波形潜流人工湿地污水处理的研究

波形潜流人工湿地包括水平流、上行流和下行流在内的混合流态,集合了潜流人工湿地和垂直流人工湿地的优点,优于传统潜流人工湿地。本文主要结合波形潜流人工湿地的特点,探讨波形人工湿地微生物群落结构及污染物去除机理,为强化波形潜流人工湿地的净化功能提供参考。     

人工湿地黑臭水体处理系统微生物脱氮机理研究

以上海市老段浦I、II和北夏3座水平潜流人工湿地黑臭河道处理系统为研究对象,进行了水平潜流湿地处理黑臭河道氨氮的转化及脱氮机理的研究。研究表明,3座人工湿地的pH值均呈弱碱性,且沿湿地水流方向变化较小。溶解氧值在0.09—0.35mg/L范围内波动,氨氮沿湿地的流向呈递减的趋势,亚硝态氮及硝态氮浓度较低。在老段浦人工湿地的同一土样中,亚硝化细菌的数量远大于硝化细菌的数量,北夏人工湿地中,湿地前端的亚硝化细菌与硝化细菌的数量近似相等,但在湿地末端亚硝化细菌数量要远小于硝化细菌的数量。原位曝气抑制反硝化反应试验研究表明,3座人工湿地都发生了"新"的脱氮途径-短程硝化-反硝化反应,其中两座老段浦人工湿地50%的氮以短程硝化-反硝化反应去除。北夏人工湿地中约20%的氮以短程硝化反硝化的途径去除。       

人工湿地污水处理系统三种红树植物抗性生理特性

研究了淡水条件下潜流型人工湿地污水处理系统中红树植物海桑、桐花树和木榄的抗性生理特性.结果表明,在为期1年的试验中,人工湿地污水处理系统3种红树植物超氧物歧化(SOD)、过氧化物酶(POD)和过氧化氢酶(CAT)活性持续升高并维持在较高水平,脯氨酸含量在7～9月达到最高水平,质膜透性没有明显的变化规律.对人工湿地与深圳福田自然保护区3种红树植物抗性生理指标进行比较,前者SOD、POD和CAT活性明显低于后者,脯氨酸含量前者明显高于后者,而丙二醛（MDA）含量和质膜透性则两者没有差别.3种红树植物能较好地适应淡水条件下潜流型人工湿地污水处理系统.     

抚仙湖窑泥沟人工湿地的除磷效果研究

为了减缓和控制抚仙湖局部湖湾水体富营养化趋势,在抚仙湖北岸建设了净化面积1 hm²的人工湿地.综合利用生物氧化塘、水平潜流人工湿地和表面流人工湿地治理技术,对入湖河道窑泥沟污水中磷的去除效果进行了试验研究.结果表明,该人工湿地系统对磷具有较强的去除能力.总磷去除率在57.7%～81.10%之间,平均去除率为54.9%.单位面积磷滞留量平均为26 mg·m^-2·d^-1,其中,湿地植物同化作用磷滞留量为26.1 mg·m^-2·d^-1,约占磷滞留总量的10%,大部分磷去除是通过基质吸附和沉降作用,但主要湿地植物水芹的季节变化对相应功能区的除磷效果会产生一定影响.试验期间,各功能区单位面积磷滞留量依次为水平潜流人工湿地＞生物氧化塘＞沉淀池＞表面流人工湿地.     

