高氮城市生活垃圾渗滤液短程生物脱氮

采用"两级UASB-缺氧-好氧系统"处理高COD与高NH4 -N的城市生活垃圾渗滤液.180天的试验结果表明:UASB1(一级UASB)与UASB2(二级UASB)最大COD去除速率分别为12.5、8.5 kg·m-3·d-1,UASB1的NOx--N的最大去除速率为3.0 kg·m-3·d-1.系统COD去除率为80%～92%,出水COD为800～1500 mg·L-1.原渗滤液的NH 4-N为1100～2000 mg·L-1,A/O工艺的最大NH4 -N去除速率为0.68kg·m-3·d-1;在17～30℃,通过NO-2-N累积率为90%～99%的短程硝化,NH4 -N的去除率在99%左右,出水NH4 -N小于15 mg·L-1.回流处理水和二沉池回流污泥中的NOx--N分别在UASB1和A/O工艺的缺氧段实现完全反硝化,使系统无机氮TIN去除率达80%～92%.同时高效的反硝化为硝化提供了充足的碱度,使A/O工艺pH大于8.5,维持较高的游离氨浓度,结果表明,高游离氨(FA)是导致短程硝化的主要因素.以pH作为控制参数调控A/O工艺的曝气时间,可以有效的抑制亚硝酸盐氧化菌(NOB)的增长,实现种群优化和稳定的短程硝化.     

Degradation and removal methods of antibiotics from aqueous matrices--a review

Over the past few years, antibiotics have been considered emerging pollutants due to their continuous input and persistence in the aquatic ecosystem even at low concentrations. They have been detected worldwide in environmental matrices, indicating their ineffective removal from water and wastewater using conventional treatment methods. To prevent this contamination, several processes to degrade/remove antibiotics have been studied. This review addresses the current state of knowledge concerning the input sources, occurrence and mainly the degradation and removal processes applied to a specific class of micropollutants, the antibiotics. In this paper, different remediation techniques were evaluated and compared, such as conventional techniques (biological processes, filtration, coagulation, flocculation and sedimentation), advanced oxidation processes (AOPs), adsorption, membrane processes and combined methods. In this study, it was found that ozonation, Fenton/photo-Fenton and semiconductor photocatalysis were the most tested methodologies. Combined processes seem to be the best solution for the treatment of effluents containing antibiotics, especially those using renewable energy and by-products materials.     

汽车尾气净化催化剂Ag/SAPO-34选择性催化还原NO

评价了Ag/SAPO-34分子筛催化剂选择性还原NO的活性,并运用漫反射红外光谱原位研究NO在Ag/SAPO-34催化剂上的选择性催化还原机理.结果表明Ag/SAPO-34有良好的低温活性,在氧气浓度为3.6%和温度为573K～673K时NO还原成N2的转化率达70%;催化剂活性随C3H6浓度的增加而升高,随空速的增加而稍有下降.基于漫反射红外光谱,认为反应机理为:NO、丙烯和氧反应,在Ag/SAPO-34催化剂上生成吸附的有机-氮氧化物,再由这些吸附物种分解成N₂,催化还原的关键是形成有机-氮氧化物中间体.氧的作用是充分促进丙烯活化以及增加NO_x吸附态含量,并且氧的存在是有效产生一系列中间物不可缺少的条件.     

改性TiO_2光催化降解三苯甲烷类污染物

以硫酸钛为原料采用水热法制备了掺Fe3＋TiO2晶体粉末,采用X射线衍射仪（XRD）对样品的结构进行了表征。在可见光条件下,用溴酚蓝、甲基绿、甲基蓝、孔雀石绿、甲基紫和碱性品红等6种典型三苯甲烷类化合物为目标降解物,研究了以自制的掺Fe3＋TiO2晶体粉末对它们的催化降解作用。实验结果表明,制备的掺Fe3＋TiO2晶体属于锐钛矿型。6种化合物的光催化降解反应遵循拟一级动力学规律,且可用Langmuir-Hinshelwood（L-H）动力学模型描述,其表观反应速度常数（k）的大小顺序为：溴酚蓝〈甲基绿〈甲基蓝〈孔雀石绿〈甲基紫〈碱性品红,大小变化次序与其半衰期t1/2成反比,并从分子结构上对它们的降解规律进行定性解释。     

C/N比和曝气量影响MBR同步硝化反硝化的研究

通过连续运行MBR研究了C/N比和曝气量对同步硝化反硝化的影响,结果表明,在环境温度13～23℃,MLSS为6.0～6.8 g/L,进水NH⁺₄-N浓度50 mg/L,曝气量0.5 m³/h,HRT为6 h实验条件下,总氮去除率随着进水C/N比的增加而增加,在C/N比为6∶1～8∶1时,TN去除率达到79%～89%,低的C/N比抑制反硝化,过高的C/N比增加了碳源补加的成本。改变反应曝气量,当C/N比为6∶1,曝气量为0.4 m³/h时,TN的去除率达到了最大值85%。曝气量过高或过低,TN去除率均下降。并对在不同曝气量下MBR 内的DO 值分布进行了初步研究。     

