复合沸石滤床修复北方景观水体的实验研究

以天然矿物质沸石、细砂及煤渣取代传统滤料构建复合基质生态床，表面种植景观植物，采用下向流-上向流运行方式修复北方景观水体。分别进行静态实验及不同循环速率下的动态实验，考察对水体污染物去除过程。结果表明，2种运行方式下对水体NH⁺₄-N去除率都在85%以上，其中以1 h为循环周期的运行方式去除率达97%，较静态提高12.8%；TN去除率最高为84%；TP去除不稳定，过程缓慢。煤渣层对NH⁺₄-N的去除效果差，硝化作用不彻底与反硝化作用的加强使下层出水NH⁺₄-N 、NO^-₂-N及NO^-₃-N浓度均高于上层。提高循环速率有利于对氮的去除。     

不同填充率对移动床生物膜反应器的产泥性能影响研究

研究了不同填充率下（10%～70%）移动床生物膜反应器的生物膜特征和处理效果，以及填充率与污泥产率的关系。结果表明：随着填充率的增加，填料上生物膜厚度逐渐减少，反应器中附着微生物浓度逐渐增加；污泥产率因填充率不同而有很大差异,同一个反应器内污泥产率随填充率的增加而减少；在进水COD为400 mg/L、NH⁺₄-N为40 mg/L、水力停留时间为12 h条件下，不同填充率下COD去除率均可达到94%以上，NH⁺₄-N去除率达到97%以上。     

改良型A2/O-MBR工艺的反硝化除磷性能研究简

重点考察了一种改良型膜生物反应器（A²/O-MBR）的脱氮除磷性能。该工艺主要特点在于对膜池硝化回流液进行了固液分离，并将上清液和浓缩污泥分别回流至缺氧池和厌氧池，这种改进提高了系统对氮、磷的同步去除效率。实验结果表明，在水力停留时间（HRT）为12 h，污泥龄（SRT）为30 d，混合液回流比为200%的运行条件下，进水COD、NH₄⁺-N、TN和TP平均浓度分别为（225±38）、（24.8±3.9）、（26.7±2.9）和（2.90±0.53）mg/L时，增加膜池硝化回流液固液分离装置前后，系统对COD和NH₄⁺-N的去除都维持在较高水平，而系统对TN和TP的去除效果显著提高，出水TN和TP平均浓度分别由（14.9±3.3）mg/L和（1.95±0.72）mg/L下降到（9.4± 1.9）mg/L和（0.91±0.38）mg/L，表明增加膜池硝化回流液固液分离装置显著改善了A²/O-MBR系统的脱氮除磷效果。反硝化除磷活性实验结果进一步表明，改进后系统中反硝化除磷活性占总除磷活性的比例由51.5%上升至61.7%，说明增加膜池硝化回流液固液分离装置强化了系统的反硝化除磷性能。     

SBR-BAF工艺处理效能的试验研究

根据生物除磷和脱氮的机理,污水的脱氮除磷存在基质竞争和泥龄等方面的矛盾。为了分析和解决这个问题，设计开发了一种新的污水生物处理工艺——SBR-BAF复合工艺,并以模拟城市生活污水为处理对象对该工艺的处理效能进行了考察。试验结果表明，系统对COD（不计BAF加入的外碳源）、TP、NH⁺₄-N和TN的平均去除率分别为96%、98%、93%和84%，出水中COD、TP、NH⁺₄-N和TN的平均浓度分别为20、0.23、3.24和7.68 mg/L，各项水质指标均达到《城镇污水处理厂污染物排放标准》（GB 18918-2002 ) 规定的一级标准中的A标准。     

低温条件下BAF+SPD组合工艺对滇池入湖河水的脱氮效果

为缓解湖泊富营养化问题，需进一步降低入湖河流氮的含量。针对滇池流域新运粮河的低C/N水质特征，研究了冬季低温条件下的微曝气生物滤池（BAF）及固相反硝化（SPD）组合异位脱氮工艺。结果表明，BAF+SPD组合工艺启动挂膜阶段，约3周后，NH₄⁺-N的去除率达80%以上，而反硝化细菌增殖相对缓慢，约5周后，NO₃^--N的去除率达80%以上；稳定运行的低温阶段，除降雨时间外，NH₄⁺-N平均去除率达80%，出水NH₄⁺-N浓度<1 mg/L；NO₃^--N平均去除率达到85%以上，出水NO₃^--N浓度<1 mg/L；TN平均去除率达80%以上，出水TN浓度<2 mg/L，主要水质指标达到国家地表水Ⅴ类标准。     

