高级氧化技术矿化水中三氯甲烷和二氯甲烷理论极限浓度分析

对环境安全性尤其是饮用水安全而言,通常认为的高级氧化技术(AOPs)"彻底降解"大多数有毒有机污染物的观点需应用化工热力学分析来检验.本文分别以三氯甲烷(CHCl3)和二氯甲烷(CH2Cl2)为模型体系,分析了不同氯代甲烷初始浓度、pH值和羟基自由基(·OH)浓度下,AOPs矿化水中氯代甲烷的平衡浓度(即矿化理论极限浓度).结果表明,CHCl3和CH2Cl2与·OH矿化反应的理论极限浓度均随着初始浓度的增加而增加,随着·OH浓度的增加而明显减小;CHCl3与·OH矿化反应的理论极限浓度随着pH值的增加而明显减小(pH3.0～3.5除外),CH2Cl2与·OH矿化反应的理论极限浓度在文献报道的·OH浓度下随着pH值的增加无明显变化,而在·OH浓度分别增至文献值的10和100倍时,CH2Cl2与·OH矿化反应的理论极限浓度随着pH值由2.0增至3.0和由3.5增至4.5而不断减小,由3.0增至3.5和由4.5增至5.0而增加.较高的·OH浓度,较高pH值(pH4.0～5.0)的酸性环境以及较低的初始浓度对氯代甲烷的彻底矿化更有利.     

介质阻挡放电脱除甲醛的化学动力学模拟

对大气压介质阻挡放电脱除甲醛进行了化学动力学模拟, 建立了时空平均化的模型, 并对相关的结果进行了实验验证. 分析了各主要物种的浓度随放电时间的变化, 在模拟空气气氛下, HCHO主要由O·和OH·自由基脱除, 其中, OH·自由基的作用更为突出. 强调了氮分子的第一电子激发态N2(A3∑+u)的作用, 它与O2、H2O 分子的碰撞增加了O·和OH·自由基的浓度,在氮气气氛中, N2(A3∑+u)态是使HCHO脱除的主要物种.讨论了HCHO初始浓度、气体流量对HCHO 脱除比能耗和产物中CO2/CO 摩尔比值的影响, HCHO 初始浓度较高时, 甲醛脱除的比能耗较低, 在输入能量密度<60 J·L-1, HCHO 初始浓度较低时, 产物中nCO2 /nCO值较高.     

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.     

漆酶催化氧化水中有机污染物*

漆酶是一种含铜的多酚氧化酶, 属于铜蓝氧化酶蛋白, 能催化氧化多种难降解的有机污染物。漆酶催化氧化水中有机污染物具有底物广泛、能耗低、易操作、环境友好等优点,是一项前景广阔的生物处理技术。本文综述了漆酶对水中有机污染物的催化降解,主要从漆酶的化学组成、结构、催化降解机理、漆酶的固定化、影响因素（溶液pH值、温度、金属离子、营养因子、有机溶剂、漆酶的浓度、底物的初始浓度等）、降解的动力学以及漆酶在处理水中有机污染物的应用等五个方面介绍了相关的研究进展。漆酶催化氧化有机物的机理主要表现在底物自由基中间体的产生和氧气还原成水两个方面。本文提出了目前漆酶催化氧化水中有机污染物存在的主要问题,并展望了漆酶降解水体中有机污染物的发展方向。     

UV/H2O2工艺湿法脱除燃煤烟气中NO的研究

在自行设计的内置紫外光-鼓泡器中，利用UV/H₂O₂高级氧化工艺湿法脱除燃煤烟气中的NO气体。主要对紫外光强度、H₂O₂初始浓度、NO初始浓度以及烟气总流量对NO脱除效率的影响进行了考察。研究结果表明，在实验范围内，NO脱除效率随着紫外光强度和H₂O₂初始浓度的增加而增加，但当达到一定值后，NO脱除效率的增加幅度均变得相对平缓；NO脱除效率随着NO初始浓度以及烟气总流量的增加呈近似线性减小。通过离子色谱对液相离子产物进行了定性与定量检测，并对NO中的氮元素进行了物料平衡计算，在此基础上对NO脱除路径与产物形态进行了理论分析。
     

