影响大气汞化学过程的敏感因子分析

为了分析汞在大气中的化学行为,在一个化学模式中加入汞的气相、气液平衡和液相反应,模拟大气汞及其化合物的演变规律,并分析了气象因子(云、光解率、温度)和化学因子(气态O3、H2O2、HO2、OH和气态零价汞Hg0(g))的初始体积分数对各形态汞及其化合物浓度和Hg0(g)转化率的影响.模拟结果表明,在中等大气污染条件下,Hg0(g)的每小时平均转化率为2.91%.敏感性试验结果表明,云量、光解率、温度、O3和Hg0(g)的初始体积分数对不同形态汞的影响较为显著.云量的增加、光解率的增加、臭氧初始体积分数的升高,各形态汞的平衡时间缩短,除气态氧化汞和一价汞离子外,其他形态汞的平衡浓度均会降低,Hg0(g)的转化率增加.温度增加将抑制Hg0(g)的转化.Hg0(g)的初始体积分数增加,各形态汞的浓度升高,但其平均转化率没有显著变化.不同因子对汞化学过程的相对作用对区域或全球大气汞的环境模拟具有指导意义.     

十六烷基三甲基季铵盐-乙硫醇铵盐复合改性膨润土吸附性能研究

用十六烷基三甲基季铵盐(HDTMA)和乙硫醇铵盐(AET)双阳离子同时复合改性内蒙钙基膨润土(NMB),制得新型吸附材料HDTMA-AET-NMB.利用X射线衍射(XRD)、热分析(TG-DTA)、红外光谱(FT-IR)及N2-BET等测定发现,复合改性膨润土的表面性质和层间结构已发生显著改变.对重金属离子Cd2+和对硝基苯酚(PNP)的吸附研究表明,HDTMA-AET-NMB能协同吸附混合水溶液中的目标污染物,对水中重金属离子的吸附机理是膨润土层间的AET与被吸附的Cd2+形成了稳定的配合物;对水中对硝基苯酚的吸附源于其在长碳链疏水介质中的分配.复合改性膨润土可望应用于重金属-有机物混合废水的处理.     

黄土高原沟壑区小流域土壤有机碳与环境因素的关系

研究不同环境要素共同作用下的土壤有机碳分布特征及其与环境因素的关系对于全面准确评估黄土高原地区土壤有机碳状况和土壤碳循环具有重要意义.结合野外调查和室内分析,研究了黄土高原沟壑区典型小流域土壤不同组分有机碳分布特征及其与地形条件、土地利用方式和土壤类型之间的关系.结果表明,黄土沟壑区小流域土壤总有机碳变异较小(变异系数为34%),高活性有机碳变异较大(变异系数为43%),有机碳的变异性随其活性的增强而增大.各组分有机碳之间极显著正相关,而且在不同环境条件下的含量顺序一致.各组分有机碳在不同地形条件下以塬面土壤最高,沟道土壤最低:在不同土地利用方式下以林地和农田土壤较高,草地土壤较低;在不同土壤类型中则以黑垆土最高,红土最低.不同环境条件下各组分有机碳之间的关系分析表明,环境条件不但直接影响有机碳的分布,还通过影响有机碳不同组分之间的关系来改变其分布特征.研究区总有机碳与活性有机碳之问的关系受环境条件影响最大,中活性与高活性有机碳之间的关系受环境条件影响最小.     

春季南黄海溶解有机碳的分布特征及其受控因素

依据2007年4月对南黄海调查所得的溶解有机碳(DOC)数据,初步分析了南黄海DOC的分布特征及其影响因素。结果表明,2007年春季南黄海DOC的质量浓度为0.91～2.69 mg/L,平均值为1.62 mg/L,北部近岸DOC浓度高,长江口北部海域及南黄海中部外海DOC含量较低;在垂直方向上,10 m层DOC含量略高,各水层量值相差不大。DOC的分布趋势主要受控于水文结构,某些河口海域,生物生产对DOC含量也有一定的贡献。     

苏州澄湖湖底硬粘土地球化学特征及其成因意义

位于太湖平原的苏州澄湖,湖底十分平坦,主要由硬粘土组成。在湖底获得18.00m长的柱样,0～6.00m为长江三角洲东部平原区的第一硬粘土层。通过AMS14C测年、元素含量测定及物源判别函数DF、n(Na)/n(K)与CIA指数计算和A-CN-K三角模型图等分析,探讨了该硬粘土的成因及堆积后的后期改造作用。研究结果表明,该硬粘土形成于大约29～10kaB.P,为晚更新世晚期的风成堆积物。湖底硬粘土自堆积后至澄湖形成,长期暴露于地表,经历了强烈的风化成土作用,为中等风化强度。且3.50m上下段化学风化过程明显不同,3.50m以下硬粘土段为早期去Na、Ca阶段;3.50m以上硬粘土段已经进入中期去K阶段,经历了比前期更加强烈的化学风化和成土作用。反映了对全球气候变化及区域气候条件的响应。与典型风成堆积物相比,化学风化强度从洛川黄土→洛川古土壤、西峰红粘土→镇江下蜀土→澄湖SC6硬粘土→宣城风成红土依次增强。     

