人工湿地基质除磷研究进展

基质除磷被认为是人工湿地磷去除的主要方式，除磷效果不仅受基质自身物理化学性质的影响，还受水力条件、磷负荷、pH值、季节、温度、有机负荷、溶解氧、干湿交替等因素的影响。本文较系统分析了湿地基质除磷的作用机理和基质除磷效率的影响因素，最后对今后研究的方向进行了展望。     

垂直流人工湿地填料对尾水深度处理的效果

为了提高垂直流人工湿地对污水处理厂尾水脱氮除磷的效果,选择沸石、活性炭和牡蛎壳三种人工湿地填料在不同厚度和水力负荷下进行了研究。结果表明,三种填料单独使用时,牡蛎壳、活性炭、沸石分别对总磷、COD、氨氮有显著的去除效果。在活性炭∶牡蛎壳∶沸石=1∶2∶7配比使用时,水力负荷会影响人工湿地对污染物的去除效果,0.5 m~3/(m~2·d)水力负荷下各试验池对污水的处理效果最好,出水水质最为稳定,总氮总磷受水力负荷影响较大,氨氮与COD则受其影响较小。     

陶粒-沸石-活性炭组合填料生物滤池的研究

采用陶粒、沸石、活性炭填料合理组合作为曝气生物滤池的填料对高校生活污水进行处理。研究了组合填料生物滤池生物膜的培养,不同水力负荷、容积负荷和气水比对污水处理效率的影响,以及该生物滤池对生活污水的处理效果。结果表明,采用组合填料生物滤池,接种挂膜培养周期为25d,在水力负荷为2．5m3／（m2·h）,气水比3．5：1,组合填料生物滤池出水COD、BOD5、SS、NH3-N和色度平均值达到《城市污水再生利用城市杂用水水质》GB／T18920—2002水质要求。     

废水回用工艺中曝气生物滤池的特性研究

以页岩陶粒为滤料,对曝气生物滤池的运行性能进行了研究。通过考察水力负荷对COD、氨氮去除效果的影响试验,容积负荷对COD去除效果试验,BAF对浊度的去除效果、抗冲击能力试验;结果显示:COD最佳水力负荷为7.0m3/h,NH4+-N最佳水力负荷为5.0m3/h,COD最佳容积负荷为5.89kg/(m3.d);进水浊度平均为12.7NTU,出水浊度平均为3.5NTU时,平均去除率为72.4%。水力冲击负荷对硝化菌的影响较小,而对异养菌影响较大。     

以造粒粉煤灰为过滤介质去除景观水中磷的研究

研究了造粒粉煤灰的最大磷吸附量、磷吸附速率等吸附特征，以及颗粒粒径、磷浓度、水力负荷对景观水除磷效果的影响。还进行了为期21天的连续过滤试验，发现滤床在高水力负荷条件下能持续地去除景观水中的磷。     

沸石人工湿地填料对氨氮的去除效果

选取沸石作为人工湿地填料,对沸石吸附实验的水力负荷、污染负荷、运行方式分别进行研究,探讨沸石对氨氮的去除效果及影响因素。结果表明,沸石对氨氮有较好的处理效果,相同条件下远优于砂石。水力负荷会影响沸石对氨氮的去除效果,低水力负荷下的处理效果和稳定性均较好。沸石在不同氨氮浓度下的去除效果差别不大。运行方式对氨氮的去除有一定影响,6 h间歇周期运行时,沸石填料对氨氮的去除效果好于其他间歇周期。     

新型填料在生物接触氧化工艺中的应用研究

以处理120L／d城镇生活污水的生物接触氧化小试装置为研究平台,介绍了新型内置悬浮球形填料一生物接触氧化工艺的特点及运行状况。试验结果表明：两种新型内置悬浮球形填料对反应器充氧效率、接种挂膜速率、污水处理效果对比均为纤维束状填料好于筒状填料;与连续曝气相比,采用间歇曝气的运行方式,在使出水NH3-N达标的基础上,提高了TN和TP的去除率,系统的同步硝化反硝化现象和反硝化除磷现象比较明显,具有较强的经济性和实用性。     

AO工艺同步聚合氯化铝辅助除磷应用研究

在深入了解除磷机理的基础上,通过实验室小试和生产性试验,研究AO工艺同步PAC的除磷效果,配制浓度对除磷效果的影响,投药量与除磷效率的关系,得出了PAC投加量估算公式,并进行了除磷成本核算。结果表明,AO工艺同步PAC除磷具有良好的除磷效果和运行稳定性;PAC适宜的配制浓度为2％～4％;PAC除磷吨水成本为0．06～0．15元／m3.     