柊叶和象草波式潜流人工湿地的对比研究

为探索柊叶和象草在人工湿地中的应用及其净化机理,该研究以柊叶和象草为人工湿地植物分别构建了波式潜流人工湿地系统,分析了柊叶和象草波式潜流人工湿地对生活污水中COD_(cr)、TN和TP的净化效果,观察了柊叶和象草两种植物在不同季节的生长状况。结果表明:经过15个月的连续运行,在表面水力负荷约0.3 m·d~(-1)的条件下,柊叶和象草波式潜流人工湿地平均去除率是COD_(cr)分别为66.1%和70.1%,TN分别为60.4%和63.7%,TP分别为74.1%和75.1%。两种植物生长良好,根系发达,象草的地上生物量是柊叶的2.1倍,地下生物量相当;冬季象草生长缓慢,柊叶部分叶片的四周干枯,但二者都不会枯亡。这说明两个人工湿地对COD_(cr)、TN和TP都具有较好的去除效果,但无显著性差异,柊叶和象草能明显提高潜流人工湿地的净化效果。     

人工湿地去污模型的统一结构特征

通过对典型人工湿地去污模型的分析比较,提出了基于各模型微分方程而建立的统一去污模型。该模型能够将典型去污模型作为特例而导出,并能很好地解释这些模型之间的过渡关系。以潜流湿地中NH4^＋和BOD5的降解为例,对统一去污模型的应用情况进行了简单探讨,表明利用统一去污模型结构有助于深入揭示去污机理,从而提出更为精确的去污模型。     

潜流湿地和表面流湿地的净化效果与植物生长比较

分别以砾石和土壤为填料构建成潜流人工湿地和表面流人工湿地,处以较大水力负荷的污水处理。比较了两种湿地对污水的净化效果,结果表明在较大水力负荷条件下两种湿地的净化效果都较差,但潜流湿地对各种污染物的净化能力都优于表面流湿地;土柱法测量了湿地植物的根系生物量,结果显示湿地植物地上部分长势差异不明显,但潜流湿地的根系生物量显著低于表面流湿地的根系生物量(P<0.05)。结合前期实验结果得出湿地净化效果不仅与湿地植物根系生物量有相关关系,还与其他因素有一定的相关关系。     

水平潜流人工湿地堵塞初期微生物群落结构变化

为了寻找合适的湿地堵塞监测指标,文章通过运行4组湿地装置来模拟水平潜流人工湿地堵塞的过程,并研究人工湿地中微生物群落在湿地堵塞初期的响应。在人工湿地反应器运行过程中,定期监测基质过滤速率与人工湿地处理性能,包括化学需氧量(COD)、总氮(TN)和总磷(TP)去除效率,同时应用高通量测序技术测定并分析湿地反应器中微生物群落结构组成与多样性。结果表明:随着堵塞的形成,在4组人工湿地中,基质过滤速率和TP的去除效率持续下降,而COD和TN的去除效率分别为50%—85%和10%—20%; 16S rDNA测序结果表明堵塞会降低细菌群落的丰富度和多样性;人工湿地系统中的优势菌门主要是变形菌门(Proteobacteria)、厚壁菌门(Firmicutes)和绿弯菌门(Chloroflexi)等,且当湿地进入堵塞初期后,变形菌门丰度明显增加,具体表现为其门下的反硝化细菌属(Thauera、Zoogloea和Rhizobium)丰度显著增加,此外厚壁菌门和绿弯菌门的有机物降解菌属(Clostridium sensu stricto、Gracilibacter和Levilinea)的丰度也明显增加,这...     

人工湿地污水处理工艺设计关键及生态学问题

人工湿地污水处理系统是一种经济高效的污水生态处理技术方式．然而,湿地污水处理技术在性能上仍须有待发展与完善,尤其需要对其处理工艺参数进行不断改进和系统优化．本文针对人工湿地污水处理工程中有关水力停留时间、水传导因素、表面负荷率和工程构筑物设计等技术参数,概括性地剖析、探讨了国内外人工湿地污水处理工艺的设计关键及其主要技术内涵,给出了一些重要的优化模型与最佳数值;与此同时,分析、提出了利用生态学方法克服人工湿地工程运行中所涉及的野生生物管理与蚊蝇控制等问题。     

