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1.
以城市污水厂二级出水为研究对象,利用大孔吸附树脂将污水中溶解性有机物(Dissolved organic matter,DOM)分离成疏水酸性、中性、碱性物质和亲水性物质等4个组分,同时分析了各组分的有机物特性.结果表明,二级出水溶解性有机物中疏水酸性物质是二级出水溶解性有机物的主要组成部分.4种组分中均含有腐殖质类物质,疏水酸性物质(Hydrophobic acids,HOA)和疏水中性物质(Hydrophobic neutrals,HON)中腐殖酸类峰的荧光强度较大,亲水性物质(Hydrophilic fraction,HI)中的蛋白峰荧光强度较大.腐殖质类物质分子量分布较为单一,主要分布在0.9 k Da左右,而疏水性组分蛋白类物质分子量分布较为广泛,在200 k Da左右及小于9 k Da时均有一定分布,亲水性组分蛋白类物质主要由分子量小于9 k Da的物质组成.X射线光电子能谱(X-ray photoelectron spectroscopy,XPS)分析结果表明,HOA、HON中含有较多的芳香族化合物,而疏水碱性物质(Hydrophobic bases,HOB)、HI中则含有较多的羰基和羧基类官能团.  相似文献   

2.
好氧颗粒污泥胞外聚合物的产生及其分布   总被引:15,自引:0,他引:15  
考察了不同操作条件和基质条件对好氧颗粒污泥中胞外聚合物(EPS)产生的影响及其在污泥和体系上清液中的分布.结果表明:随体系操作条件和基质条件的变化,好氧颗粒污泥内部和上清液中的EPS含量呈规律性变化.相对而言,好氧颗粒污泥中EPS含量的变化幅度较小,过多的EPS则释放到上清液中.大量EPS的释放只发生在颗粒污泥解体时,而酸性条件和不适当的C/N比不利于好氧颗粒污泥的形成及形态保持.体系溶解氧为4.5 mg·l-1,pH为中性,污泥负荷小于等于0.37kgCOD·kg-1MLSS·d-1,碳氮比为20∶ 1时,好氧颗粒污泥中EPS的含量约占污泥总质量的9%-12%,与厌氧颗粒污泥(0.6%-20%)相近,但远低于絮状活性污泥(80%),此时,EPS在上清液中的含量最低或接近最低,为14-26 mg·l-1.  相似文献   

3.
对全国1982—2013年30个省市投运城镇污水处理设施现状、处理规模、运行负荷等进行统计分析,探讨了我国污水处理产业的发展历程、处理工艺和技术的演变趋势.分析表明,截止2013年,全国投运城镇污水处理设施4136座,总污水处理能力达到1.2×108m3·d-1,平均污水处理负荷率约为76.7%.污水处理设施的数目、规模以及处理能力存在明显的地域差异,东部发达地区明显高于西部欠发达地区.随着污水处理设施的发展,污水处理工艺也处于不断改进完善和探索中,而主体处理工艺的选择主要受到经济发展水平、地域特点等因素的影响.目前应用最多的主体工艺技术有厌氧-缺氧-好氧法(A2/O)、氧化沟工艺、循环活性污泥法(CASS)以及厌氧-好氧工艺(A/O)4种.近10年,CASS工艺在新建污水处理设施中的应用有逐渐增加的趋势.  相似文献   

4.
蛋白质和磷酸水解酶在废水处理系统中的活性和作用   总被引:1,自引:0,他引:1  
通过分析亮氨酸氨基肽酶和碱性磷酸酶,研究了厌氧-缺氧-好氧废水处理系统中蛋白质和磷酸水解酶的活性及其作用.结果表明,亮氨酸氨基肽酶存在缺氧和好氧池中的活性分别达19.2 цmol L-1 h-1和21.6 ц mol L-1 h-1;而碱性磷酸酶在厌氧池中占主导地位,平均活性达32.5 ц mol L-1,h-1,好氧池中的活性只有厌氧池的一半,缺氧池中的酶活性最小.动力学研究得到,厌氧条件碱性磷酸酶的最大反应速度v 为778.42 ц mol L-1 h-1,是亮氨酸氨基肽酶Vmax值的一百倍以上;亮氨酸氨基肽酶的Vmax值在厌氧、缺氧、好氧池中依次增大.此外,外加的NO2-、NO3-离子对亮氨酸氨基肽,酶和P043-离子对碱性磷酸酶的活性均有不同程度的促进作用,只有浓度为50 mg/L的P043-对碱性磷酸酶有显著的抑制.  相似文献   