影响聚磷菌与聚糖菌竞争的关键因素研究进展

增强生物除磷（EBPR）是一种高效、经济的除磷工艺，然而在某些条件下聚糖菌的过量繁殖导致除磷效果恶化。文章阐述了影响聚磷菌和聚糖菌生长的关键因素，从而可以选择性的培养聚磷菌并使其处于竞争优势，这对于提高EBPR的除磷效果、增强工艺的稳定性具有重要的意义。     

城镇污水处理厂NPR工艺低温运行的效能分析

介绍了天津市某城镇污水处理厂NPR工艺的特点及运行状况。通过对污水厂的运行监测数据分析,研究了该工艺在低温条件下处理城镇生活污水时的脱氮除磷效果。结果表明:NPR工艺具有一定的优异性,它能在降低能耗的前提下使系统COD和SS的去除率进一步降低,出水能达到中水回用标准,有利于污水的再生利用;低温影响NPR系统的硝化及反硝化率,低温下有机物的去除更易受到有机负荷的影响;温度对生物去除SS,COD和TP的效果影响不大,对NH3-N及TN的去除效果影响比较明显。低温下污水处理厂COD、SS、NH3-N、TN、TP的平均去除率分别为72.1%、94.9%、67.5%、55.1%、66.5%。     

不同水力负荷条件下的人工湿地污染处理效果分析

本文研究了水力负荷对抚仙湖北岸典型人工湿地净化河道污水处理效率的影响。研究表明,TN、TP及SS去除率随着水力负荷的增加而下降,COD去除率受水力负荷的影响程度相对较小。综合考虑水力负荷对氮磷、有机物及悬浮物等水质净化效果的影响,如果不考虑其它因素,仅从系统处理效果的角度选择水力负荷,人工湿地系统的最佳水力负荷为0.5 m3/m2·d以下。     

RIVER PHOSPHORUS DYNAMICS AND RESERVOIR EUTROPHICATION POTENTIAL1

ABSTRACT: Sediments from the Pompton and Passaic Rivers at Two Bridges were analyzed for potentially available phosphorus fractions and total phosphorus (TP). Water samples from the same sites were analyzed for dissolved phosphorus, TP, suspended solids (SS), and volatile SS. Significant negative correlations between river TP concentrations and flow were observed. However, storm flows resulted in increases in TP and SS concentrations and flux (loadings). Most of the increase in river P loading at high flow was in the dissolved fraction, suggesting that the sediments may be a large source of dissolved P. Concentrations of potentially available P in the sediments ranged from 140 to 1310 times the TP concentration in the overlying water. According to a modified Vollenweider model, current P concentrations in the Pompton and Passaic Rivers will result in excessive P loading in the Wanaque Reservoir if even small volumes of river water are pumped to the reservoir through the recently completed Wanaque South pipeline. Reductions in sewage treatment plant effluent P concentrations alone will not produce sufficient decreases in river phosphorus concentrations to avoid this predicted overloading and eutrophication.     

Lake eutrophication management modeling using dynamic programming

Lake eutrophication problems have received considerable attention in Taiwan, especially because they relate to the quality of drinking water. In this study, steady-state river water quality and lake eutrophication models are solved using dynamic programming algorithms to find the nutrient removal rates for eutrophication control during dry season. The kinetic cycle of chlorophyll-a, phosphorus and nitrogen for a complete-mixed lake is considered in the optimization framework. The Newton-iterative technique is adopted to solve the nonlinear equations for the steady-state lake eutrophication model. The optimization framework is applied to Cheng-Ching Lake in southern Taiwan. Several nutrient loading scenarios for eutrophication control are studied. Optimization results for nutrient removal rates and corresponding wastewater treatment capacities of each reach of the Kao-Ping River define the least cost approach to lake eutrophication control. A natural purification method, structural free water surface wetland, is also suggested to save more investment and improve river water quality at the same time.     

新型分层生物滴滤池去除污水中氮磷的性能研究

生物滴滤池是农村生活污水处理的主要技术之一,但其存在氮、磷去除能力有限,稳定性不高等缺点。为提高新型分层生物滴滤池的氮磷去除效率,探索最佳工艺条件,本文采用新型分层生物滴滤池为试验装置,考察了滤料种类、水力负荷、回流比等对装置去除污水中氮磷性能的影响。结果表明,当滤料为炉渣、水力负荷为4 m3＆#183;m-2＆#183;d-1、回流比为2：1时滤池去除氮磷的效果最好,对NH4＋-N、TN、TP、COD的平均去除率分别可达到87.08%、57.37%、66.04%、80.78%;采用较高的回流比是滴滤池提高脱氮效果的一条有效途径。     

