垂直流人工湿地系统保护饮用水源的实例

简述了复合垂直流人工湿地污水处理系统专有技术的由来,并结合石岩人工湿地一期工程叙述了垂直流人工湿地的工艺原理、技术特点、植物特点、处理效果等,结果表明采用垂直流人工湿地生态污水处理系统保护饮用水源,能达到污水净化和美化环境的“双赢”目标。     

小型一体式污水处理装置脱氮效果研究

针对农村分散型污水水质稳定、水量小的特点,采用生物接触氧化与复合垂直潜流人工湿地组合技术,构建小型一体式污水处理装置,通过试验运行考察其脱氮效果.研究结果表明,在进水总氮、氨氮浓度为19.5 mg/L、11.8 mg/L情况下,装置出水分别为5.5 mg/L、4.7 mg/L.湿地系统中的脱氮主要发生在湿地表层0～20 cm.下行流湿地去除效果明显优于上行流湿地效果,是上行流湿地去除效果的2倍和3倍.通过生物+生态模块组合处理农村分散型污水,出水TN、NH3-N的平均去除率可达到71 8%和60 2%.     

垂直—水平流人工湿地系统除污效果研究

以武汉汉阳桃花岛城市面源污染控制示范工程为依托，研究示范工程中垂直—水平流人工湿地系统对生活污水的净化效果。结果表明，在人工湿地水力停留3 d的情况下，垂直—水平流人工湿系统对COD、SS、TP和TN均具有明显去除效果。其中，对COD、SS的去除率主要位于垂直流阶段，对TP和TN的去除率主要位于水平流阶段。水平流湿地中，种植黄花美人蕉的湿地单元对COD、TP和TN处理效果略高于种植鸢尾和红花美人蕉的湿地单元。     

人工湿地不同水流方式对生活污水净化的比较

通过小型复合流式人工湿地实验,监测了CODcr、TN、TP、NO3--N、NH4 -N等指标,旨在通过实验,找到处理污水的最佳水流方式.结果表明,垂直流和垂直流搭配对CODCr、TN、NH4 -N去除最好;而潜流和潜流搭配对NO3--N去除最好.人工湿地基质是影响磷的处理效果的主要因素,通过合理的操作方式可以最终从污水中除磷.在复合型人工湿地中延长水力停留时间能增加污染物的去除率.     

垂直流人工湿地对河涌污水的处理效果研究

研究垂直流人工湿地系统在珠江三角洲城市河涌污水净化中的作用。以广州市猎德涌为例,采用芦苇、风车草、宽叶香蒲、美人蕉4种不同植物构成的垂直流人工湿地对污水中NH4^＋—N、CODcr及TP的去除进行实验研究。结果表明,在水力停留时间3d、连续进水的情况下,4种植物对CODcr的去除效果差异性不是很显著。     

垂直潜流锰砂人工湿地处理钢铁废水

研究了以锰砂为填料的垂直流人工湿地处理钢铁废水的效果,试验结果表明:湿地系统对CODCr、Fe、Mn、TP、NH3-N的平均去除率分别为52%、97%、94%、95%和83%.夏季湿地对各种污染物的去除效果最好.HRT在2～5 d时,其改变对污染物的去除影响很小,低温条件对NH3-N的去除效果有一定的影响.对以Fe、Mn、浊度的去除为目的的人工湿地而言,在南方的冬季仍可达到良好效果.     

含镉废水人工湿地处理系统中基质微生物数量和酶活性研究

构建了美人蕉-红蛋(MH)和彩叶草-风车草(CF)两种不同植物组合的复合垂直流人工湿地系统,以不种植物的垂直流人工湿地系统(CK)为对照,研究不同湿地系统基质微生物数量和酶活性及其与无机废水中镉的去除效果的相关性。结果表明,在不同的植物系统中,微生物数量和酶活性为:MHCFCK;在同一个湿地系统中为下行池大于上行池;在有植物的系统中其微生物数量和酶活性的垂直分布为0~5 cm5~15cm15~20 cm;基质中真菌、放线菌数量和蔗糖酶活性与镉去除率呈显著正相关,而细菌数量和脲酶活性与镉去除率相关性不显著。     

