不同城市功能区土壤中酞酸酯污染特征

对天津市和辽宁省鞍山市不同城市功能区以及不同工业类型所在地共计12个土壤样品进行采样调查,采用气相色谱-质谱联用仪(GC-MS)对样品中15种酞酸酯类化合物进行分析测定,研究了两市土壤样品中酞酸酯的污染水平,分析了不同城市功能区以及石化、化工、钢铁等工业行业所在地土壤中酞酸酯的浓度差异,研究了不同酞酸酯类化合物的单体污染特征,将两市土壤样品中DBP和DEHP的浓度与国内外部分城市进行了比较,分析了产生上述结果的原因。结果表明,天津市各采样点总酞酸酯(ΣPAEs)浓度在0.524～2.058 mg/kg之间,鞍山市各采样点ΣPAEs浓度在0.779~2.016 mg/kg之间;两城市不同城市功能区土壤ΣPAEs浓度均呈现风景区<生活区<工业区的趋势;15种酞酸酯中,DBP和DEHP在天津市和鞍山市各采样点土壤样品中均有检出,为两城市土壤中酞酸酯主要污染物,其浓度值与国内其它城市处于同一污染水平,略高于我国贵州地区。     

BAF去除氨氮关键影响因素研究

为探讨曝气生物滤池去除氨氮的关键因素,选取沈阳仙女河污水处理厂(40万t/d)现场进行实地研究。通过测定不同条件下(pH、进水COD浓度、溶解氧、温度、水力负荷)的氨氮去除率,并进行主成分分析结果显示,影响BAF工艺脱氮的关键因素是温度、溶解氧和水力负荷。当温度在14~30℃之间时,氨氮的去除率一直维持较高,当温度低于14℃时,氨氮的去除率较低;随着溶解氧浓度的增大,氨氮的去除率也随之升高,当溶解氧增加到5.6 mg/L时,氨氮的去除率达到80%~90%,接近饱和状态;在水力负荷为3.08~4.15 m3/(m.2h)之间时,氨氮的去除率上升,超过该值,则氨氮去除率下降。     

重金属离子与依诺沙星相互作用的荧光光谱法研究

荧光分析法是利用物质的荧光性质对物质进行分析的方法,文章应用荧光法研究了不同温度下重金属离子Cu2+、Pb2+及Mn2+与喹诺酮类药物依诺沙星(ENX)的相互作用。结果表明:Cu2+、Pb2+及Mn2+对ENX内源荧光的猝灭机制属于形成复合物所引起的静态猝灭,利用Stern-Volmer关系式计算了ENX与重金属离子Cu2+、Pb2+及Mn2+之间的猝灭常数KSV及结合位点数,根据热力学参数(自由能变ΔG、焓变ΔH、熵变ΔS)确定了ENX与重金属离子之间的主要作用力类型为静电作用力。该研究为探讨环境中重金属离子与ENX的作用机理和环境效应提供了理论依据。     

重金属铜在砂质壤土土柱中运移的数值模拟

通过室内土柱出流实验,分析了重金属离子铜在饱和砂质壤土中的运移行为,发现高浓度的入流液有利于铜离子的运移。同时借助于软件包CXTFIT,用确定性平衡模型和非平衡两区模型对铜离子的出流动态进行了拟合,并预测了土柱不同深度处铜离子浓度随时间的变化过程。结果表明,室内饱和均质条件下,应用确定性平衡模型拟合参数模拟精度要高于非平衡两区模型,可以不用考虑不动水体对铜离子运移的影响。     

NaClO氧化水中As(Ⅲ)的实验研究

利用氧化剂将水中的As(Ⅲ)氧化成As(Ⅴ),既可提高去除效果,又可降低毒性。文章以NaClO作为氧化剂进行了氧化As(Ⅲ)的相关实验,实验结果表明:pH在4~11的范围内对NaClO氧化As(Ⅲ)的影响不大,As(Ⅲ)的氧化率随着NaClO的投加量和氧化反应时间的增加而增大,其氧化过程更符合一级动力学过程。结论:NaClO氧化As(Ⅲ)迅速,氧化率基本可达到100%,氧化效果明显。     

The culture of compound bioflocculant and the analysis of its activated components

利用农业固体废弃物秸秆类纤维素为原料制备复合型生物絮凝剂（CBF）,优化了CBF的培育条件。同时解析了CBF活性物质在发酵液中的分布,并对CBF的活性组分进行了研究。结果表明,在高效纤维素降解菌HIT-3的作用下,秸秆类纤维素发酵3天产糖量达到高峰,此时接入CBF产生菌于灭菌后的纤维素发酵液中,在30℃、140r/min的旋转式摇床上培养36h,整个过程中只需将纤维素发酵培养基的pH值调节到7.2。在上述条件下CBF可获得较优的絮凝效果;多糖是CBF的主要组成成分,CBF的热稳定性良好。其絮凝活性物质主要分布在上清液中。     

