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。     

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。     

复式潜流湿地净化生活污水的试验研究

研究了新型复式潜流人工湿地对生活污水的净化效果。在不同水力负荷、季节、曝气方式等条件下经过小试试验,分析了该湿地对污染物净化效果的影响。结果表明,该系统出水水质稳定,达到《城镇污水处理厂污染物排放标准》（GB18918--2002）的一级A标准。在水力负荷184mm·d。条件下COD、NH,一N去除率最大分别可达87．2％、68．9％。冬季低温条件下对各类污染物去除率仍大于20％。正交试验分析得知,最佳运行条件是气温28．6℃、水力负荷0．184m3·m-2·d-1、水力停留时间2．4d。对比试验表明,采用预曝气方式对湿地净化效果明显优于厌氧处理。     

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。     

高水力负荷下垂直流人工湿地净化景观水的研究

目前人工湿地普遍占地面积较大,使其在景观水处理中的应用受到限制,针对这一问题,构建实验水池模拟人工湖,构建高效垂直流人工湿地,对其在高水力负荷下净化劣Ⅴ类富营养化池水进行了研究.结果表明,湿地系统在1.64 m3/(m2·d)和3.28 m3/(m2·d)的高水力负荷下净化池水均取得了良好效果,水力负荷提高到5.74 m3/(m2·d),湿地出现了一定程度的堵塞,净化效果相对较差.本实验系统净化池水的最佳水力负荷为3.28 m3/(m2·d),该水力条件下系统对浊度、CODCr、NH 4-N、TP的平均去除率分别为64.9%、41.0%、24.7%、58.5%.     

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。     

潜流湿地处理旅游区生活污水生产试验:以COD为例

以某大型潜流人工湿地污水处理工程为实验基地，对潜流人工湿地工艺进行生产研究，本文介绍其对COD的去除性能。该工程COD进水平均98mg／L，出水平均38mg／L，达到GB18918-2002中一级A排放标准。当单级湿地进水COD浓度小于80mg／L，两级串联湿地进水COD浓度小于100mg／L时，可使湿地出水浓度小于50mg／L。工艺类型上，下行流湿地优点突出、最为全面，优势明显。不同植物配置上，本生产实验条件下，一级湿地种植芦苇和芦竹去处效果接近，二级湿地不同植物优劣排序：灯芯草〉美人蕉〉香蒲〉水竹〉香根草。     

生物填料塔处理餐厅污水的研究

分别以自行开发的组合型填料和焦炭作生物载体构成的生物填料等塔对餐厅污水处理进行了试验研究,试验考察了污水入塔COD值对塔中DO的影响,观察到的结果表明：长期在高入塔COD下运行对生物膜系统的持久、稳定不利;水力停留时间取3h－4h,COD的容积去除负荷为4kg/m^3.d时,出水既可达标,又可保持较高的处理能力;鼓风曝气时,气水比取8－12可使出水达标,而功耗较低;在相同的微生物系统和操作条件下,布水布气性好的组合填料处理效果高于布水气性差的焦炭。     

人工湿地技术处理生活污水

本文评估了一级强化预处理＋人工湿地在处理生活污水方面的使用范围,提出当进水中氨氮达到35mg/L,通过一级强化预处理以及人工湿地的出水难以达到一级B标准;同时由于人工湿地大部分为厌氧环境,对硝态氮去除效果良好,本文提出在进水氨氮浓度较高的情况下,将硝化加入人工湿地的预处理,利用人工湿地的一部分硝化能力和良好的反硝化能力使出水达标排放。     

人工湿地技术在农村生活污水综合治理中的应用探讨

农村生活污水具有浓度低、成分复杂、生化性高的特点,以豫南某村人工湿地工程为例,介绍人工湿地组合工艺处理农村生活污水,并对污染负荷、湿地床结构、基质材料及植被选择、水力条件等设计参数进行分析。结果表明,人工湿地系统能够有效处理农村生活污水,操作管理简单,在我国农村具有很强的推广意义。     