组合工艺处理扎染废水的研究

采用水解调节池-厌氧折流反应池-组合好氧装置-垂直流人工湿地工艺处理扎染废水.厌氧折流反应池、好氧装置的设计容积负荷分别为0.5 kgCOD_(Cr)/(m~3·d)和0.3 kgCOD_(Cr)/(m~3·d),人工湿地水力负荷为0.35 m~3/(m~2·d).运行结果显示,系统运行稳定,污染物去除效果明显,COD_(Cr)、NH_3-N、TN和色度平均去除率分别为77%、85%、70%和89%,出水水质达到GB 18918-2002-级B标准.生化反应段对COD_(Cr)和色度的去除贡献率较大,而人工湿地对氮的去除较为明显,对COD_(Cr)去除贡献率相对较小.     

小型复合流人工湿地的设计及对有机物去除效率的分析

人工湿地能有效地处理污水，而且运转费用低。本文通过一个小型复合流人工湿地的设计及两个月的运作，监测了COD、NH3-N、NO3^-—N、NO2^-—N等指标，并分析了影响这些指标变化的主要因素，探讨该湿地对有机物的去除效率。实验结果表明，复合流人工湿地对有机物的去除效果较好，CODMn的去除率可达到60％～70％；植物在湿地污水处理中起着相当重要的作用；该湿地对NH3^-—N和NO3^-—N有一定去除效果，而对NO2^-—N的去除没有明显的效果。     

堵塞对湿地内水流流态及污水处理效果的影响

通过在污水中加入氯化钠示踪剂,研究人工湿地及其对照系统内水力停留时间的分布(HRTD),探讨潜流人工湿地和垂直流人工湿地中植物在堵塞前后对水流流态的影响,探讨堵塞对上述两种人工湿地水流流态的影响。结果表明:对于潜流人工湿地(SFCW),堵塞前湿地植物缩短了水力停留时间(HRT),堵塞后延长了HRT;对于垂直流人工湿地(VFCW),堵塞前湿地植物对水流流态无明显影响,堵塞后延长了湿地内的HRT。堵塞对湿地内水流流态影响明显,潜流和垂直流湿地由于堵塞其HRT分别延长了12.3%,22.6%。堵塞后湿地对污水的净化能力都要强于堵塞前,但是湿地的污水处理量减小,堵塞严重时湿地丧失其污水净化功能。     

不同植物配置人工湿地冬季生活污水净化效果比较

以某三级串联水平潜流人工湿地污水处理工程为实验基地,研究了5种华南地区常见湿地植物的选择和配置对净化冬季生活污水的影响,为华南地区人工湿地合理优化配置植物提供一定的依据。结果表明:人工湿地系统在冬季对COD、BOD5、TP和大肠菌群仍有较好的去除效果,对TN的去除效果较差。在实验条件下,COD和BOD5的降解主要发生在第一级湿地单元,TP和TN的降解主要发生在第三级湿地单元。三级串联湿地系统净化效果较佳的植物搭配是:第一级栽种水生美人蕉,第二级栽种再力花,第三级栽种菖蒲。     

沼液预处理最优混凝搅拌条件的研究

通过混凝法对沼液进行预处理最优条件的研究,为沼液预处理提供参考。在实验室条件下,对COD、TN、TP、色度和SS的去除率综合评价混凝工艺效果。实验中依次进行混凝剂投加量、助凝剂投加量、pH和搅拌强度的单因素实验,进而通过正交实验确定沼液预处理最优的混凝搅拌条件。试验结果表明:PAC投加量为4 g/L、PAM投加量为50 mg/L、搅拌速度为200 r/min、混凝阶段同时投加PAC和PAM,处理后的水样COD、TN、TP、色度和SS分别为216.20、181.99、0.18、11.77和71.67 mg/L,去除率分别达到92.51%、88.85%、99.75%、98.37%和89.46%,达到畜禽养殖业污染物排放标准(GB18596-2001),减轻了后续污水处理的负荷,为沼液实际处理提供了理论支持。     

Application of membrane bioreactor system with full scale plant on livestock wastewater.