5.
研究了蛋白质在厌氧-缺氧-好氧城市污水处理系统中吸附和降解的特性,分别确定了蛋白质在厌氧、缺氧和好氧条件下的吸附等温线模型,建立了蛋白质在厌氧、缺氧和好氧状态下的降解动力学模型,并对模型预测结果进行了验证分析,结果表明,Freundlich模型可以较好地描述蛋白质在厌氧、缺氧和好氧污泥卜的吸附过程,牛血清白蛋白水解成氨基酸是其生物降解过程的控速步骤,序批式动力学降解试验还表明,厌氧降解速率系数K厌、缺氧降解速率系数k缺与好氧降解速率常数的比值分别为0.40和0.98,说明在同一活性污泥系统的厌氧和缺氧条件下,蛋白质也能被较好地降解,模型得到的各池混合液出水中蛋白质的浓度模拟结果与实测结果相一致(相对误差<10%).无论在厌氧、缺氧还是好氧环境中,酸溶蛋白质没有积累.  相似文献   

6.
叶志伟  贝尔  汪隽  张晓健  陈超 《环境化学》2021,40(1):185-194
天然含氮有机物是水环境中的重要组成部分,其在天然水体中的形态及分布对环境质量有显著影响.本文围绕水中天然含氮有机物在氮循环中的地位、迁移转化以及其在国内主要水域中的分布情况,对天然含氮有机物的研究现状进行了梳理.我国不同水域中溶解性含氮有机物(DON)浓度相差较大;其中水体中DON浓度一般在1.0 mg·L-1以下;沉积物中DON浓度通常为几十至几百mg·kg-1.水体DON以分子量<1 kDa的有机物为主,主要成分是尿素、氨基酸等物质.沉积物DON以分子量<1 kDa和>30 kDa的有机物为主,其中前者主要由芳构化程度较高的氨基酸等小分子有机物构成,后者以腐殖质类为主.水体中部分胺类物质本身具有一定毒性,游离氨基酸等DON还是卤乙腈、卤代酰胺、卤代硝基甲烷、卤化氰和亚硝胺等含氮消毒副产物的重要前体物.由于水体中许多含氮有机物具有生物可利用性,有机氮可能是引起水体富营养化的重要原因之一.  相似文献   

7.
垃圾渗滤液中有机物分子量的分布及在MBR系统中的变化   总被引:33,自引:0,他引:33  
陈少华  刘俊新 《环境化学》2005,24(2):153-157
利用凝胶层析方法分析了垃圾渗滤液中有机物分子量的分布情况,并考察了利用膜生物反应器(MBR)处理垃圾渗滤液系统中有机污染物分子量的分布以及水溶性腐殖质(AHS)含量的变化.研究发现,垃圾渗滤液中的有机物主要由两部分组成,即分子量大于6000的大分子物质和分子量小于1500的小分子物质.大分子物质主要是水溶性腐殖质,而小分子物质主要由挥发性有机酸及水溶性腐殖质组成.大分子的AHS难以被微生物降解,但能被微滤膜截留.大部分小分子的AHS既难以被微生物降解,又不能被膜截留,是构成MBR处理出水COD的主要成分.  相似文献   

