ADMS-EIA模型在污水处理厂恶臭影响预测中的应用

正污水处理厂属于环保工程,项目运行后有利于减少污水中有害物质排放.污水处理厂在发挥环境效益的同时,也会对环境产生不利影响,诸如排放尾水、产生恶臭和污泥等污染物.其中恶臭是污水处理厂运行中不可避免的一个污染问题,而其影响预测评价也是污水处理厂环境影响评价工作中的重点.污水处理厂的恶臭主要来自格栅间、进水泵房、曝气沉砂池、初沉池、生化池、污泥浓缩池、污泥脱水机房和污泥堆     

光催化臭氧＋高速纤维球过滤工艺处理生化出水

城乡结合部入河口是指分散点源的生活污水、雨水等经二级处理后排入河道时的入口.这里的污水特点是水量大,一般要求达标入河,如在这里进行深度处理,可将污水变成杂用水,成为城市用水第二水源.故开发新颖、高效的入河口污水深度处理工艺已成为关注对象.     

聚合氯化铝铁(PAFC)絮凝剂污水除磷的研究

用聚合氯化铝铁(PAFC)絮凝剂对城镇生活污水除磷处理效果进行研究,研究内容包括:PAFC用量对模拟污水和实际生活污水除磷效果的影响,污水经PAFC处理后pH值的变化情况,污水酸度对除磷效果的影响,PAFC用量对模拟污水和实际生活污水除浊效果的影响.结果表明:铝铁复合絮凝剂有良好的除磷效果,除磷处理后磷含量可低于0.5mg·l-1,能达到生活污水国家一级排放标准;污水处理后pH值较稳定;除浊效果好,除浊率可达到95%以上.     

菰和菖蒲在污水中的生长特性及其净化效果比较

通过漂浮栽植菰(Zizania latifolia)和菖蒲(Acoruscalamus),研究了它们在低、中、高3种浓度污水中的生长特性及其对这3种浓度污水的净化效果.结果表明,菰和菖蒲均在中浓度污水中生长最好.菰在中浓度污水中的生物量显著高于低浓度和高浓度中;菖蒲在中浓度污水中的生物量略高于低浓度和高浓度中,但差异不显著.菰对中浓度污水中TN、NH3-N、TP和CODCr的去除率分别为97.4%、95.3%、98.5%和71.4%,对高浓度污水中TN、NH3-N、TP和CODCr的去除率分别为96.4%、97.7%、88.2%和76.1%,净化效果均显著高于低浓度中.菰可作为中、高浓度污水的净化植物.菖蒲净化中浓度污水的效果最好,对TN、NH3-N、TP和CODCr的去除率分别为97.5%、94.1%、98.5%和72.7%;对高浓度污水中的NH3-N和CODCr去除效果也较好,去除率分别为97.8%和86.7%,但对TN和TP的去除率分别为89.5%和70.9%,显著低于对低浓度和中浓度污水中TN和TP的去除率.图1表4参13     

上海市受纳污水河流中多溴联苯醚的生态风险评价

以上海市某污水处理厂出水及其受纳河流为研究对象,测定了19种多溴联苯醚(PBDEs)同系物的浓度和分布特征,估算了污水处理厂PBDEs的年度排放负荷,并初步评价了受纳污水河流PBDEs的生态风险水平.结果表明,污水、河流水体及沉积物中PBDEs的总浓度分别为5050 pg.L-1、1310 pg.L-1和3.8 ng.g-1干重,其中BDE-209为主要成分.在排污口下游,PBDEs并没有随距离的增加而明显降低.该污水厂每年通过污水排放的五溴、八溴和十溴联苯醚分别为2.2、5.1和56.2 g.生态风险评价表明,目前该污水厂污水受纳河流中PBDEs导致的生态风险较低.     

