The anaerobic ammonia oxidation(Anammox) bioreactor was successfully started up with the nitrifying activated sludge. After anaerobically operated for 105 d, the bioreactor reached a good performance with removal perc...The anaerobic ammonia oxidation(Anammox) bioreactor was successfully started up with the nitrifying activated sludge. After anaerobically operated for 105 d, the bioreactor reached a good performance with removal percentage of both ammonia and nitrite higher than 95% and volumetric total nitrogen removal as high as 149.55 mmol/(L·d). The soft padding made an important contribution to the high efficiency and stability because it held a large amount of biomass in the bioreactor.展开更多
Ammonium and nitrite are two substrates of anammox bacteria, but they are also inhibitors under high concentrations. The performance of two anaerobic ammonium-oxidizing (anammox) upflow biofilm (UBF) reactors was inve...Ammonium and nitrite are two substrates of anammox bacteria, but they are also inhibitors under high concentrations. The performance of two anaerobic ammonium-oxidizing (anammox) upflow biofilm (UBF) reactors was investigated. The results show that anammox UBFs become unstable under nitrogen loading rate (NLR) applied higher than 1.0 g/(L·d). The consumptions of acidity in the anammox reaction lead to the increase of pH, which is as high as 8.70-9.05. Free nitrous acid concentration is accompanied to be lower than the affinity constant of anammox bacteria, and then starvation effect appears. Moreover, free ammonia concentration increases to 57-178 mg/L, resulting in inhibitory effect on the anammox bacteria. Both negative effects contribute to the instability of the anammox bioreactors.展开更多
基于目前短程硝化–厌氧氨氧化(partial nitritation and anammox, PN/A)工艺处理城镇污水中反应器运行不稳定和氮去除负荷低的问题,本文设计一种新型复合生物反应器:序批式–折流板–分置膜生物反应器(sequencingbatch-baffled-separat...基于目前短程硝化–厌氧氨氧化(partial nitritation and anammox, PN/A)工艺处理城镇污水中反应器运行不稳定和氮去除负荷低的问题,本文设计一种新型复合生物反应器:序批式–折流板–分置膜生物反应器(sequencingbatch-baffled-separatemembranebioreactor,SASMBR)。将该反应器应用于PN/A工艺处理城镇污水,探究反应器的性能,并对SASMBR运行PN/A工艺的运行成本进行分析。结果表明,采用SASMBR反应器运行PN/A工艺处理城镇污水,能够实现高效稳定的脱氮效果,TN去除率达到80%~85%,氮素去除负荷(nitrogenremovalrate,NRR)达到0.20~0.22kgN/(m-3·d-1),出水TN浓度维持在8 mg/L以下。16SrRNA基因测序分析发现,短程硝化SASMBR反应器内设置的折流板能够富集氨氧化细菌(ammoniaoxidationbacteria,AOB),确保短程硝化SASMBR反应器的良好性能;厌氧氨氧化SASMBR内固定在折流板两侧的无纺布可以有效地持留厌氧氨氧化菌(ammoniumoxidizingbacteria,AnAOB),同时,厌氧氨氧化SASMBR内丰度升高的AOB可以为AnAOB提供生长的厌氧环境和NO2--N基质,使厌氧氨氧化SASMBR反应器能够快速启动和高效稳定运行。SASMBR的运行成本为0.037元/m3,比传统城镇污水处理厂的运行成本大幅度降低。展开更多
文摘The anaerobic ammonia oxidation(Anammox) bioreactor was successfully started up with the nitrifying activated sludge. After anaerobically operated for 105 d, the bioreactor reached a good performance with removal percentage of both ammonia and nitrite higher than 95% and volumetric total nitrogen removal as high as 149.55 mmol/(L·d). The soft padding made an important contribution to the high efficiency and stability because it held a large amount of biomass in the bioreactor.
基金Project(2006AA06Z332) supported by the National High-Tech Research and Development Program of ChinaProject(30770039) supported by the National Natural Science Foundation of ChinaProject(2008BADC4B05) supported by the National Science and Technology Pillar Program
文摘Ammonium and nitrite are two substrates of anammox bacteria, but they are also inhibitors under high concentrations. The performance of two anaerobic ammonium-oxidizing (anammox) upflow biofilm (UBF) reactors was investigated. The results show that anammox UBFs become unstable under nitrogen loading rate (NLR) applied higher than 1.0 g/(L·d). The consumptions of acidity in the anammox reaction lead to the increase of pH, which is as high as 8.70-9.05. Free nitrous acid concentration is accompanied to be lower than the affinity constant of anammox bacteria, and then starvation effect appears. Moreover, free ammonia concentration increases to 57-178 mg/L, resulting in inhibitory effect on the anammox bacteria. Both negative effects contribute to the instability of the anammox bioreactors.
文摘本文探索了应用循环曝气膜生物反应器富集培养厌氧氨氧化菌,并处理含氮废水的可行性。通过曝气量对膜通量影响的实验,确定最佳曝气量为0.2 m^3/h。通过对曝气量对厌氧氨氧化菌活性的实验,相比无曝气条件,在曝气量为0.2 m^3/h的条件下,厌氧氨氧化活性未受到影响。在长期实验中,该反应器的氮负荷及氮去除率高达1.8 kg TN/m^3·d及80%。相比无曝气条件,保持曝气量为0.2m^3/h时,膜清洗周期从6天延长到36天。