8.
提取了活性污泥胞外聚合物(EPS)和溶解性微生物代谢产物(SMP),并按EPS的紧密程度对松散EPS、紧密EPS的分层组分以及SMP属性进行了分析鉴定.结果表明,以葡萄糖为基质时,松散EPS的主要组成是多糖,紧密EPS的主要组成是蛋白质,而SMP主要由腐殖质类物质构成.SMP、松散EPS、紧密EPS和总样EPS的三维荧光图谱显示其只有类色氨酸峰和类腐殖酸峰,其类腐殖酸峰主要是由生物代谢产生的腐殖质组成.大分子量腐殖质类物质在几种组分中均出现,但是具有腐殖质特性的分子量为8500 Da的组分会在SMP中大量生成,而具有腐殖质特性的分子量为400 Da的组分只存在于EPS的紧密层中,这与微生物对这3种物质的生物可利用性有关.  相似文献   

9.
城镇污水处理厂废水中存在大量生物毒性物质,但该废水对动物的生殖能力影响研究还十分缺乏。利用大型溞暴露实验,检测广州市某采用A~2/O工艺的城镇污水处理厂出水的急性毒性和生殖毒性。48 h急性毒性实验表明,所有水样均未表现出急性毒性效应。慢性生殖毒性(14 d)测试结果表明:(1)从进水到缺氧池出水均能显著提高第一胎产溞数量;(2)进水和沉砂池出水显著增加受试期总产溞数量;(3)从厌氧池到出水工艺段受试溞的第一胎产溞时间均推后;(4)好氧池出水的毒性显著降低,但仍然对大型溞具有生殖毒性。研究表明,好氧池(A~2/O)工艺能够显著去除具有大型溞生殖毒性的物质,但污水处理厂废水的生殖毒性仍需要引起关注。  相似文献   

10.
以某印染废水二级生化出水为研究对象,考察了生化出水中有机污染物中各组分含量、分子量分布特点等特性,以及各类有机物在硫酸镁混凝处理过程中的去除行为.实验结果表明,该印染废水的生化出水溶解性有机物的主要成分是疏水性物质,以溶解性有机碳(DOC)表征时占总DOC的78%,其中非酸疏水物质约占46%,而以UV254表征时约占总55%,以美国染料生产协会色度值(ADMI7.6)表征时为97%,其中以非酸疏水物质的贡献最大,达到66%,并且非酸疏水物质中不饱和双键或芳香环有机物的含量较高.生化出水中的DOC主要集中在小于1000 D的有机物上,占37%.在硫酸镁的最佳混凝条件下,可以有效地去除由大分子量的非酸疏水物质引起的色度,而对小分子量的有机物也有一定的去除效果.  相似文献   

11.
• N-Cl-DCAM, an emerging N-DBP in drinking water was investigated. • A new BAC has a better removal efficiency for N-Cl-DCAM precursors than an old BAC. • N-Cl-DCAM precursors are more of low molecular weight and non-polar. • Adsorption of GAC plays a major role in removal of N-Cl-DCAM precursors by an O3-BAC. N-chloro-2,2-dichloroacetamide (N-Cl-DCAM) is an emerging nitrogenous disinfection by-product (N-DBP) which can occur in drinking water. In this study, an analytical method based on liquid chromatography with tandem mass spectrometry (LC-MS/MS) was developed to validate the concentration of N-Cl-DCAM, which was found to be 1.5 mg/L in the effluent of a waterworks receiving raw water from Taihu Lake, China. The changes of N-Cl-DCAM formation potential (N-Cl-DCAMFP) in the drinking water treatment process and the removal efficiency of its precursors in each unit were evaluated. Non-polar organics accounted for the majority of N-Cl-DCAM precursors, accounting for 70% of the N-Cl-DCAM FP. The effect of conventional water treatment processes on the removal of N-Cl-DCAM precursors was found to be unsatisfactory due to their poor performance in the removal of low molecular weight (MW) or non-polar organics. In the ozonation integrated with biological activated carbon (O3-BAC) process, the ozonation had little influence on the decrease of N-Cl-DCAM FP. The removal efficiency of precursors by a new BAC filter, in which the granular activated carbon (GAC) had only been used for four months was higher than that achieved by an old BAC filter in which the GAC had been used for two years. The different removal efficiencies of precursors were mainly due to the different adsorption capacities of GAC for individual precursors. Low MW or non-polar organics were predominantly removed by GAC, rather than biodegradation by microorganisms attached to GAC particles.  相似文献   

