Development and simulation studies of an unsteady state biofilter model for the treatment of cyclic air emissions of an α‐pinene gas stream

This paper describes the development and simulation of an unsteady state biofilter model used to predict dynamic behaviour of cyclically‐operated biofilters and compares it with experimental results obtained from three, parallel, bench‐scale biofilters treating both periodically fluctuating concentrations and constant concentrations of an α‐pinene‐laden gas stream. The dynamic model, using kinetic parameters estimated from the constant concentration biofilter, was able to predict the performance of cyclic biofilters operating at short cycle periods (ie, in the order of minutes and hours). Steady state kinetic data from a constant concentration biofilter can be used to predict unsteady state biofilter operation. At a 24 h cycle period, the dynamic model compared well with experimental results. For long cycle periods (ie, hours and days), removal efficiency decreased after periods of non‐loading: the longer the period of non‐loading, the poorer the biofilter's performance at the re‐commencement of pollutant loading. At longer time scales the model did not effectively predict transient behaviour, as adsorption and changes in kinetic parameters were not accounted for. Modelling results showed that similar biofiltration performance for the cyclic and constant concentration biofiltration of α‐pinene is expected for biofilters operating solely in the first order kinetics regime. Poorer performance for cyclic biofilters following Monod kinetics spanning the entire kinetics range is expected as the cycle amplitude increases. The most important parameters affecting the performance of a cyclically‐operated biofilter with short cycle periods are: amplitude of cyclic fluctuations, C_{g, max}/C_g, relative value of the half‐saturation constant in the Monod expression, K_s, and effective diffusivity of α‐pinene in the biofilm, D_e. Copyright © 2005 Society of Chemical Industry     

卷烟企业异味对大气环境的影响分析

云南某卷烟厂制丝、卷接包及香料厨房生产过程中产生非常浓烈的异味,异味主要为有机高分子碳氢化合物,还含有少量低分子有机碳氢化合物和微量的氨气.通过公众参与调查和模式预测,判定其影响范围在下风向650 m以内.项目处于某城市建成区,由于项目周围学校、居民区等敏感点众多,因此,为减轻该厂生产过程中排放的异味对周围环境的影响,该厂要么尽快搬迁,要么根据项目异味气体的特征,采取生物滤池或化学洗池等对异味进行治理,并针对有挡雨帽和无挡雨帽排气筒两种情况分别提出了异味的最低去除效率.     

城市污水生物脱氮除磷技术的研究进展

评述了近年来城市污水生物脱氮除磷技术的研究进展,重点介绍了生物处理的新方法:ANAMMOX–SHARON组合法、好氧同步脱氮除磷法和倒置A2/O法,并比较了各种工艺的优缺点。指出反硝化聚磷技术在倒置A2/O工艺中的应用将成为城市污水同步脱氮除磷研究的一个重要发展方向。     

电气石对好氧反硝化菌株反硝化特性的影响

用化学全分析、扫描电镜、Bruauer-Emmett-Teller法和粒度分析仪对内蒙赤峰电气石进行测试表征,研究了电气石对好氧反硝化菌株反硝化特性的影响.结果表明:电气石能够促进好氧反硝化菌株的生长繁殖,纯培养16 h后,细菌数量增加384%.电气石还可以增强好氧反硝化菌株的反硝化能力,与未投加电气石的相比较,NO-3-N,NO-2-N,化学需氧量的浓度降低,总氮去除率提高32.8%.电气石对菌液体系的氧化还原电位具有调控作用,可以使体系的氧化还原电位降低20%,这一作用可能是电气石提高好氧反硝化菌株反硝化能力的重要因素.     

膜生物反应器同步脱氮除磷研究进展

综述了膜生物反应器的同步脱氮除磷工艺,介绍了影响膜生物反应器同步脱氮除磷效率的几个因素,探讨了同步脱氮除磷工艺中同时脱氮除磷的机理,并在此基础上提出了研究方向和应用前景.     

