低温下曝气生物滤池预处理污染河水的试验研究

采用两段曝气生物滤床串联工艺预处理入滇新运粮河河水,研究了其在冬天低温条件下对有机物和氨氮的去除效果,并考察了pH值的变化。结果表明,在进水流量为2.4 m3.d-1、水温为13-16℃、原水ρ（CODCr）为66.46-107.82 mg·L-1、ρ（氨氮）为22.15-30.68 mg·L-1的水质特征条件下,系统对CODCr和氨氮的去除率分别为36.08%-50.37%和76.98%-93.56%。其中,碳氧化段以去除有机物为主,硝化段以去除氨氮为主;系统中硝酸氮质量浓度明显升高,无亚硝氮的积累;装置对总氮的平均去除率为19.56%,可以认为总氮的去除是同步硝化反硝化的结果。系统中pH值有所变化但维持在7-8之间,其中碳氧化段pH值升高,硝化段pH值下降。系统对有机物和氨氮良好的去除效果为后续进一步的生物处理提供了条件。     

以马蹄莲为主体植物的人工湿地处理低浓度污水中试研究

人工湿地中集污染物吸收效果好、生境改善、观赏性好和经济性好于一体的植物筛选将支持湿地的长效低耗运行。报道了以观赏性和经济性植物马蹄莲(Zantedeschia aethiopica)为主要植物的人工湿地中试床(5 m×1 m×1.1 m)处理低浓度农村污水的研究。结果表明,在水力负荷为6,10和20 cm.d-1的条件下,该系统对CODCr(化学需氧量)、TN(总氮)、硝氮、氨氮和TP(总磷)的去除率分别大于56.4%、71.4%、71.4%、49.6%和56.6%。同处旺盛生长期(8月)而温度相近时,低水力负荷(6 cm.d-1)组的硝氮、氨氮和TP的去除率高;高水力负荷(20 cm.d-1)组的TN去除率高,进水TN中的有机氮占的比例比低水力负荷(6 cm.d-1)的高10%。马蹄莲人工湿地系统在休眠期(6月和7月)和在旺盛生长期相比,由于温度高而具有高的CODCr和N去除率,由于枯枝落叶的腐烂溶出以及进水负荷高而具有低的TP去除率。研究结果可为人工湿地等生态系统中选择植物时参考。     

人工快速渗滤法处理小城镇污水的模拟试验研究

小城镇污水既是水资源的主要污染源,同时也是可利用水资源的重要组成部分,高效率、低成本的小城镇污水处理技术是农业生态安全和工程节水的急需。研究采用人工快速渗滤方法处理小城镇污水,在湿干比一定（湿干比1∶3）的条件下设3种填料比[V（土）∶V（砂）=1∶1、2∶1和3∶1）和3种不同水力负荷周期[短周期（0.5 d进水,1.5 d落干）、中周期（1 d进水,3 d落干）和长周期（3 d进水,9 d落干）]进行交叉试验。跟踪测定处理后水中COD、总磷、凯氏氮和铵氮的去除率。结果表明,系统的COD和总磷去除效果较好,最高去除率分别达到73.19%和54.86%。COD的去除受水力负荷周期影响较大,在长水力负荷周期条件下去除效率高,总磷的去除受水力负荷周期的影响小。系统对凯氏氮和铵氮的去除效率偏低,两者的最高去除率分别为46.67%和40.67%,均在长周期条件下取得。     

粉煤灰渗滤系统处理城市非点源污染物效果评估

对粉煤灰介质渗滤系统处理城市非点源污染物的效果进行了研究.吸附实验表明粉煤灰对氨氮和磷酸盐具有良好的吸附能力.渗滤系统对雨水径流污染处理采用室内小试的方式进行,在70 d内共模拟33次雨水负荷,期间渗滤装置对溶解有机碳(DOC)的平均去除率为88.1%,总氮(TN)的平均去除率为41.0%,氨氮(NH0-N)平均去除率为95.5%,总磷(TP)去除率为81.0%,符合城市非点源污染控制的实践要求.污染物去除主要以吸附过程为主,有机物、氨氮、磷的去除主要发生在渗滤柱表层的0—10 cm,硝化-反硝化主要发生在0—40 cm之间.滤层高度可以从130 cm适当减小为100 cm.吸附动力学表明粉煤灰对氨氮的吸附在3 h达到平衡,对磷酸盐的吸附平衡时间为6 h.微生物对渗滤系统的影响需要进一步研究,随着运行时间的延长,微生物效应将得以体现,污染物的去除效果可能会进一步提高.     