浮水植物处理对猪场污水中可溶性有机物组成的影响

采集江西省余江县规模化猪场污水,选取青萍(Lemna minor)、紫背浮萍(Spriodela polyrrhiza)和大薸(Pistia stratiotes)等3种浮水植物分别进行处理.通过布置4个半月的温室试验,研究浮水植物处理对污水中可溶性有机物(Dissolved organic matter,DOM)组成及其荧光特性的影响.在试验过程中,定期采样监测污水中可溶性有机碳(Dissolved organic carbon,DOC)、总氮(Total nitrogen,TN)和总磷(Total phosphorus,TP)去除效率的变化.试验结束后,收获浮水植物并测定其生物量、TN和TP浓度,以及叶绿素含量.同时,基于三维同步荧光和平行因子分析方法,对污水中DOM组分进行识别和分析.结果表明,浮萍科植物的生物量倍增时间更短,而大薸生物量和养分日累积量更大.随着培养天数的增加,浮水植物处理污水中DOC、TN和TP去除率分别达到75%、90%和80%以上,且明显高于对照处理.在猪场污水中,DOM组分主要包括一个类蛋白质组分和两个类腐殖质组分;培养初期,猪场污水以类蛋白质组分为主.随着试验天数的增加,类蛋白质组分比例呈显著降低的趋势,而类腐殖质组分逐渐增加.与对照相比,种植浮水植物显著降低污水中类蛋白质组分比例,而提高类腐殖质组分比例.此外,浮水植物处理显著降低污水DOM的新鲜度指数,而增加微生物性来源类腐殖质组分的比例.综上,浮水植物在改善猪场污水中有机养分去除效率的同时,提高了DOM组分的腐殖化程度.     

高碑店污水处理厂对改善通惠河水质净化贡献分析

北京东南郊的通惠河,是元朝时期挖掘的一条人工河道,上世纪中叶起,原北京市四城区和东郊化工路的生活污水和工业废水未经任何处理直接排入其中,使其成为了一条名副其实的污水河,整个流域也蒙受了巨大的污染.上世纪90年代,北京市政府投资建成了日处理量100万吨的高碑店污水处理厂.将污水通过通惠河南、北两岸的污     

在线固相萃取——高效液相色谱法紫外检测污水处理厂污水中直链烷基苯磺酸盐(LAS)

直链十二烷基苯磺酸盐(LAS)是合成洗涤剂中含有的重要阴离子表面活性剂之一.LAS进入水体后,与其它污染物结合形成分散胶体颗粒,对工业污水和生活污水的物理、化学和生化特性都有很大影响,并产生潜在的危险.GB 8978—1996《中华人民共和国国家标准污水综合排放标准》规定LAS一级排放限量为5 mg.L-1.     

利用化学分析和生物毒性监测方法综合评价污水污泥环境影响的研究

利用化学分析和发光细菌生物毒性联合检测方法评价了上海地区7处污水处理厂污水污泥(分别用S1～S7表示)中主要污染物水平和毒性大小.结果表明,污水污泥样品S5和S7的重金属超过CJ/T 309-2009《城镇污水处理厂污泥处置农用泥质》标准和全国平均水平,主要超标重金属为Cd、Hg和Cu;污水污泥中多氯联苯、有机氯农药和二(噁)英类含量与组成则处于安全水平;样点S1～S6的多环芳烃(PAHs)平均含量低于CJ/T 309-2009中A级标准与欧盟和美国关于污水污泥的土地倾倒标准,但样点S7的w(ΣPAHs)达到34.61 mg·kg-1,超过CJ/T 309-2009最高允许限值的6倍.污水污泥浸出液化学分析结果表明,PAHs和重金属含量低于GB 5085.3-2007《危险废物鉴别标准浸出毒性鉴别》和欧盟EN 12457.2-2002 《废弃物表征浸出颗粒废弃物和污泥浸出一致性试验》标准,但所有样点的溶解性总有机碳均超过欧盟EN 12457.2-2002标准.发光细菌综合生物毒性结果表明:样点S3的综合毒性最高,S1、S6和S7次之,S2、S4和S5较低,以生活污水为主要来源的污水污泥的综合生物毒性较高.该结果可为污水污泥的后续处理和处置提供基础数据.     

