污水厂二级出水溶解性有机物臭氧化特性研究

采用液相色谱荧光检测器将三维荧光图谱与凝胶色谱分子量分布相结合,对污水处理厂二级出水溶解性有机物(EfOM)的臭氧化反应特性进行了研究.结果表明臭氧会使得二级出水溶解性有机物三维荧光强度明显降低.HPLC-SEC的结果表明臭氧不会改变腐殖质类物质的分子量分布,但臭氧会与小分子蛋白类物质发生反应.根据制备液相的分析结果,小分子蛋白类物质中含有大量苯环及其他共轭结果物质,因此臭氧会优先与小分子蛋白类物质发生反应.同时,XPS分析结果表明臭氧在低投加量下就会与苯环结构反应,提高脂肪类饱和有机物含量,随着投加量进一步升高,含氧官能团(羰基,羧基)数量有所升高.     

臭氧氧化深度处理二级处理出水的研究

以某城市污水处理厂二级处理出水为原水,研究了臭氧氧化深度处理对水中残留有机物以及病原微生物的降解和去除效果.结果表明,臭氧投加量达到6mg/L时,DOC、UV254、色度的去除率分别为15.49%、36.36%、73.61%,环境激素类痕量有机物邻苯二甲酸二丁酯(DBP)和邻苯二甲酸二(2-乙基己基)酯(DEHP)的去除率分别为37.29%和14.6%,三维荧光光谱荧光峰的各区域有机物质平均去除率在80%以上,DBP出水浓度为2.64mg/L,DEHP出水浓度为1.4mg/L,满足《城市污水再生利用地下水回灌水质》(GB/T 19772-2005)的标准.臭氧投加量达到10mg/L时,出水中指示性微生物粪大肠菌群仍接近103CFU/L,5mg/L有效氯消毒后出水粪大肠菌群仍接近10CFU/L,6mg/L臭氧与5mg/L有效氯组合消毒出水的粪大肠菌群下降至3CFU/L,满足《城市污水再生利用景观环境用水水质》(GB/T 18921-2002)的标准.三卤甲烷(THMs)的生成量随着有效氯投加量的增加而增加,臭氧与氯组合消毒过程与氯单独消毒过程相比,THMs生成量减少了78.08%.     

炼油厂达标废水中溶解性有机物的表征

采用超滤和凝胶色谱法调查了炼油厂达标废水中溶解性有机物 (DOM)的分子量分布 ,并用树脂吸附和离子交换技术研究了该废水DOM中疏水性酸 (HoA)、碱 (HoB)及中性物 (HoN)和亲水性酸 (HiA)、碱 (HiB)及中性物 (HiN)的比例 ,用气相色谱 质谱法 (GC MS)定性分析了疏水性有机物的组成 .结果表明 ,某炼油厂达标废水的TOC为 12 0 6～ 16 80mg·L-1,其中溶解性有机碳 (DOC)为 10 15～ 14 4 4mg·L-1;分子量 <1k的DOM约为 80 % (以TOC计 ) ;DOM中HiN、HoN、HoA、HiB、HoB及HiA的含量分别为 2 9 7% ,2 6 5 % ,2 1 1% ,13 4 % ,5 1%及 4 2 % .鉴定出的HoN包括脂肪烃、苯系物、含硫化合物及邻苯二甲酸酯类化合物等 ,其中C10和C11脂肪烃、甲基亚硫酰苯及邻苯二甲酸二丁脂化合物的含量相对较高 .根据表征结果提出了回用处理建议.     

电化学处理黄姜生化尾水研究

黄姜提取皂素过程中会产生大量废水,传统的生化方法难以去除这些废水中的难降解有机污染物.因此,本文以黄姜皂素生化尾水为研究对象,分别采用DSA+铁电极组合、不锈钢+铁电极组合、单独钛钌网电极(DSA)对其进行深度处理.结果表明,在原水CODCr为150mg.L-1,色度为200度,Cl-浓度为3338mg.L-1的情况下,不锈钢+铁电极组合、单独DSA电极处理后CODCr去除率分别为35%和43%,色度去除率分别为78.7%和84.6%.相较而言,DSA+铁电极组合在电流密度为95A.m-2、初始pH=7.28时处理30min后,CODCr和色度的去除率分别达到62%和99.5%.采用紫外光谱、三维荧光光谱和凝胶色谱对水质变化进行了详细分析.结果表明,水中难降解有机组分被降解矿化,生成分子量较小的脂肪酸.     

