序批式曝气生物滤池处理含海水污水中的硝化性能

采用序批式曝气生物滤池工艺,以牡蛎壳为填料、含海水污水为处理对象,系统考察不同的海水含率、原水葡萄糖和氨氮浓度等原水条件下的硝化性能。结果表明,对于海水含率在40%到100%的污水处理,氨氮去除率可达到95%以上,表明该生物滤池中的氨氧化菌(AOB)可耐受较高的海水盐度;耐海水盐度的驯化硝化细菌中,AOB的耐盐度抑制能力强于亚硝酸氧化菌(NOB),当海水含率大于70%时,NOB的活性更容易受到抑制。在高海水盐度下,降低原水的葡萄糖与氨氮浓度可提高NOB活性。牡蛎壳附着生物膜与液相悬浮污泥中的AOB和NOB均参与了氨氮去除,生物膜中的AOB和NOB活性高于悬浮污泥。     

兼氧接触氧化与土地渗滤联合处理农村污水的研究

采用兼氧接触氧化与土地渗滤联合处理工艺对农村混合污水进行了试验.结果表明,系统对污染物有良好的去除效果.在进水COD 397～564 mg/L条件下,兼氧接触氧化水力停留时间为24 h时COD去除率大于75%;经过土地渗滤系统处理,在0.02 m3/(m2·d)的水力负荷下,COD去除率大于60%,氨氮、总磷的去除率大于99%.     

海水及浓海水吸收二氧化硫

采用鼓泡法研究了海水及浓海水对二氧化硫的吸收效果,并考察了吸收液温度、气体流量、盐度及碱度等因素的影响.结果表明,相同条件下,浓海水对二氧化硫的吸收能力较海水明显提高,且温度越高浓海水优势越明显,气体流量为200 mL/min,二氧化硫浓度为3 140 mg/m3,25℃时,浓海水的穿透时间较原海水延长20 min,60℃时则延长30 min.相同碱度条件下,盐度的增加对海水吸收二氧化硫无明显影响;而在相同盐度条件下,碱度的增加可显著提高海水吸收二氧化硫的能力.     

厌氧折流板反应器—生物接触氧化组合工艺处理生活污水研究

采用厌氧折流板反应器(ABR)-生物接触氧化组合工艺(以下简称组合工艺)进行生活污水处理试验研究,确定最佳水力停留时间(HRT),在此基础上考察组合工艺对生活污水COD、SS和TN的去除效果。结果表明:(1)组合工艺最佳反应条件为组合工艺HRT 20h(ABR段HRT 15h,生物接触氧化池段HRT 5h)、温度14℃。(2)在最佳反应条件下,组合工艺对生活污水COD、SS具有良好的去除效果,COD、SS去除率平均分别为81.0%、95.8%;对生活污水TN去除效果较差,去除率平均仅为64.7%。     

两段接触氧化法处理生活污水的实验研究

接触氧化法具有处理效率高,耐冲击负荷,出水水质好,占地面积小等特点.本文在两段接触氧化法处理生活污水的模拟实验基础上,探讨了水力停留时间、供气量对处理效果的影响.实验结果表明:在总气水比为5∶1,两段的水力停留时间均为1 h时,COD、BOD5和SS的平均去除率分别达到94.5%、93.2%和91.7%.与活性污泥法相比,两段接触氧化法对氨氮有较好的去除效果.工程实例运行情况表明,出水水质符合国家污水排放标准,该法也适用于厂矿企业及城镇生活小区的生活污水处理.     

长/短HRT交替运行的农村污水AAO工艺溶解氧调控策略

农村污水瞬时排水的水量波动会引起处理过程水力停留时间变化,直接导致系统污水处理效能不佳等问题。选取农村污水AAO污水处理系统,探明了长/短HRT交替运行下最优DO条件,以及HRT与DO的响应关系,并提出了适宜农村地区的污水处理最佳DO调控策略。结果表明,好氧区DO维持约在1 mg·L^-1,系统的污染物去除效能较好,出水COD、TN分别为14.88、10.15 mg·L^-1,对应去除率为92%、64%。HRT改变直接影响系统好氧区DO变化,通过调控不同HRT下的DO,在保证出水水质的前提下,可实曝气量降低73%,能耗降低67%。该研究结果对农村污水AAO污水处理系统优化运行和提质增效提供参考。     

曝气生物滤池用于分散型污水处理及其动力学浅析

将曝气生物滤池用于分散型污水处理,分析了反应器在不同水力负荷条件下对污染物的去除效果,同时从动力学角度对反应器作了浅析,总结出一个动力学模型.实验证明,该模型对出水水质预测和水力负荷条件的确定具有一定的工程实践指导作用.     

