水中有机污染物微观分布的理论模型与方法

考虑实际水体,建立了有机污染物在水中分布的理论模型,用物理化学方法推导出计算污染物在水体中分布的数学方程式和数学解析式.用MNDO方法计算了卤代苯的相对分布值(PN),结果与辛醇-水分配系数实验值相符合.     

水环境介质中有机污染物微观分布的理论模型——污染物·水复合体·水簇模型

以水簇模拟水环境介质, 水体中有机污染物的分子状态用水-有机污染物分子复合体模拟,得出有机污染物在水环境介质中微观分布的数学表达式, 经过微观动力学方法处理, 得到了相应的数学解析式.用 ab initio 方法 STO-3G 基组计算了4个多环芳烃在水中的微观分布情况, 计算结果与辛醇-水分配系数的实验值相吻合.     

水环境介质中有机污染物微观分布的理论模型：污染物.水复合体 …

以水簇模拟水环境介质,水体中有机污染物的分子状态用水－有机污染物分子复合体模拟,得出有机污染物在水环境介质中微观分布的数学表达式,经过微观动力学方法处理,得到了相应的数学解析式。用ａｂ ｉｎｉｔｉｏ方法ＳＴＯ－３Ｇ基组计算了４个多环芳烃在水中的微观分布情况,计算结果与辛醇－水分配系数的实验值相吻合。     

有机污染物在水环境介质中分布的理论研究

用物理化学原理从分子水平研究有机污染物在水环境介质中的分布。建立了模拟水环境介质一维模型，推导出计算分布值的数学表达式．     

太湖水体中有机污染物的分析

利用超临界流体萃取与热脱附两种样品预自理方法的优势互补,与气相色谱分析相结合对太湖水体中不同沸点有机污染物进行了分析,发现太湖水中除了烃类污染物外还存在大量含氮有机污染物。其分布表明入湖河道中排放的工业污染物的流入是导致太湖水富营养化的一个重要因素。     

抗生素不同解离形态在水环境中的光化学行为

表层水体中存在众多可解离的有机污染物,揭示其不同解离形态的环境光化学行为,对于污染物的环境持久性和风险评价具有重要意义.抗生素是在水环境中广泛存在的新型有机污染物,其中氟喹诺酮类(FQs)、磺胺类(SAs)、四环素类(TCs)等抗生素因分子结构中含有羧基、羟基和/或氨基等可电离基团,在水中以多种解离形态共存而备受关注.抗生素的多种解离形态不仅以不同的丰度共存于环境表层水体中,而且不同的解离形态表现出相异的环境光化学转化行为和风险.本文总结了水环境中可解离抗生素光化学行为研究的最新进展,介绍了pH值对直接和间接光解动力学的影响,着重评述了抗生素不同解离形态的光化学反应动力学、转化产物和路径,讨论了可解离抗生素光化学转化的环境半减期和风险,最后对抗生素不同解离形态的光化学行为研究进行了展望.     

顶空气相色谱法测定包装纸中有机污染物在纸和空气间的分配系数

食品包装纸中有机污染物在纸和空气间的分配系数Kpaper/air是研究食品包装纸中有机污染物向食品迁移的一个重要的理化参数.本研究推导了顶空气相色谱法(HS-GC)测定包装纸中有机污染物的Kpaper/air的理论关系式.本方法不需要测定纸张中有机污染物的具体浓度,只需测定两份纸样的不同体积及峰面积即可计算出Kpaper/air值.进行了顶空气相色谱法精确度和准确度的计算分析和实验验证,证实了本方法的精确性和准确性.研究还表明,本测定方法中两份纸样的体积比x是一个重要参数.本方法可以快速、便捷、准确的测定包装纸中有机污染物在纸和空气间分配系数Kpaper/air.     

物理法COD减排理论极限能耗的热力学分析

首先针对系统的可持续性发展提出了三点本质要求,在此基础上提出了基于减排过程节能机制的热力学框架,并根据热力学第一、第二定律建立了计算物理法脱除有机污染物理论极限能耗的热力学分析方法.此外,以典型有机污染物的脱除为例,分别计算了封闭体系中298.15K和1.01325×105Pa下不同初始浓度、不同种类以及不同COD减排量的有机污染物脱除的理论极限能耗.本文的计算结果表明,废水中有机污染物的减排需要很高的能耗,脱除相同量有机污染物所需的理论极限能耗随着初始浓度的减小而显著增加,且不同种类污染物处理的难易程度和能耗高低相差很大,这充分说明减排与节能有着密不可分的联系,充分考虑污染物的种类、物理化学性质、毒性和浓度将有助于减排政策的科学制定.     