人工湿地塘床系统净化地表水的试验研究

成都市活水公园人工湿地塘床系统对枯水期府河水中的ＣＯＤｃｒ,ＢＯＤ５,ＴＮ,ＴＰ,ｏｉｌ,ＬＡＳ,Ａｒ－ＯＨ,ＮＨ３,Ｓ＾２－等污染物的去除率在８５％以上,总大肠菌群的去除率达９９．９％以上,其净化效果能够满足净化地表水或污水深度处理的需要。由此可见,人工湿地塘床系统是一种生态滤池。     

高效除氮菌在模拟潜流人工湿地中的应用

研究高效除氮菌的加入对模拟潜流人工湿地除污效果的影响。结果表明，除氮菌提高了污水中COD、氨氮及总磷的去除率，对COD的去除率可以提高10％左右，总磷最高可提高20％，试验三天，对氨氮的去除率也提高20％-30％。     

BATCH REACTOR UNVEGETATED WETLAND PERFORMANCE IN TREATING DAIRY WASTEWATER1

ABSTRACT: Wetlands that treat holding pond effluent can be designed to utilize the pond storage capacity to allow flexibility in system management. Management of a wetland as a sequencing batch reactor can simplify operation and control detention times, but little performance data on such systems are available. The objective of this study was to evaluate the batch reactor wetland concept by quantifying removal of chemical oxygen demand (COD), total suspended sediments (TSS), total nitrogen (TN), ammonium (NH₄), nitrate (NO₃), total phosphorus (TP), and orthophosphate (PO₄) and by assessing the suitability of first‐order kinetics. Weekly samples were collected following batch loadings of wetland cells with high concentration or low concentration dairy holding pond wastewater during both fall and spring seasons. During three‐week batch periods without plants, overall mass removal averaged 54 percent for COD, 58 percent for TSS, 90 percent for TN, 72 percent for NH₄, ‐54 percent for NO₃, 38 percent for TP, and ‐8 percent for PO₄. Best fit, first‐order kinetic rate constant (k) and background concentration (C*) for COD varied by season, with k = 0.024/d and C*= 0 mg/l in fall and k = 0.056/d and C*= 200 mg/l in spring. Ammonium exhibited a consistent C*= 0 mg/l but had variable rate constants of k = 0.121/d for low concentration treatments and k = 0.079/d for high concentration treatments. Using first‐order kinetics was also appropriate for TN, with k = 0.061/d and C*= 0 mg/l for all loadings and seasons, but was not consistently appropriate for TP or PO₄. These results support the use of first‐order kinetics to describe treatment in batch reactor wastewater treatment wetlands without vegetation, perhaps during the establishment phase or in open water zones of vegetated wetlands. Further work is needed to assess the effects of vegetation.     

Microcosm wetlands for wastewater treatment with different hydraulic loading rates and macrophytes

Constructed wetlands (CW) usually require large land areas for treating wastewater. This study evaluated the feasibility of applying CW with less land requirement by operating a group of microcosm wetlands at a hydraulic retention time (HRT) of less than 4 d in southern Taiwan. An artificial wastewater, simulating municipal wastewater containing 200 mg L(-1) of chemical oxygen demand (COD), 20 mg L(-1) of NH4+-N (AN), and 20 mg L(-1) of PO4(3-)-P (OP), was the inflow source. Three emergent plants [reed, Phragmites australis (Cav.) Trin. ex Steud.; water primrose, Ludwigia octovalvis (Jacq.) P.H. Raven; and dayflower, Commelina communis L.] and two floating plants [water spinach, Ipomoea aquatica Forssk.; and water lettuce, Pistia stratiotes L.] plants were tested. The planted systems showed more nutrient removal than unplanted systems; however, the type of macrophytes in CW did not make a major difference in treatment. At the HRTs of 2 to 4 d, the planted system maintained greater than 72,80, and 46% removal for COD, AN, and OP, respectively. For AN and OP removal, the highest efficiencies occurred at the HRT of 3 d, whereas maximum removal rates for AN and OP occurred at the HRT of 2 d. Both removal rates and efficiencies were reduced drastically at the HRT of 1 d. Removals of COD, OP, and AN followed first-order reactions within the HRTs of 1 to 4 d. The efficient removals of these constituents obtained with HRT between 2 and 4 d indicated the possibility of using a CW system for wastewater treatment with less land requirement.     