A full-scale plant of an MBR system treating livestock wastewater has shown impressive results. The Cheorwon County Environmental Authorities adopted the MBR process with UF membrane for retrofitting the old plant, which removes organic matter, nitrogen and phosphorus at a high level. According to 6 months operation data, BOD and SS removal were about 99.9% and COD(Mn), TN and TP removal were 92.0%, 98.3% and 82.7%, respectively. It is considered that the temperature at the bioreactor has to be controlled to be below 40 degrees C so as to ensure sufficient nitrification. It appeared that the MBR system is competitive with other conventional technologies for treatment of livestock wastewater such as piggery waste.     

土壤过滤系统处理农村生活污水的 试验研究

采用一种土壤过滤系统处理农村生活污水,考察了该工艺对CODCr、BOD5、NH3-N、全氮（TN）和全磷（TP）的去除效果。实验结果表明,当水力负荷约为0.05 m3/（m2·d）, 水力停留时间为3 d时。该土壤过滤系统对CODCr、BOD5、NH3-N、全氮（TN）和全磷（TP）的去除效果较好,平均去除率分别达到84.6%、83.3%、64.3%、59.8%和70%。出水CODCr约为18.3~42.1 mg/L,BOD5约为8.9~17.3 mg/L,NH3-N约为11.2~17.7 mg/L,TN约为21.2~31.3 mg/L,TP小于2.0 mg/L,出水水质优于农田灌溉水质标准（GB 5084—2005）。气温变化和进水污染物浓度对处理效果影响明显。总体上来讲,温度大于22 ℃时,进水污染物浓度越低处理效果越好。     

折流式曝气生物滤池设备的开发及应用研究

针对三峡库区小城镇生活污水处理特点,研发折流式曝气生物滤池(BBAF)设备,通过将多级串联组合式BAF集成在同心圆式反应器内,形成了良好的力学性能和水力条件.在设计参数下运行时,对SS、COD、NH3-N、TN和TP的平均去除率分别为76％、83％、97％、26％和45％.高气水比有利于COD和NH3-N的去除,但会削弱TN、SS的去除效能,BBAF适宜的气水比为9.当处理负荷在1.5～3.0 m3/h范围内变化时,SS、COD和NH3-N的平均去除率无明显波动,出水水质稳定,表明设备具有较强的抗冲击负荷能力,对小城镇污水量变化系数大的特点具有很好的适用性.     

北方某人工湿地净化能力分析

在对北方某人工湿地长期观测取得的大量详尽数据的基础上,分析了人工湿地系统总体净化能力和潜流人工湿地水质动态变化特征。结果表明:该人工湿地示范工程对水质净化效果较为明显,对各类污染物的去除率平均可达40%;潜流人工湿地可对污水进行深度处理,对BOD5、NH4-N的去除效果最好,去除率为80%～90%,对NO3-N、TN的去除效果较好,去除率为65%～75%,对CODMn和SS的去除效果一般,去除率为40%～60%,对TP的去除效果随着时间推移逐渐减弱,碎石吸附对TP去除起主要作用。     

Application of subsurface wastewater infiltration system to on-site treatment of domestic sewage under high hydraulic loading rate

In order to enhance the hydraulic loading rate(HLR) of a subsurface wastewater infiltration system(SWIS) used in treating domestic sewage,the intermittent operation mode was employed in the SWIS. The results show that the intermittent operation mode contributes to the improvement of the HLR and the pollutant removal rate. When the wetting-drying ratio(R WD) was 1.0, the pollutant removal rate increased by(13.6 ± 0.3)% for NH3-N,(20.7 ± 1.1)% for TN,(18.6 ± 0.4)% for TP,(12.2 ± 0.5)% for BOD,(10.1 ± 0.3)% for COD, and(36.2 ± 1.2)% for SS, compared with pollutant removal rates under the continuous operation mode. The pollutant removal rate declined with the increase of the HLR. The effluent quality met The Reuse of Urban Recycling Water e Water Quality Standard for Scenic Environment Use(GB/T 18921-2002)even when the HLR was as high as 10 cm/d. Hydraulic conductivity, oxidation reduction potential(ORP), the quantity of nitrifying bacteria, and the pollutant removal rate of NH3-N increased with the decrease of the R WD. For the pollutant removal rates of TP, BOD, and COD, there were no significant difference( p 0.05) under different R WD s. The suggested R WD was 1.0. Relative contribution of the pretreatment and SWIS to the pollutant removal was examined, and more than 80% removal of NH3-N, TN, TP, COD, and BOD occurred in the SWIS.     