固相萃取-气相色谱-质谱法测定地面水中半挥发性有机化合物

九龙江是福建省第二大河流,流经龙岩、漳州和厦门3地区13个县市,是闽南地区人民的主要饮用水源.该流域水体中无机污染物早已列入常规监测项目,其污染程度有逐年加重的趋势,而有机污染物则缺乏实测数据,因此有必要测定该流域水体中有机污染物,以确定九龙江流域水体有机污染程度.     

环境中有机磷污染物碱性的理论研究

有机膦化合物的碱度对深入了解有机膦类污染物的降解有着重要的意义. 发展基于第一性原理的理论方法精确计算有机膦化合物的pKa值有重要意义. 本研究工作发展了精确计算有机膦阳离子化合物pKa值的方法: 用B3LYP/6- 31＋G(d)优化气相结构, PBEPBE计算单点能量, IEFPCM/Bondi (f＝1.0)计算溶剂化能. 理论值与实验值比较, 其平均偏差和均方根差分别为－0.6 pKa单位和0.7 pKa单位. 基于此方法, 我们研究了常见有机膦污染物阳离子的碱性, 定量计算其pKa值. 并进一步讨论了这类化合物的α取代效应和远程取代效应对其碱性的影响, 总结了影响杂环有机膦化合物阳离子酸性的因素.     

Heat capacity and cluster structure of saturated water vapor

The value and temperature dependence of the heat capacity of saturated water vapor are studied. It is shown that the behavior of the heat capacity is determined by the formation of dimers, tetramers, and higher-order clusters, and by excitation of the hydrogen bond vibrations within these clusters. The temperature regions that correspond to water vapor as (a) a mixture of monomers and dimmers and (b) as a mixture of monomers, dimmers, and tetramers, are determined.     

Dilute Methane Treatment by Atmospheric Pressure Dielectric Barrier Discharge: Effects of Water Vapor

Oxidation of dilute methane in oxygen containing mixtures by atmospheric pressure dielectric barrier discharge at moderate temperature (below 150°C) has been studied with regard to the effect of water vapor. First, the impact of water vapor on methane conversion was studied in nitrogen. In dry nitrogen, methane was converted into hydrogen cyanide and hydrogen in the absence of oxidant. When water was added, it both acted as a scavenger in competition with methane for reactive nitrogen species and changed the reaction product speciation from HCN to carbon monoxide and carbon dioxide. The addition of water also led to the formation of hydrogen and nitrogen oxides. In the presence of oxygen, the addition of 1% water vapor enhanced methane conversion. Increasing water vapor content above 1% had a slight positive effect on methane conversion, and was found to enhance selectivity of the reaction products toward carbon dioxide over carbon monoxide.     

水合物生成条件下甲烷在水中的吸附

采用悬滴法系统地测定了温度274.2 ~ 282.2 K、压力0.1 ~ 10.1 MPa下甲烷/纯水间界面张力。实验结果表明在恒定温度下界面张力随压力的增加而增大。在高压条件下,压力对界面张力有很大的影响。不同温度和压力下计算出的甲烷在水中的表面过剩浓度结果表明,压力越高,温度越低,甲烷在水溶液中的吸附浓度越高。同时,计算出的甲烷在水溶液中的表面吸附自由能结果表明,在水合物生成条件下,甲烷在水中的吸附比298.2 K更容易。     

Improving methane storage on wet activated carbons at various amounts of water

Different mesoporous activated carbons were prepared by both chemical and physical activation processes and were examined for methane uptake in the presence of water.Methane isotherms were obtained at ...     

The interface between water and a hydrophobic gas

Classical molecular dynamics simulations have been performed to investigate the interface between liquid water and methane gas under methane hydrate forming conditions. The local environments of the water molecules were studied using order parameters which distinguish between liquid water, ice and methane hydrate phases. Bulk water and water/air interfaces were also studied to allow comparisons to be made between water molecules in the different environments and to determine the effects of the different methane densities studied. Good agreement between experimental and calculated surface tensions is obtained if long range corrections are included. The water surface is found to have a structure which is very similar to that of bulk water, but more tetrahedral, and more clathrate-like than ice-like. In these simulations the concentration of methane in water at the interface is shown to be appropriate for clathrates at higher gas densities (pressures). The orientation of water molecules around methane molecules in the interfacial region appears to depend only weakly on pressure and one of the difficulties in forming hydrate is the availability of water molecules tangential to the hydrate cage. At the interface, the water structure is more disordered than in the bulk water region with increased occurrence compared with the bulk of those angles and orientations found in the clathrate structure.     