废水中有机污染物降解机理的研究方法

我国废水排放总量较大,且废水中含有的多种有机污染物一直是人类生命健康的潜在威胁,因此对废水处理的研究必不可少,而理解废水中有机污染物的降解机理是处理各种废水的基础.本综述概述了国内外针对各种有机污染物降解机理的研究方法,主要包括实验手段和计算模拟两大类.实验手段中主要采用光谱分析技术检测有机污染物降解过程中生成的中间产物,进而推测有机污染物的降解路径.但是由于实验条件和实验方法的不同,对于同种物质的降解机理研究,不同的实验结果存在着争议.基于量子化学计算、定量构效关系模型（QSAR）、定量结构-生物降解性能关系模型（QSBR）、统计分子碎化模型（SMF）等计算模拟方法为有机污染物降解机理的研究提供了新的方法.将实验手段和计算模拟有机结合起来,可为有机污染物的降解机理研究提供参考和指导.     

对流扩散传质滞后的电极过程中之非Poisson涨落与非Nernst浓度极化

根据对流扩散传质滞后的恒稳电极过程中边界层的物理图像, 提出了该类电极过程的简化随机模型, 建立了相应的浓度极化的随机热力学理论, 揭示了非Nernst浓度极化来自于随电流密度增大电极化学反应体系涨落分布的非Poisson化与对中心极限律的偏离, 进一步阐明了与滞后的扩散步骤共存的对流传质对非Nernst浓度极化的效应及其规律. 同时, 给出了对流引起的非Nernst浓度极化的随机热力学算例.     

氢解还原法进行环境污染控制

化学氢解法具有脱卤、脱氮、脱硫、脱芳构化等作用,目前的研究表明该方法对环境中的许多重要污染物都具有还原去除效果,包括卤代化合物、硝基芳香化合物、有机硫化合物、多环芳烃等有机污染物,以及硝酸盐、硫酸盐、氮氧化物、二氧化硫、重金属等无机污染物。为此,本文综述了氢解还原方法降解各类污染物的研究现状,分别介绍了上述各种污染物氢解还原的脱除机理以及影响因素的作用机制,基于绿色化学的要求分析了氢解还原方法的技术优势,从提高氢解效率和节能的角度提出了今后的研究方向。     

液相色谱过量热力学函数变化规律性探讨

本文从溶液热力学和色谱理论推导出过量热力学函数与色谱参数间的关系, 测定了苯的同系物在液-液分配过程中, 过量焓变等函数与流动相组成、样品碳数的线性关系,并求得经验方程式. 同时研究了不同样品焓变和熵变的线性补偿规律. 并试图从溶液理论进行计算.     

红外光谱及其理论模拟在砷吸附过程中的应用

红外光谱技术具有分析速度快、分辨率高、灵敏度高、可以实时原位分析监测等优点。基于密度泛函理论对矿物吸附砷污染物体系红外光谱进行理论计算，分析对比红外光谱实测特征峰和理论计算特征峰，可以揭示砷吸附过程微观机制和表面化学形态。对红外光谱技术在水铁矿、赤铁矿、针铁矿等主要矿物吸附无机砷酸和有机胂酸的定性定量分析进行了综述，总结了红外光谱在无机和有机砷污染物吸附体系的定性定量研究及理论计算，为砷污染物精准检测分析和砷污染控制提供参考。     

Thermodynamic analysis of the theoretical energy consumption in the removal of organic contaminants by physical methods

The essential requirements for evaluating the sustainable development of a system and the thermodynamic framework of the energy conservation mechanism in the waste-removal process are proposed.A thermodynamic method of analysis based on the first and second laws of thermodynamics is suggested as a means to analyze the theoretical energy consumption for the removal of organic contaminants by physical methods.Moreover,the theoretical energy consumption for the removal by physical methods of different kinds of...     