基于水质模拟的不确定条件下两阶段随机水资源规划模型

针对流域内不同企业的水资源分配及企业生产污染排放导致的水环境问题,运用区间两阶段随机规划的方法,耦合区间两阶段模型（ITSP）和区间水质模型（IS-P）,建立不确定两阶段随机水质-水量耦合规划模型（ITSP-SP）.该模型以流域内系统利益最大为目标函数,模拟了流域内各个企业的水量分配及排污过程中河道水质变化,并在保证河流水质达标前提下优化预计分配水量,调整企业生产规模.通过模型运算得到区间解,为管理者提供了多样的决策方案.并且,该模型充分考虑不确定因素对系统利益的影响,能够有效的规避系统决策失误及方案缺失现象.     

道南膜技术测定Ca(NO3)2溶液体系中汞的化学形态

虽然道南膜技术(DMT)已经成功用于土壤/溶液中多种重金属自由态离子浓度的测定,但DMT技术测定Hg的形态尚未解决.采用DMT测定Ca(NO3)2溶液体系中Hg化学形态.实验结果表明,Hg在阳离子交换膜内的吸附除静电吸附外还存在结合力更强的化学吸附,Hg在阳离子交换膜内扩散成为Hg跨膜传输受阻的主要因素,限制道南膜技术用于Hg形态测定.Hg2+和Hg(OH)2都表现出在阳离子交换膜上的强烈吸附,供端(Donor)Hg损失达50%以上.缩短试验时间至8h以内,可在一定程度上降低Hg吸附.计算结果表明,由于大量的Hg滞留在阳离子交换膜内,在计算受端(Acceptor)Hg浓度时引入滞留系数补偿供端Hg的损失,较好地预测了Ca(NO3)2溶液体系中Hg的化学形态.     

Oxidative removal of acetaminophen using zero valent aluminum-acid system: Efficacy, influencing factors, and reaction mechanism

Commercial available zero valent aluminum under air-equilibrated acidic conditions (ZVAl/H⁺/air system) demonstrated an excellent capacity to remove aqueous organic compounds. Acetaminophen (ACTM), the active ingredient of the over-the-counter drug Tylenol^®, is widely present in the aquatic environment and therefore the treatment of ACTM-contaminated water calls for further research. Herein we investigated the oxidative removal of ACTM by ZVAl/H⁺/air system and the reaction mechanism. In acidic solutions (pH < 3.5), ZVAl displayed an excellent capacity to remove ACTM. More than 99% of ACTM was eliminated within 16 hr in pH 1.5 reaction solutions initially containing 2.0 g/L aluminum and 2.0 mg/L ACTM at 25 ± 1\textcelsius. Higher temperature and lower pH facilitated ACTM removal. The addition of different iron species Fe⁰, Fe²⁺ and Fe³⁺ into ZVAl/H⁺/air system dramatically accelerated the reaction likely due to the enhancing transformation of H₂O₂ to HO. via Fenton's reaction. Furthermore, the primary intermediate hydroquinone and the anions formate, acetate and nitrate, were identified and a possible reaction scheme was proposed. This work suggested that ZVAl/H⁺/air system may be potentially employed to treat ACTM-contaminated water.     

Biological sulfate removal from acrylic fiber manufacturing wastewater using a two-stage UASB reactor

A two-stage UASB reactor was employed to remove sulfate from acrylic fiber manufacturing wastewater. Mesophilic operation (35±0.5℃) was performed with hydraulic retention time (HRT) varied between 28 and 40 hr. Mixed liquor suspended solids (MLSS) in the reactor was maintained about 8000 mg/L. The results indicated that sulfate removal was enhanced with increasing the ratio of COD/SO₄^2-. At low COD/SO₄^2-, the growth of the sulfate-reducing bacteria (SRB) was carbon-limited. The optimal sulfate removal efficiencies were 75% when the HRT was no less than 38 hr. Sulfidogenesis mainly happened in the sulfate-reducing stage, while methanogenesis in the methane-producing stage. Microbes in sulfate-reducing stage performed granulation better than that in methane-producing stage. Higher extracellular polymeric substances (EPS) content in sulfate-reducing stage helped to adhere and connect the flocculent sludge particles together. SRB accounted for about 31% both in sulfate-reducing stage and methane-producing stage at COD/SO₄^2- ratio of 0.5, while it dropped dramatically from 34% in sulfate-reducing stage to 10% in methane-producing stage corresponding to the COD/SO₄^2- ratio of 4.7. SRB and MPA were predominant in sulfate-reducing stage and methane-producing stage respectively.