巢湖流域典型村庄生活污水水质年变化特征

为揭示巢湖流域典型村庄生活污水水质特征,本文采用定点定期采样法,对巢湖流域两类典型村庄生活污水水质进行了2年测定研究.结果显示,不同月份两村生活污水的COD、NH4+-N、TN、TP等指标呈现出相同的变化趋势,各指标浓度在6—8月较低,而COD和TN浓度在12—2月较高;两村的生活污水COD、NH4+-N、TN、TP全年变化范围为46.77—424.80 mg.L-1、4.30—17.40 mg.L-1、9.36—34.38 mg.L-1、0.27—3.06 mg.L-1;大汤村和电厂新村两村生活污水全年COD、NH4+-N、TN、TP平均值分别为171.98 mg.L-1和219.60 mg.L-1、8.07 mg.L-1和11.52 mg.L-1、17.80 mg.L-1和21.33 mg.L-1、1.15 mg.L-1和1.53 mg.L-1.     

Recovery of Ni(II) from real electroplating wastewater using fixed-bed resin adsorption and subsequent electrodeposition

Resin adsorption and subsequent electrodeposition were used for nickel recovery. Treated wastewater can meet the Electroplating Pollutant Discharge Standard. The spent resin is completely regenerated by 3 BV of 4% HCl solution. 95.6% of nickel in concentrated eluent was recovered by electrodeposition. Effective recovery of high-value heavy metals from electroplating wastewater is of great significance, but recovering nickel ions from real electroplating wastewater as nickel sheet has not been reported. In this study, the pilot-scale fixed-bed resin adsorption was conducted to recover Ni(II) ions from real nickel plating wastewater, and then the concentrated Ni(II) ions in the regenerated solution were reduced to nickel sheet via electrodeposition. A commercial cation-exchange resin was selected and the optimal resin adsorption and regeneration conditions were investigated. The resin exhibited an adsorption capacity of 63 mg/g for Ni(II) ions, and the average amount of treated water was 84.6 bed volumes (BV) in the pilot-scale experiments. After the adsorption by two ion-exchange resin columns in series and one chelating resin column, the concentrations of Ni(II) in the treated wastewater were below 0.1 mg/L. After the regeneration of the spent resin using 3 BV of 4% (w/w) HCl solution, 1.5 BV of concentrated neutral nickel solution (>30 g/L) was obtained and used in the subsequent electrodeposition process. Using the aeration method, alkali and water required in resin activation process were greatly reduced to 2 BV and 3 BV, respectively. Under the optimal electrodeposition conditions, 95.6% of Ni(II) in desorption eluent could be recovered as the elemental nickel on the cathode. The total treatment cost for the resin adsorption and regeneration as well as the electrodeposition was calculated.     

Ammonia removal from low-strength municipal wastewater by powdered resin combined with simultaneous recovery as struvite

• Powdered resin was employed for ammonia recovery from municipal wastewater. • Powdered resin achievedefficient ammonia removal under various working conditions. • Co-existing cations indicated competitive adsorption of ammonia. • Ammonia was recoveredby two-stage crystallization coupled with ion exchange. Low-strength municipal wastewater is considered to be a recoverable nutrient resource with economic and environmental benefits. Thus, various technologies for nutrient removal and recovery have been developed. In this paper, powdered ion exchange resin was employed for ammonia removal and recovery from imitated low-strength municipal wastewater. The effects of various working conditions (powdered resin dosage, initial concentration, and pH value) were studied in batch experiments to investigate the feasibility of the approach and to achieve performance optimization. The maximum adsorption capacity determined by the Langmuir model was 44.39 mg/g, which is comparable to traditional ion exchange resin. Further, the effects of co-existing cations (Ca²⁺, Mg²⁺, K⁺) were studied. Based on the above experiments, recovery of ammonia as struvite was successfully achieved by a proposed two-stage crystallization process coupled with a powdered resin ion exchange process. Scanning electron microscopy (SEM) and X-ray diffractometry (XRD) results revealed that struvite crystals were successfully gained in alkaline conditions (pH= 10). This research demonstrates that a powdered resin and two-stage crystallization process provide an innovative and promising means for highly efficient and easy recovery from low-strength municipal wastewater.     