双泥膜法SBR脱氮除磷效果研究

通过实验室小试，以人工模拟生活污水为研究对象，考察了基于反硝化除磷理论开发的双泥膜法SBR工艺的脱氮除磷效果。长期试验结果表明：双泥膜法SBR工艺能使硝化菌和除磷菌各自在最佳的环境中生长，解决了传统工艺中脱氮和除磷的矛盾，节省了碳源和能源，并取得了稳定高效的脱氮除磷效果。在进水C∶N∶P为25∶5∶1，换液比为75%的情况下，系统对COD，TP和NH⁺₄-N的平均去除率分别为89.13%、96.12%和86.78%。     

C/N对Carrousel 2000氧化沟同步脱氮除磷的影响研究

就C/N对Carrousel 2000氧化沟同步脱氮除磷的影响进行了研究。结果表明，进水C/N值在5～13之间时，进水C/N不影响氧化沟系统对NH₃-N的去除效果。出水NH₃-N浓度＜1 mg/L，平均去除率达到97.40%。当C/N低于11时，TN、TP的去除率随C/N的升高而快速大幅提高，分别从5时的26.47%和14.99%升至11时的93.48%和97.03%。当C/N＞11时，氧化沟TN去除率达到93.48%，TP去除率接近100%，氧化沟具有了良好的同步脱氮除磷的效果，出水水质满足国家《城镇污水处理厂污染物排放标准》(GB 18918-2002一级A标准)要求。TP去除率与TN去除率相关系数R₂＝0.985。     

污泥回流分离工艺（RSSP）除磷脱氮试验研究

介绍了一种新型的脱氮除磷工艺——回流污泥分离工艺（return sludge separate process），及其运行情况。该工艺在传统的厌氧缺氧好氧（A²/O）的模式下，针对硝酸盐对厌氧释磷的抑制问题进行改进，提出回流污泥的气浮浓缩分离方案，以提高系统的脱氮除磷效果。研究结果表明，在进水COD为250～400 mg/L，NH⁺₄-N为30～45 mg/L，PO^3-₄-P为8～10 mg/L左右时，该工艺对NH⁺₄-N和PO^3-₄-P的去除率分别可达79.3%和95%。该系统与A²/O的平行比较数据表明，该系统能够提高氮磷综合处理效率，解决A²/O处理工艺中存在无效释磷和硝酸根抑制问题。     

温度对复合厌氧折流板膜生物反应器处理生活污水效能的影响简

将新型CAMBR反应器（厌氧折流板反应器（ABR）与膜生物反应器（MBR）优化组合）用于处理生活污水，研究温度对该反应器处理效能的影响。实验水力停留时间7.5 h，混合液回流比设置为200%，pH值为6.5~8.5，溶解氧3 mg/L左右。控制3个温度梯度：高温（32~37℃），中温（20~25℃），低温（5~10℃），每个温度运行35 d。结果表明，在高温条件下，系统出水COD、NH₄⁺-N、TN和TP平均浓度分别为25、0.5、12.5和0.7 mg/L。在中温条件下，系统出水COD、NH₄⁺-N、TN和TP浓度分别30、1.2、12.5和0.4 mg/L。在低温条件下，COD和TP分别经过15 d和20 d调整适应，出水可恢复至35 mg/L和1 mg/L。由于低温（10℃以下）对硝化细菌产生强烈抑制，出水NH₄⁺-N去除率最终稳定在35%，TN去除率为40%。低温条件下，该反应器应用于污水处理中需注意适当保温，以保证出水水质。     

容积负荷对ANAMMOX生物滤池脱氮效能的影响及其基质动力学

采用2套启动成功的上向流厌氧氨氧化（ANAMMOX）生物滤柱，通过调节进水NaNO₂和（NH₄）₂SO₄ 的浓度负荷及水力负荷，改变进水容积负荷，探讨容积负荷对ANAMMOX生物滤柱脱氮效能的影响及其动力学模型。结果表明，滤速恒定条件下，通过提高进水基质浓度来提高进水TN容积负荷，其容积负荷去除动力学过程符合Monod-Haldane基质抑制模型。进水NH₄⁺-N与NO₂^--N浓度分别低于100 mg/L和133 mg/L时，反应器脱氮效果不受明显影响，TN容积去除负荷可达4.21 kg/（m³·d），TN去除率可达80%以上。进水基质浓度恒定条件下，通过提高滤速来提高进水TN容积负荷，其容积负荷去除动力学过程符合零级动力学方程。不受基质浓度抑制的条件下，滤速为3.0 m/h、进水容积负荷为8.82 kg/（m³·d）时，反应器总氮容积负荷去除量可达7.15 kg/（m³·d），总氮去除率可达81.1%。     