沟渠式生物接触氧化法对有机物和氨氮的去除研究

生物接触氧化工艺是目前较为成熟的水质净化技术,国内外在河流水质净化、水体修复中都有较多的研究和应用.在实验室采用沟渠式生物接触氧化组合系统处理模拟村庄面源污水,较好地去除了有机物并实现氨氮转化.结果表明,当进水COD为130～290mg/L、氨氮为30～40mg/L、水力负荷为0.19～0.24m3/(m2·d)的条件下,该系统稳定运行11周,COD和氨氮的平均去除率分别达85%和79%.     

污水土壤含水层处理系统原理、管理、效率和应用

论述了污水土壤含水层处理系统中的地球化学过程.该系统通过对污染物的机械过滤、生物化学转化和降解过程、吸附/解吸过程、氧化/还原过程、沉淀/溶解过程、以及矿物的合成过程净化污水.运作周期通常为1～2 d灌水/4～5 d排干,年水力负荷变化于15～100 m之间,应根据季节变化调整水力负荷.该系统能有效去除污水中的微生物和悬浮物,降低COD和BOD含量,和去除潜在的有毒的无机成分,如重金属和含氧阴离子.作为一种低投资、低能耗、高净化效率、运行简单的自然的污水处理技术,其在世界各国得到了广泛应用.我国部分地区水资源极其短缺,在土壤和气候条件适合的地区,应用土壤含水层处理技术处理污水,实现污水资源化,既解决了污水污染环境问题,又将在一定程度上缓解该地区的水资源短缺问题,对于经济与环境的协调发展具有重要意义.     

高负荷地下土壤法处理有机污水的模拟实验研究

针对传统地下污水渗滤系统的主要缺陷,提出了采用人工土壤提高系统的污水承载能力,采用多层过渡结构增大颗粒有机物的接触氧化表面积,采用高渗透性夹层增加氧气供应,以提高污水地下处理系统的水力负荷,延长其使用寿命.以我国南方典型的红壤土、砂和砾石为填充材料进行了实验室模拟实验,供试污水来自中国科学院广州地球化学研究所生活小区.结果显示,在25 cm/d的水力负荷下,系统没有被堵塞的迹象,采用每天2次投配污水的方式（每次12.5 cm）,渗透系数为0.6 cm/min的土柱可以达到很好的出水效果,其COD、BOD5、SS、TN和TP去除率分别达到81.5%、84.6%、88.8%、82.6%和98%.     

NaCl盐度对耐盐活性污泥沉降性能及脱氮的影响

针对海水冲厕工程的实施,采用序批式活性污泥反应器(SBR)处理实际含盐生活污水,考察了盐度对耐盐活性污泥沉降性能及脱氮效能的影响。研究发现,经过长期盐度驯化后的污泥系统也会出现丝状菌污泥膨胀。在经过10 g/L盐度长期驯化的污泥系统中,污泥容积指数(SVI)随着盐度的升高而降低,盐度升高使丝状菌减少,污泥絮体变小变密实。但是,盐度降低时会引发更严重的污泥膨胀,导致污泥流失。对脱氮性能的研究表明,硝化菌的耐盐能力较强。当盐度由10 g/L改变为0、5、15、20 g/L时,氨氮去除率依然可以维持在99%以上。但亚硝酸盐积累率无论是盐度升高或降低时都升高,这表明驯化后污泥中的亚硝酸氧化菌(NOB)对盐度变化的耐受能力比氨氧化菌(AOB)弱,无论盐度升高或降低都会对其产生较大的影响。     

The adsorption behaviour of dimethyltin from seawater onto sedimentary phase in Tianjin Harbor

The adsorption of dimethyltin from a seawater matrix onto suspended particulate matter was studied. The influences of pH and salinity, adsorption isotherms at various temperatures, and the adsorption rate under certain experimental conditions were determined. It was found that the adsorption capacity was highest at c. pH 6 and decreased with increasing salinity. The adsorption behaviour at various temperatures was described best by a Langmuir isotherm. The adsorption capacity of dimethyltin was higher in natural seawater than in artificial seawater at the same temperature.     