Population dynamic studies on phytoplankton cultures

The use of ozone as an oxidative supplement to biological filtration and to control epizootic microbial outbreaks coincident with maintaining a biological filter was investigated in a 2,271-1 (600 gallon) closed marine-water system. Under conditions of a relatively large biomass load (1.82 kg/3801), filter-bed effluent levels of total ammonia (0.135±0.01 ppm), un-ionized ammonia (0.0074±0.0006 ppm) and nitrite (0.17±0.01 ppm) were maintained within acceptable limits. Reservoir ozonation (100 mg/h/380 l) further significantly reduced (P<0.005) these levels. Nitrates were significantly elevated (P<0.005) with ozonation. Cessation of ozonation elevated total ammonia, un-ionized ammonia and nitrite levels above acceptable limits within 24 h. Resuming ozonation rapidly reversed this trend. Ozone reduced the microbial content of the culture water. Ozonation is suggested as a means of maintaining oxidative flexibility when used as a supplement to biological filtration. Further, prevention of epizootic microbial outbreaks may be accomplished without danger to the biological filter provided a proper system design is utilized.Contribution No. 342, Department of Biology.     

D201树脂对双组分萘系化合物的吸附分离

用D201强碱性阴离子交换树脂自双组分水溶液中选择吸附分离1-氨基-2-萘酚-4-磺酸(1,2,4-酸)和2-萘酚,考察了溶液pH值、浓度、温度、树脂床高及流速等因素对吸附和分离系数的影响.结果表明,在pH 3—6时,树脂对1,2,4-酸有较高的吸附量及吸附选择性,利于1,2,4-酸与2-萘酚的选择性吸附分离.温度对吸附的影响较小,等温吸附规律符合Freundlich模型.动态吸附表明,至1,2,4-酸的泄漏点时,吸附流出液中几乎只含2-萘酚,1,2,4-酸被吸附于树脂上.随着树脂床层的增长或初始浓度和流速的减小,都使泄漏点推迟及分离系数提高.载酚酸的树脂柱可用15%质量比的NH4Cl和20%体积比的乙醇混合液定量洗脱1,2,4-酸.     

Treatment of methylene blue-containing wastewater using microorganisms supported on granular activated carbon under packed column operation

We studied the feasibility of using biological granular activated carbon-packed column in treating methylene blue-containing wastewater. The granular activated carbon with immobilized microbes was packed into a column and fed with 3 liter methylene blue-containing wastewater daily. With initial 1350 mg/l of methylene blue and 1550 mg/l of chemical oxygen demand, it was observed that the colour and chemical oxygen demand removal efficiencies were 99 and 78%, respectively. The high treatment performance of the system could be due to the simultaneous adsorption and biodegradation processes and advantages of immobilized microbes compare to suspended cell system.     

Migration of manganese and iron during the adsorption-regeneration cycles for arsenic removal