12.
• Pore structure affects biologically activated carbon performance. • Pore structure determines organic matter (OM) removal mechanism. • Microbial community structure is related to pore structure and OM removal. Optimizing the characteristics of granular activated carbon (GAC) can improve the performance of biologically activated carbon (BAC) filters, and iodine value has always been the principal index for GAC selection. However, in this study, among three types of GAC treating the same humic acid-contaminated water, one had an iodine value 35% lower than the other two, but the dissolved organic carbon removal efficiency of its BAC was less than 5% away from the others. Iodine value was found to influence the removal of different organic fractions instead of the total removal efficiency. Based on the removal and biological characteristics, two possible mechanisms of organic matter removal during steady-state were suggested. For GAC with poor micropore volume and iodine value, high molecular weight substances (3500–9000 Da) were removed mainly through degradation by microorganisms, and the biodegraded organics (soluble microbial by-products,<3500 Da) were released because of the low adsorption capacity of activated carbon. For GAC with higher micropore volume and iodine value, organics with low molecular weight (<3500 Da) were more easily removed, first being adsorbed by micropores and then biodegraded by the biofilm. The biomass was determined by the pore volume with pore diameters greater than 100 μm, but did not correspond to the removal efficiency. Nevertheless, the microbial community structure was coordinate with both the pore structure and the organic removal characteristics. The findings provide a theoretical basis for selecting GAC for the BAC process based on its pore structure.  相似文献   

13.
Dissolved organic matter (DOM) transformation in sequence batch reactor (SBR) fed with carbon sources of different biodegradability was investigated. During the biologic degradation process, the low molecular weight (MW) fraction (< 1 kDa) gradually decreased, while the refractory compounds with higher aromaticity were aggregated. Size exclusion chromatography (SEC) and fluorescence of excitation emission matrices (EEM) demonstrated that more biopolymers (polysaccharides or proteins) and humic-like substances were presented in the extracellular polymeric substance (EPS) extracted from the SBR fed with sodium acetate or glucose, while the EPS from SBR fed with slowly biodegradable dissolved organic carbon (DOC) substratestarch had relatively less biopolymers. Comparing the EfOM in sewage effluent of three SBRs, the effluent from SBR fed with starch is more aromatic. Organic carbon with MW>1 kDa as well as the hydrophobic fraction in DOM gradually increased with the carbon sources changing from sodium acetate to glucose and starch. The DOC fractionation and the EEM all demonstrated that EfOM from the effluent of the SBR fed with starch contained more fulvic acid-like substances comparing with the SBR fed with sodium acetate and glucose.  相似文献   

14.
It is well known that soluble microbial products (SMP) derived from biological systems found in wastewater treatment plant effluent are responsible for chemical oxygen demand (COD). Aerobic granular sludge (AGS) is recognized as an efficient and innovative approach for wastewater treatment. Acetate and propionate as two dominant organic substances in wastewater need to be effectively removed before discharge. The aim of this study was to investigate the effectiveness of acetate and propionate to interfere with the accumulation, molecular weight (MW) distribution and composition of SMP in aerobic granular sludge (AGS) system using two identical sequencing batch reactors (SBR) named R1 and R2, respectively, thus reducing the COD. The results demonstrated that more SMP accumulated in R1 in presence of acetate compared to R2 treated with propionate. A positive correlation for SMP formation was detected as evidenced by aeration rates, but a negative correlation with hydraulic retention time (HRT). The MW distribution analysis suggested that small molecules (MW <3?kDa) were the dominant fraction of SMP in R1 and R2, accounting for 57–79% and 39–61%, respectively. In addition, gas chromatography-mass spectrometry (GC-MS) demonstrated that esters, alkanes, alkenes and alcohols were the predominant low-MW SMP in R1 and R2. More peaks were present in R2 (61) than R1 (46). Esters were the predominant SMP (39%) in R1, while alkanes were the predominant SMP (31%) in R2. Further, microbial community analysis indicated that more α- and γ-Proteobacteria groups which readily utilize low-MW SMP were found in R2 compared to R1-granules which may have contributed to less SMP accumulated in R2. The abundant genera in the granules were Zoogloea and Azoarcus, in particular, a greater quantity of Azoarcus was detected in R2 than R1-granules, which may be associated with higher degradation of aromatics in SMP.  相似文献   