氨氮废水的厌氧氨氧化生物脱氮研究

利用从厌氧污泥中筛选和驯化的厌氧氨氧化（Anammox）菌直接启动UASB反应器,通过缩短水力停留时间（HRT）提高系统运行负荷,探讨水力停留时间对模拟废水脱氮性能的影响。结果表明,（1）富含Anammox菌的颗粒污泥能够快速启动反应器（只需14d）。（2）连续91d的HRT测试期间,系统具有良好的脱氮性能,且随着HRT的缩短,系统的脱氮效率具有波动上升的特点。NH4＋-N、NO2--N和TN（总氮）的平均去除率超过70.0%。（3）系统总氮容积负荷（TNLR）和总氮去除负荷（TNRR）最大值（以N计）分别为2.04kg·m-3·d-1和1.56kg·m-3·d-1。（4）系统能够比较好的遵循Anammox生物脱氮的理论途径：NH4＋-N、NO2--N的去除速率与NO3--N的生成速率的比例为1？1.15？0.22,与其相应理论值（1？1.32？0.26）非常接近。     

大清河人工快速渗滤系统示范工程效果分析

以滇池流域受污染的大清河为研究对象,开展了人工快速渗滤系统（CRI）示范工程研究,根据气候条件、进水水质和运行工艺分为6个工况,以探索污染负荷和工艺参数对CRI运行性能的影响。实验结果表明：水力负荷2 m.d-1、湿干比1：1是该示范工程运行的最优工艺条件。CRI系统对有机物（COD）的平均去除率范围17.42%～63.75%;对氨氮去除效果受进水水质影响,高、低污染负荷下NH3-N去除率分别为56.71%、85.48%;CRI示范工程硝化作用较强,反硝化能力较弱,对TN的平均去除率范围为10.69%～28.29%;CRI示范工程对TP的平均去除率为27.62%,最佳工艺条件下为50.23%。CRI系统可通过对填料进行优化组合、适当增大饱水带高度,强化除磷脱氮能力。     

人工增氧型复合湿地污染物净化效果

针对传统人工湿地负荷低、硝化能力弱和易堵塞的缺点,结合曝气生物滤池与人工湿地强化理论的研究成果,自主开发了人工增氧型复合湿地工艺,即生物接触氧化预处理+微曝气垂直流湿地+水平潜流湿地。通过对滇池北岸城郊混合制污水处理的模型试验,分析该工艺流程各净化单元的污染物去除效果。结果显示,人工增氧型复合湿地对不同水力负荷和污染负荷都体现了较强的缓冲调节能力和较高的净化效果。对污染物的总去除率分别为SS 94.5%、CODCr71.3%、氨氮72.3%,在进水总氮10.0 mg.L-1条件下实现了41.9%的总氮去除率,出水总氮均值为5.8 mg.L-1。     

电极生物膜自养脱氮系统中的电化学作用

设计构建三维电极生物膜反应器,成功启动后稳定运行,在全自养条件下能较好地处理低碳氮比含氮废水.结果表明,在进水不含有机碳源,电流强度为30 mA,电流密度为0.012 mA·cm-2,运行周期24 h的实验条件下,反应器处理进水氨氮浓度为30 mg·L-1的废水时,氨氮转化率达到了90.3%,总氮去除率为70.0%;处理进水硝态氮浓度为30 mg·L-1的废水时,硝态氮去除率达到了82.7%.在考察电极生物膜反应器脱氮性能的同时,探讨系统中纯电化学作用的脱氮能力.结果显示电极生物膜处理氨氮废水的系统中,纯电化学脱氮作用为系统总脱氮能力的10%左右;而处理硝态氮废水的电极生物膜系统中,无电化学还原去除NO-3-N作用.     