Integrated biological–physical process for biogas purification effluent treatment

Biogas purification via water scrubbing produces effluent containing dissolved CH₄, H₂S, and CO₂, which should be removed to reduce greenhouse gas emissions and increase its potential for water regeneration. In this study, a reactor built with air supplies at the top and bottom was utilized for the treatment of biogas purification effluent through biological oxidation and physical stripping processes. Up to 98% of CH₄ was removed through biological treatment at a hydraulic retention time of 2 hr and an upper airflow rate of 2.02?L/day. Additionally, a minimum CH₄ concentration of 0.04% with no trace of H₂S gas was detected in the off gas. Meanwhile, a white precipitate was captured on the carrier showing the formation of sulfur. According to the developed mathematical model, an upper airflow rate of greater than 2.02?L/day showed a small deterioration in CH₄ removal performance after reaching the maximum value, whereas a 50?L/day bottom airflow rate was required to strip the CO₂ efficiently and raise the effluent pH from 5.64 to 7.3. Microbiological analysis confirmed the presence of type 1 methanotroph communities dominated by Methylobacter and Methylocaldum. However, bacterial communities promoting sulfide oxidation were dominated by Hyphomicrobium.     

Molecular characterization of effluent organic matter in secondary effluent and reclaimed water: Comparison to natural organic matter in source water

Municipal wastewater reclamation is becoming of increasing importance in the world to solve the problem of water scarcity. A better understanding of the molecular composition of effluent organic matter(Ef OM) in the treated effluents of municipal wastewater treatment plants(WWTPs) is crucial for ensuring the safety of water reuse. In this study, the molecular composition of Ef OM in the secondary effluent of a WWTP in Beijing and the reclaimed water further treated with a coagulation–sedimentation–ozonation process were characterized using a non-target Fourier transform ion cyclotron resonance mass spectrometry(FT-ICR MS) method and compared to that of natural organic matter(NOM) in the local source water from a reservoir. It was found that the molecular composition of Ef OM in the secondary effluent and reclaimed water was dominated by CHOS formulas, while NOM in the source water was dominated by CHO formulas. The CHO formulas of the three samples had similar origins. Anthropogenic surfactants were responsible for the CHOS formulas in Ef OM of the secondary effluent and were not well removed by the coagulation-sedimentation-ozonation treatment process adopted.     

Trihalomethane formation potential of organic fractions in secondary effluent

Organic matter is known to be the precursor of numerous chlorination by-products. Organic matter in the secondary e uent from the Wenchang Wastewater Treatment Plant (Harbin, China) was physically separated into the following fractions: particulate organic carbon (1.2–0.45 m), colloidal organic carbon (0.45–0.1 m), fine colloidal organic carbon (0.1–0.025 m), and dissolved organic carbon (DOC) (< 0.025 m). Moreover, < 0.45 m fraction was chemically separated into hydrophobic acid (HPO-A), hydrophobic neutral (HPO-N), transphilic acid (TPI-A), transphilic neutral (TPI-N), and hydrophilic fraction (HPI). The chlorine reactivity of these organic fractions obtained from both size and XAD fractionations were evaluated. The structural and chemical compositions of the HPO-A, HPO-N, TPI-A, and TPI-N isolates were characterized using elemental analysis (C, H, O, and N), Fourier transform infrared spectroscopy (FT-IR), and proton nuclear magnetic resonance spectroscopy (1H-NMR). Results showed that DOC was dominant in terms of total concentration and trihalomethane formation potential (THMFP), and there was no statistical di erence in both specific THMFP (STHMFP) and specific ultraviolet light absorbance among the 0.45, 0.1, and 0.025 m filtrates. HPO-A had the highest STHMFP compared to other chemical fractions. HPO-A, HPO-N, TPI-A, and TPI-N contained 3.02%–3.52% of nitrogen. The molar ratio of H/C increased in the order of HPO-A < HPO-N < TPI-A < TPI-N. The O/C ratio was relatively high for TPI-N as compared to those for the other fractions. 1H-NMR analysis of the four fractions indicated that the relative content of aromatic protons in HPO-A was significantly higher than those in the others. The ratio of aliphatic to aromatic protons increased in the order of HPO-A < HPO-N < TPI-A < TPI-N. FT-IR analysis of the four fractions showed that HPO-A had greater aromatic C==C content whereas HPO-N, TPI-A, and TPI-N had greater aliphatic C–H content. TPI-N contained more oxygen-containing functional groups than the other fractions.     