利用城市生态河道深度净化污水处理厂出水的工程技术研究

提出了城市生态河道工程构建的技术方法，并研究了示范工程对城市污水处理厂出水的深度净化规律。实验结果表明，在保证生态景观功能的前提下，将生态河道技术工艺用于污水处理厂出水的深度净化，能够高效、稳定地去除氮磷等营养物，河道出水可以满足城市景观水体补充水源的水质要求，出水TP、PO^3-₄、TN、NH₃-N和NO₃-N平均值分别达到0.263、0.116、2.570、0.752和2.438 mg/L，去除率分别达到85.4%、92.8%、60.8%、39.7%和77.2%。     

国家级流域水环境保护总体规划一般模式研究

流域综合水管理是发达国家普遍采用的管理模式,主要手段之一是制定流域水环境保护总体规划.流域水环境保护总体规划是流域各相关利益方就流域社会经济发展与水环境保护达成的决策,是其他所有规划制定的基础和依据,核心内容是规划目标的确定.流域水环境保护总体规划是流域综合管理的决策平台和信息共享平台,是环境保护的刚性约束,为流域水资源开发利用划定红线.流域水环境保护总体规划是目标导向型的,通过指标体系指导省级行政区负责制定的小流域水环境保护规划,协调流域内省级行政区国民经济和社会发展规划、土地利用总体规划、城市总体规划等其他部门规划.中国目前缺乏流域水环境保护总体规划,基于此提出了国家级流域水环境保护总体规划的一般模式,包括基本内容、规划文本和规划实施3个部分.流域水环境保护总体规划实施的主要手段是审批小流域水环境保护规划.     

Pharmaceuticals on a sewage impacted section of a Mediterranean River (Llobregat River,NE Spain) and their relationship with hydrological conditions

Introduction  

Mediterranean rivers are characterized by a high flow variability, which is strongly influenced by the seasonal rainfall. When water scarcity periods occur, water flow, and dilution capacity of the river is reduced, increasing the potential environmental risk of pollutants. On the other hand, floods contribute to remobilization of pollutants from sediments. Contamination levels in Mediterranean rivers are frequently higher than in other European river basins, including pollution by pharmaceutical residues. Little attention has been paid to the transport behavior of emerging contaminants in surface waters once they are discharged from WWTP into a river. In this context, this work aimed to relate presence and fate of emerging contaminants with hydrological conditions of a typical Mediterranean River (Llobregat, NE Spain).     

SITE Demonstration of the CF Systems Organic Extraction Process

The CF Systems Organic Extraction Process was used to remove PCBs from contaminated sediment dredged from the New Bedford Harbor. This work was done as part of a field demonstration under EPA’s Superfund Innovative Technology Evaluation (SITE) program. The purpose of the SITE program is to provide an independent and objective evaluation of innovative waste remediation processes. The purpose of this paper is to present the results of the SITE demonstration of this technology. Results of the demonstration tests show that the system, which uses liquefied propane, successfully removed PCBs from contaminated sediments in New Bedford Harbor. Removal efficiencies for all test runs exceeded 70 percent. Some operational problems occurred during the demonstration which may have affected the efficiency with which PCBs were removed from the dredged sediment. Large amounts of residues were generated from this demonstration project. Costs for using this process are estimated to be between $150/ton and $450/ton.     

SITE demonstration of the CF systems organic extraction process

The CF Systems Organic Extraction Process was used to remove PCBs from contaminated sediment dredged from the New Bedford Harbor. This work was done as part of a field demonstration under EPA's Superfund Innovative Technology Evaluation (SITE) program. The purpose of the SITE program is to provide an independent and objective evaluation of innovative waste remediation processes. The purpose of this paper is to present the results of the SITE demonstration of this technology. Results of the demonstration tests show that the system, which uses liquefied propane, successfully removed PCBs from contaminated sediments in New Bedford Harbor. Removal efficiencies for all test runs exceeded 70 percent. Some operational problems occurred during the demonstration which may have affected the efficiency with which PCBs were removed from the dredged sediment. Large amounts of residues were generated from this demonstration project. Costs for using this process are estimated to be between $150/ton and $450/ton.     