水华蓝藻厌氧发酵工艺技术研究

以太湖水华蓝藻为底物,用改进的CSTR(continuous stirred tank reactor)工艺,研究了不同有机负荷条件下蓝藻厌氧发酵相关参数与蓝藻藻毒素的去除效果.结果表明:在(35±1) ℃条件下,逐步提高有机负荷,系统运行稳定,有机负荷最高可达3.53 kg·m-3·d-1,此时最大容积产气率达0.89 m3·m-3·d-1,COD去除率在70%左右,甲烷体积分数达60%以上.不同负荷条件下,出料中藻毒素(MC-RR、MC-LR)检测均为阴性,已达无害化处理要求,表明该工艺可以有效处置水华蓝藻,实现能量回收与无害化处理的目标.     

活性污泥-人工湿地组合处理系统中污染物的去除

通过12个月的现场监测试验,研究了活性污泥法与四个串联潜流人工湿地构成的组合处理系统对农村生活污水的处理效果及其影响因素.结果表明,当平均处理量为82 T·d-1(36-132 T·d-1),湿地系统水力负荷为0.52-1.88 m·d-1时,组合处理系统对TSS,AN,TP,COD和BOD5的去除率分别为75%,71%,38%,81%和88%;湿地系统对COD,BOD5,SS,AN和TP的去除率分别为39%,55%,48%,5%和18%.方差分析表明,影响组合系统处理效果的主要因素是水力负荷及处理单元;湿地系统中有机污染物(COD,BOD5,SS)的去除主要是由第一块湿地完成的,而AN及TP的去除却呈现"累积"的特点;结合电子受体SO42-,NO3-及NO2-在湿地系统中的浓度变化趋势,推测湿地系统中有机污染物的生物去除主要是通过反硝化脱氮进行的,而通过硫酸盐还原(在硫酸盐还原菌的作用下)却是次要过程.     

Performance of an ANAMMOX reactor treating wastewater generated by antibiotic and starch production processes

A pilot-scale anaerobic ammonia oxidation (ANAMMOX) reactor was used to treat mixed wastewater resulting from a chlortetracycline and starch production process. The results, collected over the course of 272 days, show that the ratio of influent ammonium to nitrite, pH, and temperature can all affect the efficiency of nitrogen removal. The ratio of influent ammonium to nitrite was maintained at about 1:1 at a concentration below 200 mg·L^-1 for both influent ammonium and nitrite. The total nitrogen (TN) loading rate was 0.15–0.30 kgN·m^-3·d^-1, pH remained at 7.8–8.5, and temperature was recorded at 33±1°C. The rate of removal of ammonia, nitrite, and TN were over 90%, 90%, and 80%, and the effluent ammonium, nitrite and TN concentrations were below 50, 30, and 100 mg·L^-1.     

不同水力负荷下凤眼莲去除氮、磷效果比较

采用人工模拟方法,研究了不同水力负荷(0.14、0.20、0.33和1.00m3.m-2.d-1)对凤眼莲去除富营养化水体氮、磷效果的影响,试验期间进水TN、NH4+-N、NO3-N、TP平均质量浓度分别为4.85、1.33、2.92和0.50mg.L-1。结果表明,凤眼莲净化系统对富营养化水体具有较好的去除效果,低水力负荷(0.14、0.20m3.m-2.d-1)下,出水TN、NH4+-N和TP均达到了GB3838—2002《地表水环境质量标准》的Ⅳ类水质标准;当水力负荷提高到1.00m3.m-2.d-1后,出水TN、NH4+-N、NO3-N和TP质量浓度明显上升。4种水力负荷下,凤眼莲净化系统对TN和TP去除率分别为84.95%和80.65%、73.87%和73.04%、51.60%和64.05%、30.77%和47.79%,即随水力负荷的提高而降低;相应的TN、TP去除负荷分别为0.58和0.06、0.72和0.07、0.83和0.11、1.47和0.23g.m-2.d-1,即随水力负荷的提高而增加。综合考虑净化效果和污水处理能力,本试验条件下凤眼莲系统的水力负荷宜控制在0.33m3.m-2.d-1。     