A prototype of proposed treatment plant for sago factory effluent

Sago processing industries discharge wastewater, which poses a threat to water bodies due to their higher organic loading. Concerns about pollution related problems in the global scenario are persuading all the processing industries to adopt cleaner manufacturing practices. Hence, this study was aimed at developing a cost-effective and eco-friendly treatment plant based on microbial system to treat the sago factory effluent effectively in order to reuse the water for industrial purposes. The experimental results showed that, anaerobic treatment with mixed inoculum for 10 days followed by 6 days of fungal treatment was found to be effective in effluent treatment. The fusant showed a higher efficiency in the treatment of sago factory effluent than the parental strains.     

城市污水地下回灌深度处理技术

以城市污水地下回灌为回用目的,研究了不同的污水深度处理工艺,并着重研究了去除二级生物处理出水中有机物的处理工艺.研究结果表明,采用臭氧氧化和粉末活性炭预处理后再经土壤渗滤回灌,可大大改善水质,水中溶解性有机碳浓度可降至3mg／L以下,通过静态吸附实验选出了适于处理二级出水的粒状活性炭,并运用ADSA软件对有机物在活性炭上的吸附行为进行分析.将活性炭的动态实验同混凝、过滤结合起来,研究不同组合工艺对有机物的去除效果,筛选出了适于城市污水处理厂二级出水地下回灌的预处理工艺,其出水溶解性有机碳浓度低达3～4．5mg／L以下.     

海上石油生产水的水生生态毒性

采用水生生态毒理学常用的大型蚤(Daphnia magma)和斑马鱼(Brachydaniorerio)以及毒性单位(Tua)法对渤海海上油田的石油生产水进行生态毒性评价和分级.结果表明,这些石油生产水对大型蚤和斑马鱼均表现出一定的毒性效应.其中,水样1和水样3的毒性较大,对大型蚤的Tua分别为151.52和70.96.而对斑马鱼的Tua分别为2.41和2.12.水样3虽经处理,但其生态毒性并未得到明显的改善.水样2对大型蚤和斑马鱼都属于低毒等级,其Tua依次分别为4.39和1.97.可见,大型蚤和斑马鱼可以作为海上石油生产永生态毒性的监测指标,但在生态风险评价中大型蚤比斑马鱼更为灵敏.     

预臭氧化对二级出水微滤过程中膜有机物污染的影响

在二级出水溶解性有机物（secondary effluent organic matter,EfOM）的微滤过程中,多种因素均与膜的有机污染相关,比如总有机物的含量,溶解性有机物的亲疏水性组成等.本文主要研究了在二级出水微滤过程中溶解性有机物的膜污染,以及预臭氧化对二级出水溶解性有机物性质的影响进而对膜有机污染的影响....     

Nitrogen mass balance in a constructed wetland treating piggery wastewater effluent

The nitrogen changes and the nitrogen mass balance in a free water surface flow constructed wetland （CW） using the four-year monitoring data from 2008 to 2012 were estimated. The CW was composed of six cells in series that include the first settling basin （Cell 1）, aeration pond （Cell 2）, deep marsh （Cell 3）, shallow marsh （Cell 4）, deep marsh （Cell 5） and final settling basin （Cell 6）. Analysis revealed that the NH4＋-N concentration decreased because of ammonification which was then followed by nitrification. The NO4＋-N and NO4＋-N were also further reduced by means of microbial activities and plant uptake during photosynthesis. The average nitrogen concentration at the influent was 37,819 kg/year and approximately 45% of that amount exited the CW in the effluent. The denitrification amounted to 34% of the net nitrogen input, whereas the accretion of sediment was only 7%. The biomass uptake of plants was able to retain only 1% of total nitrogen load. In order to improve the nutrient removal by plant uptake, plant coverage in four cells （i.e., Cells 1, 3, 4 and 5） could be increased.     