15.
The formation of cancinogenic nitrosamines, esp. N-nitrosodimethylamine (NDMA) in water and wastewater treatment plants has drawn much attention in recent years. Dissolved organic matter from the transported Luan River water as water source of Tianjin was fractionated with different XAD resins and a series of ultra-filtration membranes with molecular weight (MW) cut-offs of 5k Da, 3k Da, and 1k Da, respectively. The NDMA yields from the raw water and each fraction were measured to investigate their role in NDMAyield. Results indicated that the hydrophilic fraction had a higher NDMA yield than those of hydrophobic fraction and transphilic fraction. The fraction with MW below 1k Da had a higher NDMAyield than that with larger MW. NDMA formation increased as the dissolved organic carbon (DOC) to dissolved organic nitrogen (DON) ratio decreased, which indicated that DON might serve as the real important precursor for NDMA. The correlation between NDMA yield and specific ultraviolet absorbance at 254 nm (SUVA254) suggested that the latter might not represent the specific precursors for NDMA in the water. Besides the water quality, the influences of pH, disinfectant dosage, and disinfection contact time on the formation of NDMA were also examined. These results will help water treatment plants establish measures to control this harmful disinfection by-product.  相似文献   

16.
• MEDCC combined with Fenton process was developed to treat real pesticide wastewater. • Pesticide removal was attributable to desalination in the MEDCC. • High COD removal was attributable to organic distributions in different chambers. The combination of the microbial electrolysis desalination and chemical-production cell (MEDCC) and Fenton process for the pesticide wastewater treatment was investigate in this study. Real wastewater with several toxic pesticides, 1633 mg/L COD, and 200 in chromaticity was used for the investigation. Results showed that desalination in the desalination chamber of MEDCC reached 78%. Organics with low molecular weights in the desalination chamber could be removed from the desalination chamber, resulting in 28% and 23% of the total COD in the acid-production and cathode chambers, respectively. The desalination in the desalination chamber and organic transfer contributed to removal of pesticides (e.g., triadimefon), which could not be removed with other methods, and of the organics with low molecular weights. The COD in the effluent of the MEDCC combined the Fenton process was much lower than that in the perixo-coagulaiton process (<150 vs. 555 mg/L). The combined method consumed much less energy and acid for the pH adjustment than that the Fenton.  相似文献   

17.
部分取代苯类在江水中的生物降解与结构相关性研究   总被引:2,自引:0,他引:2  
测定了27种取代苯类化合物在松花江江水中的生物降解性.采用量子化学MOPAC6.0-AM1法计算了化合物的分子量(MW)、生成热(Hf)、分子总表面积(TSA)及最高占有轨道能(EHOMO),结合辛醇/水分配系数lgp及酸解离常数pKa对其中22种化合物的BOD值进行多元线性回归分析,得到如下模型:BOD=105.73-0.439MW-0.076Hf-6.660lgPn=22,R2=0.821,SE=8.250,F=27.56,P=0.000应用所得模型对其余5个化合物的生物降解性进行了预测.只有一个化合物的相对预测误差大于20%,为20.8%.平均预测误差为12.4%.  相似文献   

18.
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.  相似文献   

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