利用人工湿地去除农业径流中农药的研究进展

人工湿地对农业径流污染物去除效果显著,已成为控制农业径流污染的有效措施.本文结合国内外研究,介绍了当前水体农药污染的现状;从物理、化学及生物角度阐述了人工湿地对农药的去除机理和关键过程;归纳总结了人工湿地对农药的去除效率,指出人工湿地对农药的去除效率随农药类型的不同而差异较大:农药的平均去除率,按农药用途分为杀虫剂＞杀菌剂＞除草剂,按农药化学结构分为拟除虫菊酯类>有机磷类>三唑类＞酰胺类＞三嗪类＞脲类;综合考虑,潜流人工湿地在农药去除方面的效果优于表面流人工湿地.在此基础上分析了农药理化性质、人工湿地工艺类型及运行参数、进水中农药浓度、湿地植物等因素对农药在人工湿地中去除的影响.最后指出了当前研究中存在的问题,并提出了研究展望.     

Modelling pollutant removal in a pilot-scale two-stage subsurface flow constructed wetlands

The hydraulic behaviour and effluent pollutant concentrations in a pilot-scale two-stage subsurface flow constructed wetland for treatment of municipal wastewater have been simulated. The experimental pilot plant is located in San Michele di Ganzaria (Eastern Sicily) and consists of four lines of two-stage subsurface flow constructed wetlands for secondary or tertiary treatment of municipal wastewater. The first stage, for each line, consists of a horizontal flow bed, while in the second stage a vertical flow bed operates for two lines and a horizontal flow bed for the other two. Phragmites sp. was used as vegetation in two lines while the other two lines are without plants. The HYDRUS-2D software was applied to describe flow and single-solute transport, while the multi-component reactive transport module CW2D was used to model the transformation and elimination processes of organic matter, nitrogen and phosphorus. Tracer studies and chemical wastewater analyses were carried out to calibrate and validate the transport model. In general, the simulation results obtained show a good match with the measured data for water flow, tracer experiments and pollutant removal processes.     

Hydraulic performance of horizontal subsurface flow constructed wetlands for different strategies of filling the filter medium into the filter basin

A quasi-two-dimensional flow cell model of a horizontal subsurface flow constructed wetland was used to investigate how partitioning the wetland into smaller vertical sections prior to filling a heterogeneous filter medium into the filter basin altered the filter material packing and thereby the flow distribution. The flow through the filter medium was visualized using Nigrosine dye. Breakthrough curves for the flow cell were obtained using chloride tracer. Three inlet–outlet configurations were examined to assess the effects of the inlet and outlet positions on the flow since the inlet–outlet locations in addition to the filter medium heterogeneity may promote the development of preferential paths and dead zones. The filter medium packing patterns were dependent on the number of sections. If the wetland model was not partitioned prior to filling (one section), the filter material formed roughly horizontal layers with alternate layers of coarse and fine material. However, increasing the number of sections reduced the layer continuity and increased the flow distribution. This yielded longer retention times and higher hydraulic efficiency factors. The effect of the inlet–outlet configuration on the hydraulic parameters was greater when the number of sections was small. These results suggest that dividing the constructed wetland into several sections prior to filling the filter medium into the basin will improve the treatment efficiency.     

Energy requirements for nitrification and biological nitrogen removal in engineered wetlands

Nitrogen in wastewater degrades aquifer and surface water quality. To protect water quality in the United States, nitrogen discharge standards are strict: typically 1.0 mg/L NH₄-N for discharge to surface water and 10 mg/L total nitrogen (TN) for discharge to soil. Passive constructed wetland treatment systems cannot meet the nitrification standards discussed in this paper, using loading rates commonly considered to be cost-effective based on economic conditions in North America. Although partial nitrification can be achieved with some vertically or intermittently loaded, subsurface flow (SSF) wetlands, complete nitrification cannot be achieved in these passive wetland treatment systems. Engineered wetlands (EWs) use mechanical power inputs via pumping of air or water to nitrify wastewater, and have evolved in large part to nitrify wastewater. The design energy requirements for these power inputs have yet to be described in the wetland treatment literature. Our paper investigates the energy and area requirements of three wetland technologies: aerated subsurface flow, tidal flow, and pulse-fed wetland treatment, compared to a mechanical activated-sludge treatment system.     