Fe-Mn binary oxide incorporated into porous diatomite (FMBO-diatomite) was prepared in situ and regenerated in a fixed-bed column for arsenite [As(III)] and arsenate [As(V)] removal. Four consecutive adsorption cycles were operated under the following conditions: Initial arsenic concentration of 0.1 mg·L^-1, empty bed contact time of 5 min, and pH 7.0. About 3000, 3300, 3800, and 4500 bed volumes of eligible effluent (arsenic concentration≤0.01 mg·L^-1) were obtained in four As(III) adsorption cycles; while about 2000, 2300, 2500, and 3100 bed volumes of eligible effluent were obtained in four As(V) adsorption cycles. The dissection results of FMBO-diatomite fixed-bed exhibited that small amounts of manganese and iron were transferred from the top of the fixed-bed to the bottom of the fixed-bed during As(III) removal process. Compared to the extremely low concentration of iron (<0.01 mg·L^-1), the fluctuation concentration of Mn²⁺ in effluent of the As(III) removal column was in a range of 0.01–0.08 mg·L^-1. The release of manganese suggested that manganese oxides played an important role in As(III) oxidation. Determined with the US EPA toxicity characteristic leaching procedure (TCLP), the leaching risk of As(III) on exhausted FMBO-diatomite was lower than that of As(V).     

壳聚糖改性沸石吸附废水中的苯酚

开发新型低成本苯酚吸附剂是含酚废水处理技术的重点.采用90%脱乙酰度壳聚糖制备改性沸石,在与天然沸石对比的基础上,研究了改性沸石去除废水中的效果.并对影响去除率的主要因素,包括壳聚糖与斜发沸石质量比、废水pH值,吸附时间,改性沸石用量,苯酚的质量浓度等进行研究.通过正交试验确定吸附废水中苯酚最佳工艺条件是:壳聚糖与沸石质量比为1∶20.沸石-壳聚糖颗粒吸附剂用量为12 g·L-1,废水中苯酚质量浓度不大于40mg·L-1,pH值为4～6,吸附平衡时间为35 min,苯酚去除率为90%;吸附适合用Langmuir吸附等温方程来模拟.     

Verhalten von Nanosilber in Kläranlagen und dessen Einfluss auf die Nitrifikationsleistung in Belebtschlamm

Background, aim and scope The application of nanosilver is increasing. Knowledge on the fate and behavior of nanosilver in wastewater and wastewater treatment plants is scarce. Studies under real world conditions are completely lacking. We studied (1) the impact of nanosilver on the nitrification of sewage sludge, (2) quantified the mass flow of nanosilver in a pilot-plant, and (3) verified the mass balance in a full-scale municipal wastewater treatment plant where nanosilver is introduced to the municipal plant by an indirect discharger. Materials and Methods The addition of four different nanosilver additives on ammonia oxidation in activated sludge has been studied in batch-reactors at two concentrations (1, 100?mg/L Ag) with two exposure times (2?h, 6?days). The pilot-plant treating 70 population equivalents of domestic wastewater is operated with a 12?day sludge age. Nanosilver was applied to the activated sludge tank within two sludge ages. The silver concentrations were measured in sludge and effluent samples during dosing and the following two sludge ages. The adsorption and speciation of silver particles has been analyzed using scanning electron microscopy (SEM) coupled with energy dispersive X-ray spectroscopy (EDX). Influent, effluent and sludge were sampled on a full-scale plant (60?000 equivalent inhabitants) and analyzed for silver. Results Silver nitrate, metallic nanosilver, nano-scaled silver chloride and microcomposite silver did not show any effect on ammonia oxidation after the addition of 1?mg/L Ag to the activated sludge (corresponding to 250?mg Ag per kg solids). In contrast, 100?mg/L Ag inhibited the nitrification process by 100?% after the addition of silver nitrate and 20–30?% after addition of colloidal polymer-coated nanosilver. A complete mass balance of the pilot-plant, a steady-state system with known fluxes, demonstrates significant enrichment of silver in the sewage sludge (96?%) after the addition of silver chloride to the plant and small losses of silver into the secondary effluent (4?%). The mass fluxes are similar to metallic colloidal nanosilver investigated under the same conditions. The mass balance has been consistently confirmed by the full-scale study in a municipal wastewater treatment plant. The silver fluxes correspond to the fluxes of the suspended solids in sludge and effluent. Overall, it is estimated that from public wastewater treatment plants about 4–40?mg/a Ag per inhabitant equivalent are discharged annually to the receiving water. The analysis by SEM-EDX demonstrates adsorption and incorporation of nanosilver on biological flocs. This method yields first insight into complex building and transformation of silver associated with sulfide after adding metallic nanosilver and silver chloride to wastewater. Discussion Silver ions released from nanosilver react immediately with large amounts of chloride present in wastewater to form silver chloride. Silver ions may react with organic ligands or sulfide groups additionally. Consequently, even silver nitrate added with 1?mg/L Ag (250?mg Ag/kg TS) to activated sludge did not inhibit nitrification activity. Very high amounts of nanosilver, i.?e. 100?mg/L Ag, overburdened the system and equilibrium condition between silver ion release and ligands was not reached. The mass balance reflects the excellent attachment of nanosilver to activated sludge and biological flocs. Therefore, the main elimination process of nanosilver is attachment to the activated sludge. The elimination of nanosilver is high compared to organic and inorganic micro pollutants omnipresent in wastewater. Any further reduction of suspended solids in the effluent water will reduce the silver load. Conclusions Generally, in wastewater nanosilver occurs bonded to activated sludge flocs and therefore the elimination of nanosilver is efficient under operation conditions typical for wastewater treatment plants. The major fraction of nanosilver is removed from the system by the excess sludge withdrawal. Nonetheless, the efficiency may be further improved by a tertiary filtration step. All analyses of influent, effluent and sludge confirmed that silver exists as silver sulfide. Due to a negligible water solubility of this silver species, silver ions are not subsequently released. Recommendations and perspectives Nanosilver research should be driven to the identification of transformation processes in real environmental matrices and the influence of coatings on the adsorption behavior. There is no need for action to take special measures for nanosilver removal in the area of municipal wastewater treatment plants compared to ubiquitous hazardous organic pollutants may present in wastewater. Nevertheless, source control measures following the precautionary principle should be performed.     