Estimation and characterization of PCDD/Fs and dioxin-like PCBs from Chinese iron foundries

The iron foundry industry is considered to be a potential source of polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/Fs). This study investigated the emission factors and total emission amounts of PCDD/Fs and dioxin-like polychlorinated biphenyls (DL-PCBs) from iron foundries in China. The concentrations and the World Health Organization toxicity equivalents (WHO-TEQs) are presented and the congener profiles are discussed in this paper.In the present work, 26 fly ash samples were collected and tested to quantify the PCDD/Fs and DL-PCBs generated by 14 plants of different scales, and five stack gas samples were collected from two (named as EFG and LFG) of those plants. The emission levels of PCDD/Fs and DL-PCBs indicated that hot-air cupolas had lower emissions than cold-air cupolas. When iron ore lump and sinter were used as raw material, the emission factors were about 250 ng TEQ t⁻¹ of product. However, if the raw material was scrap, the emission factors varied owing to the different contents of organic materials in the raw materials. It was found that the mean WHO-TEQ values of PCDD/Fs and DL-PCBs were 144 and 34.2 pg Nm⁻³ in stack gas and 20.0 and 1.58 pg g⁻¹ in fly ash. In multiple tests, it was estimated that the mean emission factors of PCDD/Fs and DL-PCBs were 365 and 10.9 ng WHO-TEQ t⁻¹ released to residue and 2719 and 555 ng TEQ t⁻¹ released to air. The total emission amounts of PCDD/Fs and DL-PCBs from Chinese iron foundries with cupola furnaces released to residue and air were 16.8 and 146 g WHO-TEQ in 2008, respectively.     

可溶性有机质对芘在泥炭和高岭土上吸附和解吸的影响

为掌握可溶性有机质(DOM)对憎水性有机污染物吸附和解吸行为的影响,本研究选取四环多环芳烃——芘作为目标污染物,通过批平衡实验研究了不同分子量组分DOM对芘在泥炭和高岭土上吸附和解吸的影响.结果表明,吸附和解吸数据均可以用Freundlich模型很好地拟合(R2＞0.93).DOM的添加抑制了泥炭对芘的吸附,并且分子量...     

进水C/N对A~2/O-BCO工艺反硝化除磷特性的影响

采用厌氧/缺氧/好氧与生物接触氧化工艺组成的双污泥系统(A~2/O-BCO)处理实际生活污水.通过投加乙酸钠调节进水碳氮比(C/N=2.44~8.85),考察了系统的反硝化除磷特性.试验结果表明:进水有机物主要是通过改变硝化性能(即缺氧段反硝化负荷)以及聚-β-羟基链烷酸脂(PHA)的贮存和利用,进而影响系统的脱氮除磷效果.当进水C/N为4~5时,COD、TN和PO_4~(3-)-P去除率分别达到88%,80%和96%,实现了有机物、氮和磷的同步高效去除.碳平衡分析表明,A~2/O反应器去除的COD占去除总量的71.86%~77.28%,BCO反应器去除的COD仅占2%~12%,碳源的高效利用是A~2/O-BCO工艺在低C/N条件下实现深度脱氮除磷的重要原因.此外,通过进水C/N与曝气量、硝化液回流比、厌/缺氧反应时间等相关性的分析,提出了系统的优化运行策略.     

Pd/g-C3N4对水中2,4-二氯酚的催化加氢脱氯研究

分别采用光沉积法和浸渍法制备了载钯石墨相氮化碳催化剂(Pd/g-C3N4-PD和Pd/g-C3N4-IMP),并对其进行了电感耦合等离子体发射光谱(ICP-AES)、X射线衍射(XRD)、透射电镜(TEM)和Zeta电位的表征.结果表明,不同载钯量Pd/g-C3N4-PD的等电点均在pH 2.3左右;Pd/g-C3N4-PD表面Pd粒子分散均匀,且Pd粒径小于Pd/g-C3N4-IMP.分别将Pd/g-C3N4-PD和Pd/g-C3N4-IMP用于2,4-二氯酚的催化加氢脱氯研究,Pd/g-C3N4-PD的催化脱氯效果明显优于Pd/g-C3N4-IMP.低pH值利于2,4-二氯酚的催化加氢脱氯过程,但不利于保持催化剂的稳定性.     

采用Fe2+/NaClO处理乐果废水的研究

研究了利用NaClO在酸性条件下生成的HClO代替Fenton试剂中的氧化剂H2O2,在Fe^2＋的作用下对乐果模拟废水进行处理。结果表明此方法处理乐果废水的效果比较明显。使用Fe^2＋／NaClO氧化处理乐果模拟废水,在pH值等于2,NaClO与FeSO4·7H2O的投加量分别为10mL/L,2．5g／L,振荡时间为30min,乐果初始质量浓度小于53mg／L时,乐果的处理率大于88．90％。