor within 240 min, incomplete inactivation (4-log) was observed in SODIS bottles exposed to the same solar conditions.