厌氧氨氧化菌与其他细菌之间的协同竞争关系

随着污水脱氮行业的蓬勃发展,各种新工艺、新理论层出不穷.厌氧氨氧化(Anammox)工艺以其独特的优点脱颖而出,成为最具应用前景的新工艺.厌氧氨氧化菌作为该过程的执行者目前已发现5属17种,本文主要对5属17种的厌氧氨氧化菌进行总结,并对厌氧氨氧化菌种内关系中的群体感应系统进行详细介绍,此外还介绍了厌氧氨氧化菌与硝化菌、反硝化菌以及厌氧甲烷氧化菌之间的协同与竞争关系.最后给出常见竞争因素对厌氧氨氧化种群结构的影响,通过控制竞争因素来实现对厌氧氨氧化种群结构的调节.本文将厌氧氨氧化菌微生物生态学与厌氧氨氧化污水处理工艺相结合,为厌氧氨氧化工艺在污水生物处理中的应用提供理论依据.     

Comparison of biochemical characteristics between PAO and DPAO sludges

A successful enhanced biological phosphorus removal(EBPR) was observed in both anaerobicaerobic sequencing batch reactor(An-Ox SBR) to induce growth of phosphorus accumulating organism(PAO) and anaerobic-anoxic(An-Ax) SBR to induce growth of denitrifying PAO(DPAO).Although the EBPR performance of An-Ox SBR was higher by 11.3% than that of An-Ax SBR,specific phosphorus release rates in the An-Ax SBR(22.8 ± 3.5 mg P/(g VSS·hr)) and the An-Ox SBR(22.4 ± 4.8 mg P/(g VSS·hr)) were similar. Specific phosphorus uptake rates under anoxic and aerobic conditions were 26.3 ± 4.8 mg P/(g VSS·hr)(An-Ax SBR) and 25.6 ± 2.8 mg P/(g VSS·hr)(An-Ox SBR), respectively, which were also similar. In addition, an analysis of relationship of poly-β-hydroxyalkanoates(PHA) synthesized under anaerobic conditions with phosphorous release(Preleased/PHAsynthesized) and of PHA utilized under anoxic and aerobic conditions with phosphorous uptake(Puptaked/PHAutilized) verified that biological activities of EBPR per unit biomass between DPAO and PAO were similar. An analysis of the specific denitrification rate of DPAO showed that NO-3-N can be denitrified at a rate that does not substantially differ from that of an ordinary denitrifier without additional consumption of organic carbon when the PHA stored inside the cell under anaerobic conditions is sufficiently secured.     

Influence of carbon source and temperature on the denitrifying phosphorus removal process

To supply the valuable operating parameters for the popular usage of the new denitrifying phosphors removal process, it is essential to study the dominant biochemical reactions and the characteristics of denitrifying phosphorus removing bacteria (DPB). Thus, parallel batch experiments using DPB sludge were carried out to assess the effect of substrates (sewage, HAc, and endogenous carbon source) on denitrifying dephosphorus removal efficiency in this study. The results showed that the initial specific phosphorus release rate increased with the high concentration of the short-chain volatile fatty acids ratio in the influent, and sufficient phosphorus was released by DPB. This improved the subsequent denitrification and phosphorus uptake efficiency. The specific endogenous denitrification mainly relies on the internal carbon source (PHB) stored by poly-P bacteria. Denitrifying phosphorus removing bacteria were very hungry when the internal PHB was consumed. Consequently, the specific endogenous denitrification rate was low and the phosphorus uptake did not happen. On the other hand, in the experiment, the denitrifying phosphorus removal performance under two temperature conditions (8–10°C and 25–26°C) was also investigated and analyzed. It was found that the lower temperature decreased the specific phosphorus release and uptake rate, but did not inhibit the denitrifying phosphorus removal completely. Therefore, the negative influence of the low temperature on the overall phosphorus removal was not significant. Translated from Acta Scientiae Circumstantiae, 2006, 26 (2): 186–192 [译自: 环境科学学报]     

自动增氧型潜流人工湿地处理农村生活污水的研究

采用人工配水模拟太湖地区农村生活污水水质,利用改进的自动增氧型潜流人工湿地对其进行处理,结果表明:COD、NH4 -N、TP进水浓度分别在132.4～392.6mg·L-1、21.58～50.26mg·L-1、3.60～13.17mg·L-1范围内变化时,COD、NH4 -N、TP的去除负荷随着进水浓度的升高而增大,其最高去除负荷分别为226.38 kg·d-1·hm-2、44.40 kg·d-1·hm-2、10.44 kg·d-1·hm-2,相应的去除率为89.45%、88.93%、90.25%,且系统有较强的抗冲击负荷能力.     