Global search for minimum energy (H2O)n clusters, n = 3-5

The Gaussian-3 (G3) model chemistry method has been used to calculate the relative deltaG(o) values for all possible conformers of neutral clusters of water, (H2O)n, where n = 3-5. A complete 12-fold conformational search around each hydrogen bond produced 144, 1728, and 20,736 initial starting structures of the water trimer, tetramer, and pentamer. These structures were optimized with PM3, followed by HF/6-31G* optimization, and then with the G3 model chemistry. Only two trimers are present on the G3 potential energy hypersurface. We identified 5 tetramers and 10 pentamers on the potential energy and free-energy hypersurfaces at 298 K. None of these 17 structures were linear; all linear starting models folded into cyclic or three-dimensional structures. The cyclic pentamer is the most stable isomer at 298 K. On the basis of this and previous studies, we expect the cyclic tetramers and pentamers to be the most significant cyclic water clusters in the atmosphere.     

Free energy profiles for penetration of methane and water molecules into spherical sodium dodecyl sulfate micelles obtained using the thermodynamic integration method combined with molecular dynamics calculations

The free energy profiles, ΔG(r), for penetration of methane and water molecules into sodium dodecyl sulfate (SDS) micelles have been calculated as a function of distance r from the SDS micelle to the methane and water molecules, using the thermodynamic integration method combined with molecular dynamics calculations. The calculations showed that methane is about 6-12 kJ mol(-1) more stable in the SDS micelle than in the water phase, and no ΔG(r) barrier is observed in the vicinity of the sulfate ions of the SDS micelle, implying that methane is easily drawn into the SDS micelle. Based on analysis of the contributions from hydrophobic groups, sulfate ions, sodium ions, and solvent water to ΔG(r), it is clear that methane in the SDS micelle is about 25 kJ mol(-1) more stable than it is in the water phase because of the contribution from the solvent water itself. This can be understood by the hydrophobic effect. In contrast, methane is destabilized by 5-15 kJ mol(-1) by the contribution from the hydrophobic groups of the SDS micelle because of the repulsive interactions between the methane and the crowded hydrophobic groups of the SDS. The large stabilizing effect of the solvent water is higher than the repulsion by the hydrophobic groups, driving methane to become solubilized into the SDS micelle. A good correlation was found between the distribution of cavities and the distribution of methane molecules in the micelle. The methane may move about in the SDS micelle by diffusing between cavities. In contrast, with respect to the water, ΔG(r) has a large positive value of 24-35 kJ mol(-1), so water is not stabilized in the micelle. Analysis showed that the contributions change in complex ways as a function of r and cancel each other out. Reference calculations of the mean forces on a penetrating water molecule into a dodecane droplet clearly showed the same free energy behavior. The common feature is that water is less stable in the hydrophobic core than in the water phase because of the energetic disadvantage of breaking hydrogen bonds formed in the water phase. The difference between the behaviors of the SDS micelles and the dodecane droplets is found just at the interface; this is caused by the strong surface dipole moment formed by sulfate ions and sodium ions in the SDS micelles.     

Water transfer characteristics in the vertical direction during methane hydrate formation and dissociation processes inside non-saturated media

In order to study water transfer characteristics inside non-saturated media during methane hydrate formation and dissociation processes, water changes on the top, middle and bottom locations of experimental media during the reaction processes were continuously followed with a novel apparatus with three pF-meter sensors. Coarse sand, fine sand and loess were chosen as experimental media. It was experimentally observed that methane hydrate was easier formed inside coarse sand and fine sand than inside loess. Methane hydrate formation configuration and water transfer characteristics during methane hydrate formation processes were very different among the different non-saturated media, which were important for understanding methane hydrate formation and dissociation mechanism inside sediments in nature.     

Formation of pure hydrogen from methane

The methods for production of pure hydrogen from methane are summarized. One method is methane decomposition to hydrogen and carbon nanofibers. Ni-based catalysts with high activity and long life for the methane decomposition were developed. The other method is based on the redox of iron oxides, i.e., Fe₃O₄ is reduced with methane to iron metals and, subsequently, iron metals are oxidized with water vapor to form hydrogen. Iron oxide mediators that could be reduced with methane and subsequently be oxidized with water vapor at low temperatures were designed.     

水蒸气存在时Mo/HZSM-5催化剂上的甲烷芳构化反应性能

研究了水蒸气存在条件下Mo/HZSM-5沸石分子筛催化剂上的甲烷芳构化反应行为,发现水蒸气的引入可以明显地降低甲烷芳构化反应的起始温度,从而在较为温和的条件下实现甲烷的活化.适量水蒸气的加入可以在一定程度上改善Mo/HZSM-5催化剂的稳定性,过量水蒸气的引入则会抑制甲烷芳构化反应.在反应温度为973 K时,引入适量的水蒸气对芳构化反应产物的分布没有明显影响在低温条件下的甲烷芳构化反应过程中检测到有乙烯生成,该结果支持了甲烷芳构化反应可能经历了乙烯这一中间产物的机理.实验结果还表明,水蒸气对催化剂上的积炭量没有明显的影响.