PHOSPHORUS RELEASE AND ASSIMILATORY CAPACITY OF TWO LOWER MISSISSIPPI VALLEY FRESHWATER WETLAND SOILS1

ABSTRACT: Phosphorus fluxes and water quality functions of a bottomland hardwood and freshwater marsh wetland soil were compared. The effect of soil physicochemical conditions, phosphorus loading rate, and diffusive exchange between soils and the overlying food water column on phosphorus release and retention were studied. The predominantly mineral swamp forest soil displayed greater phosphorus sorption potential than the organic freshwater marsh soil. Moreover, due to its low bulk density (0.11 g cm^?3), the freshwater marsh soil surface area required for phosphorus retention is very large compared to the bottomland hardwood wetland soil. For both wetlands, soil redox status affected P release and assimilatory capacity. The more reducing the soils, the smaller their phosphorus retention capacity (greater their release). Phosphorus removal from the overlying water column into the wetland soils followed a first-order kinetic model. Under similar hydrological conditions, phosphorus was found to diffuse 1.2 times faster to the bottom. land hardwood soil than in the freshwater marsh soil. Results indicate that while the bottomland hardwood wetland soil will serve as a sink for phosphorus entering such wetland, phosphorus will be released and exported from the freshwater marsh soil into adjacent ecosystems.     

Phosphorus sorbing materials: sorption dynamics and physicochemical characteristics

The effectiveness of various management practices to reduce phosphorus (P) loss from soil to water can potentially be improved by using by-product materials that have the capacity to sorb phosphorus. This study evaluated the P sorption and desorption potential, and the physicochemical characteristics of various phosphorus sorbing materials. Twelve materials were selected and P sorption potentials ranged between 66 and 990 mg kg(-1). Iron, and calcium drinking water treatment residuals (DWTRs), a magnesium fertilizer by-product, aluminum, and humate materials all removed substantial amounts of P from solution and desorbed little. Humate had the highest maximum P sorption capacity (S(max)). Materials which had a low equilibrium P concentration (EPC(0)) and a high S(max) included aluminum and humate by-products. In a kinetic study, the Fe-DWTR, Ca-DWTR, aluminum, and magnesium by-product materials all removed P (to relatively low levels) from solution within 4 h. Phosphorus fractionation suggests that most materials contained little or no P that was readily available to water. Sand materials contained the greatest P fraction associated with fulvic and humic acids. In general, materials (not Ca-DWTR) and magnesium by-product were composed of sand-sized particles. There were no relationships between particle size distributions and P sorption in materials other than sands. The Ca- and Fe-DWTR, and magnesium by-product also contained plant nutrients and thus, may be desirable as soil amendments after being used to sorb P. Further, using Ca-DWTRs and Fe-DWTRs as soil amendments may also increase soil cation exchange and water holding capacity.     

复合人工湿地去除有机污染物的研究

人工湿地中不同的污染物的去除机理不同,其去污的影响因素也不同.在国内,人工湿地对氮磷去除的研究较多,对新型有机污染物的研究很少,在很多机理上还属空白.总结了近年来国内外湿地对有机污染物去除的研究进展情况以及不同湿地类型对去除率的影响.系统的分析了有关湿地植物,基质,微生物对于有机污染物的去除作用机理,提出了存在问题并对今后湿地去除有机污染物的研究进行了展望.     

Influence of organic loading on an anaerobic sequencing biofilm batch reactor (ASBBR) as a function of cycle period and wastewater concentration

The effect of organic loading on the performance of a mechanically stirred anaerobic sequencing biofilm batch reactor (ASBBR) has been investigated, by varying influent concentration and cycle period. For microbial immobilization 1-cm polyurethane foam cubes were used. An agitation rate of 500 rpm and temperature of 30+/-2 degrees C were employed. Organic loading rates (OLR) of 1.5-6.0gCODl(-1)d(-1) were applied to the 6.3-l reactor treating 2.0 l synthetic wastewater in 8 and 12-h batches and at concentrations of 500-2000mgCODl(-1), making it possible to analyze the effect of these two operation variables for the same organic loading range. Microbial immobilization on inert support maintained approximately 60 gTVS in the reactor. Filtered sample organic COD removal efficiencies ranged from 73 to 88% for organic loading up to 5.4gCODl(-1)d(-1). For higher organic loading (influent concentration of 2000mgCODl(-1) and 8-h cycle) the system presented total volatile acids accumulation, which reduced organics removal efficiency down to 55%. In this way, ASBBR with immobilized biomass was shown to be efficient for organic removal at organic loading rates of up to 5.4gCODl(-1)d(-1) and to be more stable to organic loading variations for 12-h cycles. This reactor might be an alternative to intermittent systems as it possesses greater operational flexibility. It might also be an alternative to batch systems suspended with microorganisms since it eliminates both the uncertainties regarding granulation and the time necessary for biomass sedimentation, hence reducing the total cycle period.