汽车涂装废水除镍的试验研究

镍是国家严格控制的一类污染物,采用化学沉淀法对汽车涂装废水进行除镍的试验研究。结果表明：投加氢氧化钙300mg／L,pH控制在11．0左右时,镍的去除率可以达到90．5％,出水完全满足《上海市污水综合排放标准（DB31／199）》。     

快速测定法与重铬酸钾法测定污水中化学需氧量的方法比较

重铬酸钾法测定化学需氧量,准确度高,但试剂消耗量大,占用空间大,耗时长,消耗大量的电和水。采用快速测定法后能快速省时、省水、省电、省试剂、省人力且操作简便。通过两种方法的比较,快速测定法的精密度及准确度均能达到国标的要求,并且具有成本低的特点,证明了此方法的可行性。快速测定法特别适用于污水处理等工艺过程控制的监测和测试。     

改性TiO2的制备、表征及光解水制氢性能研究

以陶粒为载体,采用改进的溶胶-凝胶法制备B、Ni共掺杂陶粒负载纳米TiO2光催化剂。利用XRD,TG-DTA,FT-IR等手段对其组成、结构等进行分析和表征。以250 W紫外灯为光源,三乙胺为目标污染物和电子给体,考察了B-Ni2O3-TiO2/陶粒合成体降解污染物耦合光解水制氢的光催化性能;结果表明：所制得的B-Ni2O3-TiO2/陶粒催化剂具有较高的产氢效率,并探讨了焙烧温度、三乙胺溶液初始浓度等对催化剂光催化活性的影响。     

Analysis of diffusion-adsorption equivalency of landfill liner systems for organic contaminants

The equivalence between multilayered barriers regarding diffusion and adsorption is analyzed by means of an analytical method. The bottom boundary of the liner system is defined by assuming concentration continuous and flux continuous conditions of the contaminant between the bottom liner layer and the underlying soil. Five different liner systems were compared in terms of solute breakthrough time. The results of the analysis show that breakthrough time of the hydrophobic organic compounds for a 2-meter-thick compacted clay liner (CCL) can be 3-4 orders of magnitude greater than the breakthrough time for a geosynthetic clay liner (GCL) composite liner. The GM/GCL and GM/CCL composite liner systems provide a better diffusion barrier for the hydrophilic organic compounds than that for the hydrophobic compounds due to their different Henry's coefficient. The calculated breakthrough times of the organic contaminants for the Chinese standard liner systems were found to be generally greater than those for the GCL alternatives, for the specific conditions examined. If the distribution coefficient increases to 2.8 for the hydrophobic compounds or 1.0 for the hydrophilic compounds, the thickness of the attenuation layer needed to achieve the same breakthrough time as the standard liner systems can be reduced by a factor of about 1.9-2.4. As far as diffusive and adsorption contaminant transport are concerned, GM or GCL is less effective than CCL.     

Evaluating the e ects of granular and membrane filtrations on chlorine demand in drinking water

In this study, chlorine decay experiments were conducted for the raw water from Nakdong River that is treated by Chilseo Water Treatment Plant (CWTP) situated in Haman, Korea as well as the e uents from sand and granular activated carbon (GAC) filters of CWTP and fitted using a chlorine decay model. The model estimated the fast and slow reacting nitrogenous as well as organic/inorganic compounds that were present in the water. It was found that the chlorine demand due to fast and slow reacting (FRA and SRA) organic/inorganic substances was not reduced significantly by sand as well as GAC filters. However, the treated e uents from those filters contained FRA and SRA that are less reactive and had small reaction rate constants. For the e uents from microfiltration, ultrafiltration, and nanofiltration the chlorine demand because FRA and SRA were further reduced but the reaction rate constants were larger compared to those of sand and GAC filter e uents. This has implications in the formation of disinfection by products (DBPs). If DBPs are assumed to form due to the interactions between chlorine and SRA, then it is possible that the DBP formation potential in the e uents from membrane filtrations could be higher than that in the e uents from granular media filters.