Evaluation of HCH isomers and metabolites in soils, leachates, river water and sediments of a highly contaminated area

In this work we evaluate the contamination caused by HCH residues in the soil, leachates, river water and sediments of an industrial estate of the NW of Spain. We study the distribution of the isomers in the different matrices, analysing 37 soil samples, collected in eight points at several depths, six natural leachates, four river water samples and three river sediments. Soil and leachate samples present very high levels of HCH isomers, higher than the established by legislation, and some pesticides were also detected in the analysed river water whereas no pesticides were detected in the river sediments. The distribution of isomers was different depending on the matrix analysed. Some natural degradation products and also other organochlorine pesticides were detected in the samples analysed.     

Spatial and temporal variability of sediment deposition on artificial-lawn traps in a floodplain of the River Elbe

Artificial-lawn mats were used as sediment traps in floodplains to measure sediment input and composition during flood events. To estimate the natural variability, 10 traps were installed during two flood waves at three different morphological units in a meander loop of the River Elbe. The geochemical composition of deposited and suspended matter was compared. The sediment input showed weak correlations with concentration and composition of river water. It also correlated poorly with flood duration and level as well as distance of trap position from the main river. This is due to the high variability of the inundation, different morphological conditions and the variability of sources. The composition of the deposits and the suspended matter in the river water was comparable. Hence, for the investigated river reach, the expected pollution of the floodplain sediments can be derived from the pollution of the suspended matter in the river during the flood wave.     

凤眼莲在城市重污染河道修复中的应用

外港河是秦淮河重要支流，长期以来遭受严重污染。2006年4月份起对外港河进行了综合生态治理。在前期清淤和截污的基础上，7月份开始引种凤眼莲。在上游排污口附近和外港河河口段分别设置的4个生态区以及河面上布设的水面载体内全面放养以凤眼莲为主的浮水植物。经过5个多月的初步治理，外港河水体透明度从40 cm以下提高到120 cm左右，COD下降了70.4％，TSS、TN和NH₃-N分别下降了39.6％、49.7％和21.8％。结果证明，凤眼莲在净化严重污染的河道方面起到了良好的效果，引种凤眼莲治理城市重污染河道是切实可行的；此外，用PVC管设计制作的水面载体来放养浮水植物可以点缀水面环境，美化城市河道景观。     

面向城市水系环境需水的再生水空间配置——以深圳市宝安区为例

以深圳市宝安区为例,探讨以再生水满足城市水系环境需水的方法.应用一维恒定与非恒定水质模型计算了4种补水水质方案下该区10条主要河流的环境需水量,从水量平衡角度提出全区再生水BOD5的平均值,并进一步分析了补水水质与河流环境需水量的关系.结合该区水系与污水处理系统空间位置,提出3种再生水的空间配置方法.结果表明:茅洲河和...     

The differences in phenolic content in rivers exposed and non-exposed to anthropogenic contamination

The purpose of the work was to determine the differences in a kind, number and concentrations of phenol, chlorophenols, chlorocatechols chlorinated methoxyphenols (chloroguaiacols, chlorosyringols) and 3,4,5-trichloroveratrole in the drainage of the Dzierzazna river, the flow non-exposed to anthropogenic contamination and in the Ner river, the flow exposed to anthropogenic pollution. The samples of water were collected in the Dzierzazna river in the Swoboda locality, the inflow of the Dzierzazna river - the Ciosenka river and, also, in the spring situated in Ciosny Sady locality. Water of the Ner river was collected in points near ?ód?, Konstantynów, Poddebice and Dabie towns. The compounds were condensed (adsorbed) and eluted with methylene chloride on octadecyl C18 layer in a Baker Separex system. The obtained eluent was separated using the method of gas chromatography and analysed using mass spectrometry technique. In samples collected from the drainage of the Dzierzazna river phenol, chlorophenols, guaiacol, trichloroguaiacol, tetrachloroguaiacol, trichlorosyringol and 3,4,5-trichloroveratole were determined. As no anthropogenic sources are situated within the drainage of the Dzierzazna river, we may suppose that most of the determined compounds are mainly of natural origin. No or trace concentrations of chlorinated methoxyphenols were noted in the water of the Ner river, but a higher number, and concentrations of chlorophenols and additionally chlorocatechols were determined in this flow. It is also apparent that changes in a number and concentrations of phenols in the water of the Ner river did not prove a seasonal character, which was typical of the Dzierzazna drainage waters.