Net fluxes of pesticides from the Scheldt Estuary into the North Sea: a model approach

A hydrological model was constructed with the commercially available modelling environment ECoS for the calculation of mixing plots of dissolved pesticide concentrations in the Scheldt Estuary. The model was based on a one-dimensional advection-dispersion equation and dispersion coefficients were calculated from measured salinity profiles. The model could correctly predict the movement of water masses within the estuary. Nominal flushing times of the estuary were calculated with the fraction-of-freshwater method and ranged between 25 and 95 days, depending on the freshwater discharge. Model calculations demonstrated that the application-related time profiles of pesticide input may well induce curvature in the calculated estuarine mixing plot even if the pesticide behaves conservatively. Calculated mixing plots were compared with experimental data and good agreement was obtained between the measurements and the conservative mixing plot of atrazine. For metolachlor an additional direct emission had to be modelled to explain the differences between the experimental data and the conservative mixing plot. For dichlorvos and simazine. on the other hand, an estuarine loss constant had to be included in the model. Using a least-squares procedure the estuarine loss constants for dichlorvos and simazine were estimated at half-lives of five and 26 days, respectively. Because mixing plots were strongly influenced by the time profiles of pesticide input, standard procedures in which net fluxes are calculated from mixing plots, were not applicable. Therefore, net fluxes were calculated with a newly developed procedure in which the estuarine loss constants and the estuarine flushing time were combined. For the non-conservative compounds dichlorvos and simazine, the net fluxes to the North Sea were found to be 96 and 64%, respectively, lower than the gross fluxes transported by the River Scheldt.     

Photolytic degradation of triclosan in freshwater and seawater

A 12-days photolysis experiment of triclosan, a widely used bactericide, was performed in freshwater and seawater under a low intensity artificial white light source. Photodegradation of triclosan was observed in both the freshwater and seawater samples. Assuming a first-order reaction, half-lives of triclosan in the freshwater and seawater were approximately 8 and 4 days, respectively. 2,8-Dichlorodibenzo-p-dioxin (DCDD) was detected in both the freshwater and seawater samples after 3 days of irradiation. The photodegradation of triclosan and the production of DCDD suggest that triclosan could be less stable and DCDD might be more stable in seawater than freshwater. As a result, DCDD produced from triclosan survives for a longer time in seawater.     

A2／O-MBR工艺处理低负荷污水并回用

将A2／O生物处理单元与MBR相结合构建了的处理能力为2000m3／d的A2／O—MBR工艺,并应用于缺水地区校园生活污水的处理与回用。该系统运行稳定,运行阶段的实验结果表明,在进水COD为100-200mg／L、NH4＋-N为19～33mg／L、TN为25-43mg／L、TP为35mg／L和低碳氮比的情况下,出水水质优于《城市污水再生利用城市杂用水水质》（GB／T18920-2002）的要求,且全部用于杂用及校园绿化等。经分析该工艺运行成本为0．96元／m3,每年可节省自来水73万t,获得较好的环境效益与经济效益。     

生物活性炭填料反应器处理含盐水体的硝化性能

以颗粒活性炭为填料,采用盐度梯度两步驯化法构建含盐水体生物滤器硝化功能,研究了生物滤器稳定后水力停留时间(hydraulic retention time,HRT)、进水氨氮负荷和CODMn/N等对反应器硝化性能的影响。结果表明,25～27℃,盐度30的含盐水体生物滤器硝化功能构建需73 d,其中淡水生物滤器硝化功能构建需28 d,淡水驯化为盐度15的生物滤器需19 d,盐度15驯化为盐度30的生物滤器需26 d;实验条件下生物活性炭填料反应器中生物量达到146～742.1 nmolP/g-BAC;调节进水氨氮浓度2 mg/L左右时,最佳HRT为1 h,氨氮去除率达到84.98%,相应的氨氧化菌和硝酸菌氧吸收速率(oxygen uptake rate,OUR)分别为2.091和1.948 mg O2/(g-BAC.h);HRT为1 h时,随着进水氨氮负荷的加大,氨氮去除率逐渐降低,当进水氨氮负荷由0.12增加到0.48 g-N/(kg-BAC.d)时,氨氮去除率由84.98%降低到41.68%,同时氨氧化菌OUR由2.091降低到0.625 mg O2/(g-BAC.h);随着CODMn/N的升高,氨氮去除率下降,CODMn/N从1～8时,氨氮去除率由84.98%降低到53.64%,CODMn去除率却逐渐增加,由40.86%增加到93.59%,异养菌OUR随着CODMn/N升高呈上升趋势,最大达到0.914 mg O2/(g-BAC.h)。     