Performance and modeling studies of rotating biological contactor for treatment of vegetable oil wastewater

This study focuses on a lab-scale rotating biological contactor (RBC) treating vegetable oil wastewater with high BOD and COD. The fabricated RBC was checked for efficiency in degrading polluted wastewater under different operating conditions. The maximum removal efficiencies for BOD and COD were 95.75% and 89%, respectively. This high removal percentage was obtained with 30% submergence of 10 discs rotating at 8 rpm. For the first time, bio-kinetic models were applied to the experimental results for vegetable oil wastewater. The best fit was obtained with the modified Stover-Kincannon and Grau model. The saturation constant (K_s) values were 1.872 and 3.024 g/L/d for BOD and COD, respectively, for the modified Stover-Kincannon and Grau model. For the Grau second-order model, the saturation constant was 1.416 and 3.744 g/L/d for BOD and COD, respectively. The predicted effluent BOD and COD values of the modified Stover–Kincannon model fitted almost exactly with the experimental values. This clearly predicts that this model can be best used to predict effluent BOD and COD concentration in a Rotating Biological contactor treating vegetable oil wastewater. The kinetic parameters determined in this study can be used to improve the design and operation of continuous mode RBC systems.     

人工湿地-氧化塘工艺组合对氮和磷去除效果研究

本文在小试规模上，研究了下行流湿地、推流床湿地、氧化塘和兼性塘四种处理单元的四种工艺组合对氮、磷的去除效果，研究结果表明：下行流湿地 氧化塘工艺组合具有较好的充氧效果，推流床湿地后置也可以提高出水的溶解氧。四种工艺组合对离子和TP、IP的去除无显著差异。人工湿地中硝化作用的发生有利于NH^ 4f-N的去除，增加氧化塘可以提高系统的硝化能力，但同时也会增加出水中的N0^-3-N浓度。     

香根草人工湿地处理生活污水的试验研究

通过建立香根草人工湿地系统,研究该系统对生活污水的COD、TP、TN的处理效果以及系统的耐污性。在水力停留时间(HRT)为6h的条件下,COD、TP、TN的去除率分别为63.5%、88.3%、72.4%。研究表明,香根草人工湿地系统对城镇生活污水具有较好的净化效果,且系统在该试验条件下耐污性良好。     

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.     

Effects of bed materials on the performance of an anaerobic sequencing batch biofilm reactor treating domestic sewage

The objective of this study was to determine the best performance of an anaerobic sequencing batch biofilm reactor (AnSBBR) based on the use of four different bed materials as support for biomass immobilization. The bed materials utilized were polyurethane foam (PU), vegetal carbon (VC), synthetic pumice (SP), and recycled low-density polyethylene (PE). The AnSBBR, with a total volume of 7.2L, was operated in 8-h batch cycles over 10 months, and fed with domestic sewage with an average influent chemical oxygen demand (COD) of 358+/-110mg/L. The average effluent COD values were 121+/-31, 208+/-54, 233+/-52, and 227+/-51mg/L, for PU, VC, SP, and PE, respectively. A modified first-order kinetic model was adjusted to temporal profiles of COD during a batch cycle, and the apparent kinetic constants were 0.52+/-0.05, 0.37+/-0.05, 0.80+/-0.04, and 0.30+/-0.02h(-1) for PU, VC, SP, and PE, respectively. Specific substrate utilization rates of 1.08, 0.11, and 0.86mg COD/mgVS day were obtained for PU, VC, and PE, respectively. Although SP yielded the highest kinetic coefficient, PU was considered the best support, since SP presented loss of chemical constituents during the reactor's operational phase. In addition, findings on the microbial community were associated with the reactor's performance data. Although PE did not show a satisfactory performance, an interesting microbial diversity was found on its surface. Based on the morphology and denaturing gradient gel electrophoresis (DGGE) results, PE showed the best capacity for promoting the attachment of methanogenic organisms, and is therefore a material that merits further analysis. PU was considered the most suitable material showing the best performance in terms of efficiency of solids and COD removal.