Nitrogen removal performance of municipal reverse osmosis concentrate with low C/N ratio by membrane-aerated biofilm reactor

A membrane-aerated biofilm reactor was employed to investigate the nitrogen removal of one typical municipal reverse osmosis(RO) concentrate with a high total nitrogen (TN) concentration and a low C/ N ratio. The effects of operational conditions, including the aeration pressure, the hydraulic retention time and the C/N ratio, on the systematic performance were evaluated. The nitrogen removal mechanism was evaluated by monitoring the effluent concentrations of nitrogen contents. Furthermore, the microbial tolerance with elevated salinity was identified. The results indicated that the optimal TN removal efficiency of 79.2% was achieved of the aeration pressure of 0.02 MPa, hydraulic retention time of 24 h, and the C/N ratio of 5.8, respectively. It is essential to supplement the carbon source for the targeted RO concentrate to promote the denitrification process. The inhibitory effect of salinity on denitrifying bacteria and nitrite oxidizing bacteria was significant, revealing the limited TN removal capacity of the conditions in this work. The TN removal efficiency remained more than 70% with the addition of salt (NaCl) amount below 20 g/L. This work preliminarily demonstrated the MABR feasibility for the nitrogen removal of municipal RO concentrate with low C/N ratio and provided technical guidance for further scale-up application.

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膜生物反应器（MBR）处理垃圾渗滤液的脱氮研究

采用一体式MBR处理垃圾渗滤液,系统考察MBR对COD、NH4＋-N和TN的去除效果。结果表明：可将垃圾渗滤液的COD降至650-1 500 mg·L-1范围;在HRT为1.5 d、DO为0.75-1.20 mg·L-1、不排泥条件下运行时,对TN质量浓度低于2 300 mg·L-1、容积负荷低于0.25 kg.m-3.d-1（以N计）的渗滤液进行处理,MBR对NH4＋-N与TN的去除率可分别达到87%和72%以上。在MBR处理垃圾渗滤液的运行中发现,膜的污染速度较快,并且呈现＂两段性＂的规律,采用碱＋氧化剂的清洗方式可有效去除膜污染,降低过膜压力。     

低碳氮比废水好氧颗粒污泥系统稳定性及微生物种群多样性研究

低碳氮比(C/N)废水处理是含氮废水处理中的难题之一.本实验在C/N为4:1和2:1(COD和NH₄⁺-N浓度分别为400 mg·L^-1和100 mg·L^-1,400 mg·L^-1和200 mg·L^-1)条件下,考察好氧颗粒污泥系统对低碳氮比废水的处理效果、长期运行稳定性,研究C/N对好氧颗粒微生物结构变化的影响.研究结果表明,在C/N为4:1的废水中接种活性污泥培养好氧颗粒污泥,形成的颗粒沉降性能良好,MLSS为4.94 g·L^-1,SVI30为40 mL·g^-1,COD去除率90%以上,氨氮去除率接近100%.降低碳氮比,即C/N为2:1后,好氧颗粒的物理及硝化性能无明显变化,MLSS为11.38 g·L^-1,SVI₃₀/SVI₅维持在1左右,COD去除率大于85%,氨氮去除率98%.碳氮比降低使颗粒微生物多样性减少,其中陶厄氏菌受影响较小,而硝化功能菌出现更替:噬氢菌、食酸菌、里德拜特氏菌消失,鞘氨醇单胞菌、束缚杆菌等成为优势菌种.实验表明,该低碳氮比条件下好氧颗粒污泥系统能够稳定运行,且具有优良的处理性能.     