改良型DE氧化沟工艺的除磷脱氮分析

新都污水处理厂所采取的改良型DE氧化沟经工程实践证明效果较好,针对该处理工艺流程和DE氧化沟自身的改进进行了分析,总结了为强化脱氮除磷进行改良的经验。     

污水生物除磷研究进展

水体富营养化是世界性难题,其中磷通常是主要限制因子.生物除磷工艺简单,污泥产量少,可节约能源,运行费用也较低,便于操作和磷的回收.在介绍水体中磷的来源、污染特点及其造成危害的基础上,着重综述了国内外生物除磷的研究进展,并对生物除磷存在的问题和发展趋势提出了一些看法.     

硝酸盐电子受体反硝化同时除磷试验分析

经研究发现AAA SBR系统中的活性污泥可以利用硝酸盐作为电子受体进行缺氧吸磷并同时发生反硝化脱氮。试验利用“双泥”系统进一步探讨了污水生物反硝化同时除磷的可能性,结果表明 :“双泥”系统的“双重”吸磷以及内碳源反硝化除磷方式可以使生物处理出水磷酸盐浓度趋近于零,TP≤ 0 2 3mg L、NH3 N≤ 0 5mg L、TN≤ 8mg L、CODCr≤2 5mg L。     

转炉渣诱导磷酸钙结晶法去除和回收废水中磷的研究

以转炉渣为晶种材料,利用批次结晶沉淀实验,研究不同的反应条件对诱导磷酸钙结晶法去除和回收废水中磷的影响。结果表明,最优反应条件为:pH=9.5,Ca/P摩尔比2∶1,转炉渣用量1.7 g/L,反应时间3 h,在此条件下,碳酸根对反应的影响甚小,对养猪场废水和污泥浓缩池上清液的处理,最高去除率分别达到95.36%和96.54%;转炉渣循环利用10次,回收磷的效果仍然很好。运用扫描电子显微镜(SEM)、X射线能谱仪(EDS)和X射线衍射仪(XRD)等测试手段对在最优工艺条件下重复使用10次的转炉渣进行了表征,证明回收的磷主要以羟基磷灰石(HAP)形态存在。     

水解酸化-A~2O污泥减量工艺的运行性能研究

生物处理单元采用水解酸化、多级串联接触曝气、连续流的除磷脱氮A2/O工艺,并辅以外排厌氧富磷污水侧流除磷,开发了一个新型的具有强化除磷脱氮功能的污泥减量HA-A/A-MCO工艺。用该工艺处理校园生活污水发现,在SRT60 d、进水COD 316~407 mg/L、NH4+-N30~40 mg/L、TN35~53 mg/L、TP 8~12 mg/L的条件下,出水COD≤18 mg/L、NH4+-N≤2.1 mg/L、TN≤10.3 mg/L、TP≤0.44 mg/L。研究还发现,水解酸化池处理产生的VFA能有效促进生物除磷脱氮,导致厌氧释磷量达57 mg/L,进入化学除磷池的侧流液量仅相当于进水量的13%;系统最主要的脱氮形式是SND和缺氧反硝化,SND脱氮占脱氮总量的50%,缺氧反硝化占26%;HA-A/A-MCO系统有效实现了生物相分离,并利用生物捕食作用获得较低的污泥产率,0.1 g MLSS/g COD。     

改良型A2／O-MBR工艺的反硝化除磷性能研究

重点考察了-种改良型膜生物反应器（A2／O—MBR）的脱氮除磷性能。该工艺主要特点在于对膜池硝化回流液进行了固液分离,并将上清液和浓缩污泥分别回流至缺氧池和厌氧池,这种改进提高了系统对氮、磷的同步去除效率。实验结果表明,在水力停留时间（HRT）为12h,污泥龄（SRT）为30d,混合液回流比为200％的运行条件下,进水COD、NH4＋-N、TN和TP平均浓度分别为（225±38）、（24．8±3．9）、（26．7±2．9）和（2．90±0．53）mg／L时,增加膜池硝化回流液固液分离装置前后,系统对COD和NH4＋-N的去除都维持在较高水平,而系统对TN和TP的去除效果显著提高,出水TN和TP平均浓度分别由（14．9±3．3）mg／L和（1．95±0．72）mg／L下降到（9．4±1．9）mg／L和（0．91±0．38）mg／L,表明增加膜池硝化回流液固液分离装置显著改善了A2／O-MBR系统的脱氮除磷效果。反硝化除磷活性实验结果进一步表明,改进后系统中反硝化除磷活性占总除磷活性的比例由51．5％上升至61．7％,说明增加膜池硝化回流液固液分离装置强化了系统的反硝化除磷性能。