The flower and the butterfly constructed wetland system at Koh Phi Phi—System design and lessons learned during implementation and operation

In 2007, a constructed wetland system was implemented on the tourist island of Koh Phi Phi in Southern Thailand. This paper presents the process of planning, designing and implementing the system and discusses the performance and operational issues 3 years after implementation. The system is an international lighthouse project showing the potential for aesthetical integration of constructed wetland systems in the built environment. The system comprises a wastewater collection system for the main business and hotel area of the island, a pumping station and a pressure pipe system to the treatment facility, a multi-stage constructed wetland system, and a system for reuse of treated wastewater. The treatment chains consist of vertical-flow, horizontal subsurface flow and free water surface flow units. Because the treatment system is located at the centre of the island, surrounded by resorts, restaurants and shops, the systems are designed with terrains as scenic landscaping. The wastewater is treated to meet the Thai effluent standards for total suspended solids and nitrogen, but because of inadequate pre-treatment and removal of oil and grease prior to the system, the standards for oil and grease and BOD are not met. A number of challenges during construction and operation have caused problems with clogging of the vertical flow constructed wetlands and given rise to odour problems. Safeguards were prepared, but not effectively activated, mainly because no key-person or key-authority took responsibility for managing the system.     

Removal of dimethylphenols and ammonium in laboratory‐scale horizontal subsurface flow constructed wetlands

Phenolic compounds in industrial wastewaters are toxic pollutants and pose a threat to public health and ecosystems. More recently, focus is being directed toward combining the treatment of these compounds with a cost‐effective and environmentally sound technology. The removal efficiency of dimethylphenol and ammonium nitrogen was studied, for the first time, in three different laboratory‐scale horizontal subsurface flow constructed wetlands planted with Juncus effusus. Two of the wetlands used were filled with gravel. One of these was planted and the second left without vegetation. The third wetland was a hydroponic system. It was found that the removal efficiencies of dimethylphenol was dependent on the inflow loading of the contaminant and was higher in the planted systems. Both planted systems yielded 99% removal efficiency up to loads of 240 mg/d, compared to only 73% for the unplanted constructed wetland. Factors and processes such as redox dynamics, methanogenesis, reduction of ammonium and low nitrate and nitrite concentrations imply simultaneous aerobic and anaerobic dimethylphenol transformations. A significant surplus of organic carbon was detected in the planted wetlands, which may originate from intermediates of the dimethylphenol transformation processes and/or organic plant root exudates. The present study demonstrates that horizontal subsurface flow constructed wetlands are a promising alternative system for the treatment of effluents contaminated with dimethylphenol isomers.     

Removal of Anionic Surfactants from Wastewater Using a Constructed Wetland

Removal of anionic surfactants from municipal wastewater using a constructed wetland with a horizontal subsurface flow was studied in 2007 and 2008. Extraction spectrophotometry with methylene blue served to determine the analyte concentrations in individual samples. The anionic surfactant‐removal efficiency depended on actual conditions, mostly the treated water flow intensity, its temperature, and a redox‐potential gradient in the longitudinal profile of the wetland bed. It increased with decreasing inflow and increasing temperature. The average efficiency was 83.7% in 2007 and 81.7% in 2008; however, values higher than 85% were often determined during the summer period. On the other hand, the efficiencies were usually lower than 80% in winter, especially in periods with intensive precipitation and inflows. The average concentration of anionic surfactants in water taken at the outflow was lower than 0.65 mg/l (expressed as sodium dodecyl sulfate). The most significant fraction of anionic surfactants (almost 50%) was degraded at the beginning (1 m from the inflow zone) of the wetland bed. The rhizosphere aeration via the vegetation roots strongly supported the anionic‐surfactant removal.     