Denitrification and Dephosphatation by Anaerobic/Anoxic Sequencing Batch Reactor

Removal of denitrifying phosphorus was verified in a laboratory anaerobic/anoxic sequencing batch reactor (A/A SBR). The results obtained demonstrated that the anaerobic/anoxic strategy can enrich the growth of denitrifying phosphorus removing bacteria (DPB) and take up phosphate under anoxic condition by using nitrate as the electron acceptor. The phosphorus removal efficiency was higher than 90% and the effluent phosphate concentration was lower than lmg·L-1 after the A/A SBR was operated in a steady-state. When the chemical oxygen demand(COD) of influent was lower than 180mg·L-1, the more COD in the influent was, the higher efficiency of phosphorus removal could be attained under anoxic condition. However, simultaneous presence of carbon and nitrate would be detrimental to denitrifying phosphorus removal. Result of influence of sludge retention time (SRT) on denitrifying phosphorus removal suggested that the decrease of SRT caused a washout of DPB and consequently the enhanced biological phosphorus     

生物滤料滤池处理姚江微污染水源水

通过中试试验,考察了不同滤料介质的生物滤池对于姚江微污染水源水的处理效果。结果表明,双层生物滤料滤池能够有效地去除有机物、氨氮等污染物质,可以延长滤池反冲洗周期,并能在短时间内恢复到正常处理能力,适合于传统滤池的改造。采用颗粒活性炭-石英砂滤料滤池的综合处理效果优于同类型的颗粒活性炭-沸石滤料滤池,通过加入少量臭氧(0.8～1.0mg/L)可以提高生物滤池的去除效果。     

A2O工艺缺氧生物磷去除

A lab-scale anaerobic-anoxic-oxic （A^2O） process used to treat a synthetic brewage wastewater was investigated. The objectives of the study were to identify the existence of denitrifying phosphorus removing bacteria （DPB）, evaluate the contribution of DPB to biological nutrient removal and enhance the denitrifying phosphorus removal in A^2O bioreactors. Sludge analysis confirmed that the average anoxic P uptake accounted for approximately 70% the total amount of P uptake, and the ratio of anoxic P uptake rate to aerobic P uptake rate was 69%. In addition, nitrate concentration in the anoxic phase and different organic substrate introduced into the anaerobic phase had significant effect on the anoxic P uptake. Compared with conventional A^2O processes, good removal efficiencies of COD, phosphorus, ammonia and total nitrogen （92.3%, 95.5%, 96% and 79.5%, respectively） could be achieved in the anoxic P uptake system, and aeration energy consumption was saved 25%. By controlling the nitrate recirculation flow in the anoxic zone, anoxic P uptake could be enhanced, which solved the competition for organic substrates among poly-P organisms and denitrifiers successfully under the COD limiting conditions. Therefore, in wastewater treatment plants the control system should be applied according to the practical situation to optimize the operation.     

有氧条件下生物过滤法脱氮研究

采用生物过滤法,以醋酸钠为外加碳源,探讨了有氧条件下反硝化脱氮的可行性。研究表明,通过向配制水中通入由N2 O2组成的合成气体,能方便地控制水体中溶解氧的浓度。在向配制水中通入含有少量O2的合成气后,系统中的溶解氧浓度下降比不通任何气体时下降还快。随着溶解氧含量逐渐提升,系统反硝化脱氮效果并未受到明显影响。当溶解氧达到6.4mg/L时,系统仍然具有反硝化作用,只是硝酸盐浓度下降速度比低溶解氧条件下缓慢,但是脱氮效率仍然可达85%左右。结果显示,采用生物过滤系统以及实验室培养得到的两种微生物,在一定溶解氧条件下,溶解氧对系统反硝化脱氮能力影响有限。     

Denitrifying phosphorous removal in anaerobic/anoxic SBR system with different startup operation mode

To achieve stable and efficient nitrogen and phosphorus removal and to investigate the characteristics of the A/A SBR enriched with denitrifying phosphorus removal bacteria(DPB),the whole course of startup was studied with two reactors operated in different mode.The reactor I was operated under anaerobic/settling/anoxic/settling mode,and the reactor II was operated under anaerobic/anoxic/settling mode.Differences between the two reactors in removal efficiency of COD,nitrogen and phosphorus were examined.The results indicated that efficient performance could be achieved in both reactors with different startup operation mode,while the phosphorus removal efficiency was improved sooner in reactor I than in reactor II,which suggested that reactor I would supply a more favorable condition for DPB proliferation.Meanwhile,it was observed that the amount of organic substrates consumption had a linear correlation to that of phosphorus release in anaerobic phase when DPB was accumulated in the A/A SBR denitrifying phosphorus removal system.