Performance evaluation of subsurface wastewater infiltration system in treating domestic sewage

This study was to investigate domestic treatment efficiency of a subsurface wastewater infiltration (SWI) system over time. The performances of a young SWI system (in Shenyang University, China, fully operated for one year) and a mature SWI system (in Shenyang Normal University, China, fully operated for seven years) under the same operation mode were contrasted through field-scale experiments for one year. The performance assessment for these systems is based on physical and chemical parameters collected. The removal efficiencies within the young system were relatively high if compared with the mature one: for biochemical oxygen demand (BOD), chemical oxygen demand (COD), suspended solids (SS), ammonia nitrogen (NH(3)-N) and total phosphorus (TP) were 95.0, 89.1, 98.1, 87.6 and 98.4%, respectively. However, the removal efficiencies decreased over time. The mean removal efficiencies for the mature SWI system were as follows: BOD (89.6%), COD (87.2%), SS (82.6%), NH(3)-N (69.1%) and TP (74.4%). The results indicate that the mature SWI system successfully removed traditional pollutants such as BOD from domestic wastewater. However, the nutrient reduction efficiencies (including NH(3)-N and TP) decreased after seven years of operation of the mature SWI system. Meanwhile, the SWI system did not decrease the receiving surface water quality.     

Kinetic study of slaughterhouse wastewater treatment by electrocoagulation using Fe electrodes

In this study, treatment of slaughterhouse wastewater by electrocoagulation was investigated in batch system using Fe electrodes. The effect of various variables such as electrode number, current density and operating time was tested. Pollutant removal efficiency increased with increasing electrode number and operating time. The biochemical oxygen demand (BOD(5))(,) chemical oxygen demand (COD), total suspended solid (TSS), and total nitrogen (TN) removal efficiencies using eight electrodes at a contact time of 50 min and a current density of 10 A/m(2) were 66, 62, 60, and 56%, respectively. Higher electrode numbers will allow shorter operating times to achieve certain removal efficiencies. Also, removal efficiencies increased by increasing the current density; the highest removal efficiencies of BOD(5,) COD, TSS, and TN at a contact time of 50 min and a current density of 25 A/m(2) were 97, 93, 81, and 84%, respectively. The results also show that the reactor pH varies directly with the current density; at 25 A/m(2), the reactor pH increased from an initial value of 7.1 to 7.7 after 50 min. The experimental results showed that the kinetics of BOD(5), COD, TSS and TN removal could be fitted adequately using a first order kinetic model (higher R(2)).     

Enhanced removal of chemical oxygen demand, nitrogen and phosphorus using the ameliorative anoxic/anaerobic/oxic process and micro-electrolysis

Synthetic wastewater was treated using a novel system integrating the reversed anoxic/anaerobic/oxic (RAAO) process, a micro-electrolysis (ME) bed and complex biological media. The system showed superior chemical oxygen demand (COD), total nitrogen (TN) and total phosphorus (TP) removal rates. Performance of the system was optimised by considering the influences of three major controlling factors, namely, hydraulic retention time (HRT), organic loading rate (OLR) and mixed liquor recirculation (MLR). TP removal efficiencies were 69, 87, 87 and 83% under the HRTs of 4, 8, 12 and 16 h. In contrast, HRT had negligible effects on the COD and TN removal efficiencies. COD, TN and TP removal efficiencies from synthetic wastewater were 95, 63 and 87%, respectively, at an OLR of 1.9 g/(L·d). The concentrations of COD, TN and TP in the effluent were less than 50, 15 and 1 mg/L, respectively, at the controlled MLR range of 75-100%. In this system, organics, TN and TP were primarily removed from anoxic tank regardless of the operational conditions.