Hydrodynamics of vertical subsurface flow constructed wetlands: Tracer tests with rhodamine WT and numerical modelling

Typical unsteady unsaturated conditions can profoundly affect the hydrodynamics of vertical subsurface flow constructed wetlands. In this study we analyzed the hydrodynamics of a 33 m² vertical flow pilot plant, treating municipal secondary effluents. Three different saturation conditions were analyzed under several constant flux regimes: complete saturation, partial saturation with the free water table 20 cm over the bottom of the bed, and complete drainage. Tracer tests were performed in steady state conditions by dosing rhodamine WT as square input signals. Breakthrough curves were analyzed by means of both a classical residence time distribution analysis and an originally developed numerical plug-flow model with longitudinal dispersion adapted to the unsaturated conditions. We found that the degree of global mixing in the vertical flow constructed wetland increased as the water content increased; this effect was controlled by the hydraulic residence time of the system. Conversely, the degree of local mixing was inversely affected by water content; the dispersivity was 4.5, 10, and 14 cm for fully saturated, partially saturated and draining conditions, respectively. We explain the dependency of dispersivity on water content in physical terms; however, further studies are needed to mathematically include this relationship in numerical models that describe the behaviour of vertical flow constructed wetlands.     

Polishing low-biodegradable and saline industrial effluent in a full-scale horizontal subsurface flow constructed wetland: evaluation of bio-treatability and predictive power of kinetic models

Abstract

This study evaluates the bio-treatability performance and kinetic models of full-scale horizontal subsurface flow constructed wetland used for the tertiary treatment of composite industrial effluent characterized by high-salt content ranging from 5830 to 10,400 µS/cm and biochemical oxygen demand (BOD₅): chemical oxygen demand (COD) ratio below 0.2. The wetland vegetated with Phragmites australis was operated in a semi-arid climate under an average hydraulic loading rate of 63?mm/d. The results of a 4-year operation calculated based on the concentration of pollutants showed that the average removal efficiency of COD, BOD_5, and total suspended solids (TSS) were 17.5, 5.1, and 11.2%, respectively. The system reduced up to 6.5?±?0.7% of electrical conductivity presenting poor phyto-desalination potential without considering the contribution of evapotranspiration in water balance in contrast to satisfying performance for heavy metals reduction. The comparison of the kinetics of organic matter removal obtained by the first-order and Monod models paired with continuous stirred-tank reactor and plug flow regime showed that Monod-plug flow model provided the best fit with the constants of 2.01?g COD/m²·d and 0.3014?g BOD₅/m²·d with the best correlation coefficient of 0.610 and 0.968 between the predicted and measured concentrations, respectively. The low kinetic rates indicate that the process is capable of effluent polishing instead of purification due to the presence of organic compounds recalcitrant to biodegradation and a high level of salinity.     

生态修复工程条件下污染河流水质模拟和应用

生态工程是改善河流水质的重要手段,利用数学模型可以有效模拟水环境治理和预测生态修复工程效益.本文根据实际河流资料,应用WASP水质模型进行建模和验证,模拟和评估了河流的主要化学参数,进而研究了人工湿地和曝气复氧对河流水质的生态改善作用.结果表明: WASP水质模拟结果与实测水质数据拟合良好,可以对不同生态修复情景方案进行预测分析.合理减排、人工湿地、曝气复氧均可以降低河流水体中的污染物浓度、有效改善水质.在人工湿地系统中增加曝气复氧装置,将进一步提升河流水体的生态修复效率.以吉林省伊通河曝气条件下的人工湿地工程为例,分析了其生态修复效率.结果表明: 夏季的污染物去除效果最好,可能的原因为夏季气温较高,水体中的微生物活性较强.本研究对于污染河流环境的生态修复工程设计和运行具有指导意义.