活性炭吸附石化二级出水有机物去除特性研究

采用活性炭对某石化二级出水进行吸附研究,考察了静态和动态试验下,活性炭对石化废水二级出水COD的去除效果,并讨论了吸附前后水中有机物的组分和相对分子质量的变化.结果表明:静态试验中,活性炭对石化废水二级出水的COD的饱和吸附量为1.1 mg·g-1,吸附速率为0.7 mg·min-1;通过动态试验得到了吸附的最佳条件,即HRT=1 h,水力负荷为0.76 m3·m-2·h-1,此时COD的去除率可达49.9%,出水COD低于50 mg·L-1.相对分子质量分级和树脂分级分析结果表明,活性炭对石化废水二级出水中相对分子质量小于5000的小分子有机物有较好的吸附效果,该组分被活性炭吸附的COD所占比例为59.72%,活性炭吸附作用对水中不同相对分子质量有机物分布影响不大;活性炭对石化废水中有机物组分的去除效果排序依次为:疏水碱性物质(HOB)疏水酸性物质(HOA)亲水中性物质(HIS)疏水中性物质(HON),对HOB和HOA的去除率可达到79%和61%,对HIS和HON的去除效果不佳.     

厌氧—好氧处理高得率浆APMP废水的研究

设计了生物处理高得率浆碱性过氧化氢机械浆 (APMP)废水厌氧 (UASB)—好氧 (SBR)组合技术 ,结果表明该技术可使 APMP废水 COD去除率达 90 .3 %。并用计算机处理实验结果 ,建立了厌氧—好氧关联方程及 SBR降解 APMP废水的动力学关系式。     

污水厂二级出水中THMs前体物卤代活性荧光光谱分析

通过分析城市污水处理厂二级出水中溶解性有机物(DOM)及其XAD树脂分级组分的荧光光谱,研究了DOM的结构特性以及DOM中的THMs前体物在加氯消毒过程中的反应特性与荧光强度之间的相关性.三维荧光光谱显示DOM分级组分中均存在富里酸类、腐殖酸类、芳香性蛋白质类及微生物沥出物类荧光特征峰, 且以芳香性蛋白质类和富里酸类荧光物质为主.荧光光谱区域积分法(FRI)定量分析结果表明,4类荧光物质在DOM各分级组分中的累计荧光强度(ΦT,n)分布与其在二级出水中的分布趋势较相似,总体上呈现疏水性有机酸(HPO–A) >过渡亲水性有机酸 (TPI-A)>过渡性亲水性中性物质(TPI-N)>疏水性有机中性物质(HPO-N)>亲水性物质(HPI).此外,ΦT,n与单位浓度DOC在紫外254nm处的吸光度值(SUVA)及三氯甲烷生成活性(STHMFP)有较好的相关性,但与DOC相关性较差.同步荧光光谱结果表明,在单位DOC条件下,总DOM中稠环类芳香性物质的含量高于DOM各分级组分,而DOM各分级组分中稠环类芳香性物质的含量少于腐殖酸类物质的含量.     

Nitrogen removal from sludge dewatering effluent through anaerobic ammonia oxidation process

Anaerobic ammonia oxidation（Anammox） process is a novel and promising wastewater nitrogen removal process. The feasibility of transition of Anammox from denitrification and the performance of lab-scale Anammox biofilm reactor were investigated with sludge dewatering effluent. The results showed that Anammox process could be successfully started up after cultivation of denitrification biofilm and using it as inoculum. The transition of Anammox from denitrification was accomplished within 85 d. Anammox process was found suitable to remove ammonia from sludge dewatering effluent. The effluent ammonia concentration was detected to be 23.11 mgN/L at HRT of 28 h when influent ammonia concentration was fed 245 mgN/L, which was less than that for the national discharge standard Ⅱ （25 rngN/L） of China. Volumetric total nitrogen loading rate was up to 584.99 mg TN/（L. d） at HRT of 17 h, while influent concentrations were kept 243.25 mg NH4＊ -N/L and 288.31 mg NO2^- -N/L.     