二段生物接触氧化法处理含硫废水的中试研究

用二段生物接触氧化法探索炼油过程中所产生的含硫废水的处理新方法． 结果表明：经此工艺处理后的出水 Ｃ Ｏ Ｄ、氨氮、硫化物和酚的质量浓度ρ分别为２６６ ．９ ｍｇ／ Ｌ、８２ ．８５ ｍｇ／ Ｌ、１ ．１８ ｍｇ／ Ｌ 和１ ．４３ ｍｇ／ Ｌ,相应的去除率分别为８６ ．３ ％ 、４０ ％ 、９２ ．７ ％ 和９９ ．３ ％ ,出水水质达到国家三级排放标准． 进出水水质的变化曲线表明,生物接触氧化法处理含硫废水对进水水质变化的适应能力比较强,出水水质比较稳定,显示了二段接触氧化法处理含硫废水的可行性     

Biodegradation of phenol by native microorganisms isolated from coke processing wastewater

The present investigation was undertaken to assess the biodegradation of phenol by native bacteria strains isolated from coke oven processing wastewater. The strains were designated ESDSPB1, ESDSPB2 and ESDSPB3 and examined for colony morphology Gram stain characters and biochemical tests. Phenol degrading performance of all the strains was evaluated initially. One of the strains namely ESDSPB2 was found to be highly effective for the removal of phenol, which was used as sole carbon and energy source. From an initial concentration of 200 mg I(-1) it degraded to 79.84 +/- 1.23 mg l(-1). In turn the effect of temperature (20 to 45 degrees C), pH (5-10) and glucose concentration (0, 0.25 and 0.5%) on the rate of phenol degradation by that particular strain was investigated. Observations revealed that the rate of phenol biodegradation was significantly affected by pH, temperature of incubation and glucose concentration. The optimal conditions for phenol removal were found to be pH of 7 (84.63% removal), temperature, 30 degrees C (76.69% removal) and 0.25% supplemented glucose level (97.88% removal). The main significance of the study is the utilization of native bacterial strains from the waste water itself having potential of bioremediation.