Field and laboratory simulations of storm water pulses: behavioural avoidance by marine epifauna

Epifaunal communities associated with macroalgae were exposed to storm water pulses using a custom made irrigation system. Treatments included Millipore freshwater, freshwater spiked with trace metals and seawater controls to allow for the relative importance of freshwater inundation, trace metals and increased flow to be determined. Experimental pulses created conditions similar to those that occur following real storm water events. Brief storm water pulses reduced the abundance of amphipods and gastropods. Freshwater was the causative agent as there were no additional effects of trace metals on the assemblages. Laboratory assays indicated that neither direct nor latent mortality was likely following experimental pulses and that epifauna readily avoid storm water. Indirect effects upon epifauna through salinity-induced changes to algal habitats were not found in field recolonisation experiments. Results demonstrate the importance of examining the effects of pulsed contaminants under realistic exposure conditions and the need to consider ecologically relevant endpoints.     

絮凝-微纳气泡法处理采油废水

对采自胜利油田的采油废水,分别进行了聚硅硫酸铁(PFSS)絮凝法、微纳气泡法和絮凝-微纳气泡联合法处理,考察了处理过程对采油废水水质和所配制聚合物(部分水解聚丙烯酰胺)溶液粘度的影响。结果表明,均可有效降低废水的矿化度、油含量和悬浮物含量,明显提高用其配制的聚合物溶液的粘度;联合处理效果明显高于单独采用絮凝或微纳气泡处理的效果。所处理后的废水可有望代替淡水用于油田现场配制聚合物驱油体系,在消除油田污水环境污染的同时,可节约淡水资源。     

No evidence for a critical salinity threshold for growth and reproduction in the freshwater snail Physa acuta

The growth and reproduction of the freshwater snail Physa acuta (Gastropoda: Physidae) were measured at various salinity levels (growth: distilled water, 50, 100, 500, 1000 and 5000 microS/cm; reproduction: deionized water, 100, 500, 1000 and 3000 microS/cm) established using the artificial sea salt, Ocean Nature. This was done to examine the assumption that there is no direct effect of salinity on freshwater animals until a threshold, beyond which sub-lethal effects, such as reduction in growth and reproduction, will occur. Growth of P. acuta was maximal in terms of live and dry mass at salinity levels 500-1000 microS/cm. The number of eggs produced per snail per day was maximal between 100 and 1000 microS/cm. Results show that rather than a threshold response to salinity, small rises in salinity (from low levels) can produce increased growth and reproduction until a maximum is reached. Beyond this salinity, further increases result in a decrease in growth and reproduction. Studies on the growth of freshwater invertebrates and fish have generally shown a similar lack of a threshold response. The implications for assessing the effects of salinisation on freshwater organisms need to be further considered.     

Health risk assessment of exposure to organic matter from the use of reclaimed water in toilets

To estimate the carcinogenic and non-carcinogenic risks of six volatile organic compounds (VOCs) found in reclaimed water used for flushing toilets, a probabilistic health risk assessment based on Monte Carlo simulations was used. Before Monte Carlo simulations, the contaminant volatilization model was applied to estimate the concentration of the pollutants in air. Moreover, a questionnaire was used to acquire daily exposure time and the Batch Fit tool of Crystal Ball software was applied to find the best-fitting distribution of a part of the input parameters. The risk analysis indicated that the health risks from six VOCs were lower than the negligible risk level (1?×?10^?8) in all cases, and the health risk for females was slightly higher than that for males. Overall, exposure to organic pollutants in reclaimed water during toilet flushing does not currently pose a significant carcinogenic risk to humans. In this study, we want to provide some information on the health risk from reclaimed water used for toilet flushing in China and hope that it will be useful to promote the application of reclaimed water in water-deficient areas.