Purification of AS-CMP effluent by combined photosynthetic bacteria and coagulation treatment

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污水生化出水有机物对氯贝酸臭氧降解的影响研究

常规水处理技术无法有效去除痕量的药品和个人护理品(PPCPs),臭氧工艺因具有效果可观、二次污染小等优势,尤其适合用于生化尾水的深度处理.而污水生化出水有机物(EfOM)对臭氧降解PPCPs起着至关重要的作用.本文选取腐殖酸(HA)、牛血清蛋白(BSA)、海藻酸钠(AGS)和葡聚糖(Dextran)作为模拟EfOM 4种代表物质,以氯贝酸(CA)为PPCPs模板化合物,考察了模拟EfOM化合物浓度、反应时间及溶液初始pH对臭氧降解效果的影响规律和机制.结果表明,CA臭氧降解速率符合假一级动力学方程,模拟EfOM化合物为10 mg·L~(-1) TOC时,对CA臭氧降解效果呈现出HADextran≈DW(超纯水)≈AGSBSA的规律.HA可提高HO·的生成速率从而加快CA降解效率,反应速率常数提升了3倍,去除率提高了17.5%;而BSA则明显抑制HO·的生成,从而降低CA降解速率.HA的存在对CA臭氧降解影响较为复杂,研究发现当HA浓度为1 mg·L~(-1) TOC时,能促进HO·的生成和CA的降解,而当浓度升高时会表现出抑制作用.CA臭氧降解速率和反应过程中HO·生成均随着溶液初始pH的增加而增大.pH的变化还会影响HA对臭氧降解CA的作用效果.溶液初始pH为4时,HA投加可促进HO·生成和臭氧降解;但随着pH的升高,HA的存在形态会发生改变,从而表现出对CA臭氧降解效果的抑制作用.     

Chloramination of wastewater effluent: Toxicity and formation of disinfection byproducts

The reclamation and disinfection of waters impacted by human activities (e.g., wastewater effluent discharges) are of growing interest for various applications but has been associated with the formation of toxic nitrogenous disinfection byproducts (N-DBPs). Monochloramine used as an alternative disinfectant to chlorine can be an additional source of nitrogen in the formation of N-DBPs. Individual toxicity assays have been performed on many DBPs, but few studies have been conducted with complex mixtures such as wastewater effluents. In this work, we compared the cytotoxicity and genotoxicity of wastewater effluent organic matter (EfOM) before and after chloramination. The toxicity of chloraminated EfOM was significantly higher than the toxicity of raw EfOM, and the more hydrophobic fraction (HPO) isolated on XAD-8 resin was more toxic than the fraction isolated on XAD-4 resin. More DBPs were also isolated on the XAD-8 resin. N-DBPs (i.e., haloacetonitriles or haloacetamides) were responsible for the majority of the cytotoxicity estimated from DBP concentrations measured in the XAD-8 and XAD-4 fractions (99.4% and 78.5%, respectively). Measured DBPs accounted for minor proportions of total brominated and chlorinated products, which means that many unknown halogenated compounds were formed and can be responsible for a significant part of the toxicity. Other non-halogenated byproducts (e.g., nitrosamines) may contribute to the toxicity of chloraminated effluents as well.     

Performance of hybrid constructed wetland systems for treating septic tank effluent

The integrated wetland systems were constructed by combining horizontal-flow and vertical-flow bed, and their purification efficiencies for septic tank effluent were detected when the hydraulic retention time （HRT） was 1 d, 3 d, 5 d under different seasons. The results showed that the removal efficiencies of the organics, phosphorus were steady in the hybrid systems, but the removal efficiency of total nitrogen was not steady due to high total nitrogen concentration in the septic tank effluent. The average removal rates of COD （chemical oxygen demand） were 89%, 87%, 83%, and 86% in summer, autumn, winter and spring, respectively, and it was up to 88%, 85%, 73%, and 74% for BOD5 （5 d biochemical oxygen demand） removal rate in four seasons. The average removal rates of TP （total phosphorous） could reach up to 97%, 98%, 95%, 98% in four seasons, but the removal rate of TN （total nitrogen） was very low. The results of this study also indicated that the capability of purification was the worst in winter. Cultivating with plants could improve the treated effluent quality fTom the hybrid systems. The results of the operation of the horizontal-flow and vertical-flow cells （hybrid systems） showed that the removal efficiencies of the organics, TP and TN in horizontal-flow and vertical-flow cells were improved significantly with the extension of HRT under the same season. The removal rate of 3 d HRT was obviously higher than that of 1 d HRT, and the removal rate of 5 d HRT was better than that of 3 d HRT, but the removal efficiency was not very obvious with the increment of HRT. Therefore, 3 d HRT might be recommended in the actual operation of the hybrid systems for economic and technical reasons.