异养硝化细菌处理氨氮废水及影响因素研究

从生物陶粒反应器中筛选出6株异养硝化细菌,将异养硝化细菌扩大培养后,建立SBR反应器并进行了氨氮去除的试验研究。在SBR反应器进入稳定运行阶段时,可以观察到系统对于氨氮的去除率稳定在82．96％左右,表现出较好的氨氮去除效果;出水亚硝酸盐含量一直维持在较低的水平,其最大值不超过3．84mg·L-1;COD的平均去除率为54．72％,基本实现了同一反应器中的有机物和氨氮的共同去除。异养硝化SBR反应器温度为29℃时,反应器对氨氮和总氮的去除能力最大为82．28％和47．27％;在pH值为8．0时,氨氮去除率最高达到80．15％。C／N〈4．5时,随着C／N比的增加,氨氮和总氮的去除率快速增加;在C/N为6时,氨氮去除率最高达到87．62％。     

Influence of the sewage irrigation on the agricultural soil properties in Tongliao City, China

Increasing shortages of fresh water has led to greater use of treated wastewater for irrigation of crops. This study evaluates the spatial variability of soil properties after irrigation with wastewater and freshwater. Geostatistical techniques were used to identify the variability of soil properties at the different sites. A set of physical and chemical soil properties were measured including total nitrogen (TN), total phosphorus (TP), organic matter (OM) and soil moisture. The TN concentration levels varied from 567 to 700 mg·kg^-1, while OC levels ranged from 7.3 to 16.3 mg·kg^-1 in wastewater-irrigated zones. The concentration levels of TP were between 371.53 and 402.88 mg·kg^-1 for the wastewater-irrigated sites. Wastewater irrigation resulted in higher TN, TP and OM concentrations by 18.4%, 8% and 25%, respectively. The highest TN and OM occurred along the wastewater trunk. It was also observed that nitrogen concentrations correlate with the soil's organic matter. The increase of salinity may be associated with the increase of pH, which might suggest that a reduction of pH will be beneficial for plant growth due to the decrease of salinity. The average concentrations of nitrogen in topsoil were higher than those in subsurface soils in irrigated areas. Such differences of the N profile might be due to variations in organic matter content and microbial populations. Consistent with TN and OM, soil C:N decreased significantly with an increase of depth. This phenomenon possibly reflects a greater degree of breakdown and the older age of humus stored in the deeper soil layers. The analysis of pH levels at different depths for the three sites showed that pH values for wastewater irrigation were slightly lower than the controlled sites at the same depths.     

Research on polyhydroxyalkanoates and glycogen transformations: Key aspects to biologic nitrogen and phosphorus removal in low dissolved oxygen systems

In this paper, a study was conducted on the effect of polyhydroxyalkanoates (PHA) and glycogen transformations on biologic nitrogen and phosphorus removal in low dissolved oxygen (DO) systems. Two laboratory-scale sequencing batch reactors (SBR1 and SBR2) were operating with anaerobic/aerobic (low DO, 0.15–0.45 mg·L^-1) configurations, which cultured a propionic to acetic acid ratio (molar carbon ratio) of 1.0 and 2.0, respectively. Fewer poly-3-hydroxybutyrate (PHB), total PHA, and glycogen transformations were observed with the increase of propionic/acetic acid, along with more poly-3-hydroxyvalerate (PHV) and poly-3-hydroxy-2-methyvalerate (PH2MV) shifts. The total nitrogen (TN) removal efficiency was 68% and 82% in SBR1 and SBR2, respectively. In the two SBRs, the soluble ortho-phosphate (SOP) removal efficiency was 94% and 99%, and the average sludge polyphosphate (poly-P) content (g·g-MLVSS^-1) was 8.3% and 10.2%, respectively. Thus, the propionic to acetic acid ratio of the influent greatly influenced the PHA form and quantity, glycogen transformation, and poly-P contained in activated sludge and further determined TN and SOP removal efficiency. Moreover, significant correlations between the SOP removal rate and the (PHV+ PH2MV)/PHA ratio were observed (R²>0.99). Accordingly, PHA and glycogen transformations should be taken into account as key components for optimizing anaerobic/aerobic (low DO) biologic nitrogen and phosphorus removal systems.