Combination of ion exchange system and biological reactors for simultaneous removal of ammonia and organics

A novel process for a simultaneous removal of ammonia and organics was developed on the basis of ion exchange and biological reactions. From batch experiments, it was found out that NH₄⁺ could be removed effectively by combining cation exchange and biological nitrification showing 0.98 mg N/m²?s of a maximum flux. On the other hand, the removal of NO₃⁻ was 3.5 times faster than NH₄⁺ and the maximum flux was calculated to be 3.4 mg N/m²?s. The systems for NH₄⁺ and NO₃⁻ removal were combined for establishing the IEBR process. When the process was operated in a continuous mode, approximately 95.8% of NH₄⁺ was removed showing an average flux of 0.22 mg N/m²·s. The removal efficiency of total nitrogen was calculated as 94.5% whereas that of organics was 99.5%. It was concluded that the IEBR process would be effectively used for a simultaneous removal of NH₄⁺ and organics.     

Implications of simultaneity in a physical damage function

A modeler must often rely on highly simplified representations of complex physical systems when analyzing associated economic issues. Herein, we consider a management problem in which a bioeconomic system exhibits simultaneity in processes governing productivity and damage. In this case, it may benefit the producer to sacrifice productivity to reduce the costs associated with increased damage. We specify empirically a structural damage relationship that explains the biological process by which an invasive species damages a host and estimate the structural model and its reduced form with an exceptional dataset on infestation of olives by the olive fruit fly. We contrast the results of these models with the approach typically taken in the economic literature, which expresses damage as a function of pest density. The population-based approach introduces significantly greater bias into the individual grower's choice of damage-control inputs than estimates based on the structural model.     

SBR法处理垃圾渗滤液及其同时硝化反硝化生物脱氮研究

采用SBR系统处理城市垃圾渗滤液,研究了不同C／N、130和MLSS对同时硝化反硝化脱氮效率的影响。结果表明：总氮去除率随着C／N、MLSS升高而上升;DO越低,总氮去除率越高;当进水CODCr与NH3-N浓度分别为420mg／L和112mg／L,DO和MLSS分别为1．5mg／L和5016mg／L时,CODCr、NH3-N及TN去除率分别为81．54％、96．57％和46．66％。根据试验结果,对同时硝化反硝化一个代表周期作了分析。     

射流曝气周期活性污泥法脱氮除磷研究

针对零星居民点的污水处理,开发了射流曝气周期活性污泥法工艺.它是一种连续进水、周期性间歇曝气的改良型SBR工艺,也是一种时间程序和空间程序相结合的污水处理工艺,具有良好的脱氮除磷效果.试验表明,在水力负荷4 m3/d,曝气周期为每2 h曝气15 min、静置105 min的条件下,出水COD为48.8～53.5 mg/L,去除率达79.4%～80.5%;出水TN为2.81～3.98 mg/L,去除率达82.4%～89.4%;出水NH3-N为0.36～0.78 mg/L,去除率高达96.4%～98.4%;出水TP为0.63～1.18 mg/L,去除率为67.2%～78.9%,均可达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级B排放标准.     

供碳源载体及其在低碳氮比污水处理中的应用研究

为解决低C/N污水的脱氮问题,本实验自行研制开发了一种新型碳聚合物载体.对该载体进行低C/N污水的生物膜脱氮研究,考察了HRT、pH、DO、温度等因素对系统同步硝化反硝化脱氮效果的影响.结果表明:在C/N比为4、pH=8、DO=1 mg/L、HRT=6 h,T=24℃的条件下,氨氮及总氮的去除率分别可以达到90%和70...     

Confidence limits on one-stage model parameters in benchmark risk assessment

In modern environmental risk analysis, inferences are often desired on those low dose levels at which a fixed benchmark risk is achieved. In this paper, we study the use of confidence limits on parameters from a simple one-stage model of risk historically popular in benchmark analysis with quantal data. Based on these confidence bounds, we present methods for deriving upper confidence limits on extra risk and lower bounds on the benchmark dose. The methods are seen to extend automatically to the case where simultaneous inferences are desired at multiple doses. Monte Carlo evaluations explore characteristics of the parameter estimates and the confidence limits under this setting.

Bootstrap methods for simultaneous benchmark analysis with quantal response data

A primary objective in quantitative risk assessment is the characterization of risk which is defined to be the likelihood of an adverse effect caused by an environmental toxin or chemcial agent. In modern risk-benchmark analysis, attention centers on the “benchmark dose” at which a fixed benchmark level of risk is achieved, with a lower confidence limits on this dose being of primary interest. In practice, a range of benchmark risks may be under study, so that the individual lower confidence limits on benchmark dose must be corrected for simultaneity in order to maintain a specified overall level of confidence. For the case of quantal data, simultaneous methods have been constructed that appeal to the large sample normality of parameter estimates. The suitability of these methods for use with small sample sizes will be considered. A new bootstrap technique is proposed as an alternative to the large sample methodology. This technique is evaluated via a simulation study and examples from environmental toxicology.

同时硝化反硝化生物脱氮技术研究进展

对同时硝化反硝化（SND）生物脱氮新技术的机理进行了较全面的探讨，对影响SND的控制因素及其研究现状进行了简单的综述，最后指出了实现SND存在的一些急需解决的问题。     

黄河北干流与渭河相遇洪水分析

黄河北干流与渭河位于黄土高原，暴雨是洪水的重要成因．本文分析了近２０００年的历史资料，提出该地区的洪水具有周期性，１９世纪洪水达到高峰，２０世纪洪水规模有所降低，并分析了黄河北干流与渭河及其支流径、洛河洪水相遇问题：四河相遇的概率很小，多形成特大洪水，两河相遇是较常发生的事件，多形成中等以下洪水。三门峡水库的淤积使该地区洪水灾害加剧．同时还分析了该地区洪水对黄河下游洪水的影响。     

Crosslinking acrylamide with EDTA-intercalated layered double hydroxide for enhanced recovery of Cr(VI) and Congo red: Adsorptive and mechanistic study

• Functional groups of AM and EDTA in composite increased removal of Cr(VI) and CR. • Removal process reached equilibrium within 30 min and was minimally affected by pH. • Elimination of Cr(VI) was promoted by coexisting CR. • Adsorption process of CR was less influenced by the presence of Cr(VI). • Mechanisms were electrostatic attraction, surface complexation and anion exchange. We prepared ethylenediaminetetraacetic acid (EDTA)-intercalated MgAl-layered double hydroxide (LDH-EDTA), then grafted acrylamide (AM) to the LDH-EDTA by a cross-linking method to yield a LDH-EDTA-AM composite; we then evaluated its adsorptive ability for Congo red (CR) and hexavalent chromium (Cr(VI)) in single and binary adsorption systems. The adsorption process on LDH-EDTA-AM for CR and Cr(VI) achieved equilibrium quickly, and the removal efficiencies were minimally affected by initial pH. The maximum uptake quantities of CR and Cr(VI) on LDH-EDTA-AM were 632.9 and 48.47 mg/g, respectively. In mixed systems, chromate removal was stimulated by the presence of CR, while the adsorption efficiency of CR was almost not influenced by coexisting Cr(VI). The mechanisms involved electrostatic attraction, surface complexation, and anion exchange for the adsorption of both hazardous pollutants. In the Cr(VI) adsorption process, reduction also took place. The removal efficiencies in real contaminated water were all higher than those in the laboratory solutions.