Theoretical limit of energy consumption for removal of organic contaminants in U.S. EPA Priority Pollutant List by NRTL,UNIQUAC and Wilson models

This paper quantifies the theoretical limit of energy consumption for the removal of 20 representative organic contaminants (9 chlorinated alkyl hydrocarbons, 3 chlorinated alkenes, 3 brominated methanes, 5 aromatic hydrocarbons and their derivatives) in the United States Environmental Protection Agency (U.S. EPA) Priority Pollutant List by physical procedures. The general rules of the theoretical limit of energy consumption with different initial concentrations at 298.15 K and 1.01325 × 10⁵ Pa by NRTL, UNIQUAC and Wilson models are obtained from the thermodynamic analysis with our previously established method based on the thermodynamic first and second law. The results show that the waste treatment process needs a high energy consumption and the theoretical limit of energy consumption for organic contaminant removal increases with decreasing initial concentrations in aqueous solutions. The theoretical limit of energy consumption decreases with the more C–H bonds being replaced by C–Cl or C–Br bonds in chlorinated methanes, ethanes, ethenes or brominated methanes except for 1,1,2,2-tetrachloroethane, and the energy consumption for the removal of chlorinated methanes is higher than that of chlorinated ethanes with the same C–H bonds being replaced by C–Cl bonds. For the removal of chlorinated ethenes, brominated methanes and benzene and its derivatives studied, the energy consumption has corresponding relationship with solubility and the energy consumption is higher for the removal of organics with higher solubility.     

Influence of reactor design on the electrochemical oxidation and disinfection of wastewaters using boron-doped diamond electrodes

Electrochemical oxidation is the most popular electrochemical advanced oxidation process within the scientific community owing to its simplicity and high effectiveness to treat different wastewaters. Electrode material and reactor design are important factors that influence the removal efficiency of pollutants. This work presents an overview of recent applications of electrochemical oxidation process for contaminant mineralization and water disinfection using electrochemical reactors, in batch and continuous mode of operation, fitted with boron-doped diamond electrodes. In addition, recent advances in the use of flow-through reactors (continuous single-pass and recirculation) are presented. Geometrical aspects, operating conditions, and energy consumption are provided and discussed.     

Recovery of organic acids from waste salt solutions derived from the manufacture of cyclohexanone by electrodialysis

The possibility of recovery of organic acids from waste salt solution, derived from the manufacture of cyclohexanone, by means of single anion-exchange membrane electrodialysis was studied in this paper. Some key parameters, such as voltage, current density, pH value, current efficiency and specific energy consumption are studied and analyzed in details on theoretical basis. Results indicate that single anion-exchange membrane electrodialysis is found to be a feasible method for recovery of organic acids. Several valuable acids, such as butyric and adipic acids are effectively separated from waste salt solution by only one-step electrodialysis. And it consumes less energy compared to the conventional processes.     

Separation and quantitation of hazardous wastes from abrasive blast media.

A sample of glass bead abrasive blasting material (ABM) waste, received from Robins Air Force Base (Georgia), was examined to determine whether the waste could be rendered nonhazardous by separating paint contaminants from the ABM. The sample was analyzed with size distribution and toxicity characteristics leaching procedure. A Microtrac analyzer was used to measure the size of fine particles (-325 Tyler mesh), and scanning electron microscopy analysis was performed to identify the nature of the contaminants in the ABM waste. Tests using froth flotation, magnetic separation, desliming, and acid washing were conducted to develop a process for removing the contaminants. A pilot plant test using the developed process rendered 82.1% or the ABM waste material nonhazardous.     

Removal of Multiple Contaminants from Water by Polyoxometalate Supported Ionic Liquid Phases (POM‐SILPs)

The simultaneous removal of organic, inorganic, and microbial contaminants from water by one material offers significant advantages when fast, facile, and robust water purification is required. Herein, we present a supported ionic liquid phase (SILP) composite where each component targets a specific type of water contaminant: a polyoxometalate‐ionic liquid (POM‐IL) is immobilized on porous silica, giving the heterogeneous SILP. The water‐insoluble POM‐IL is composed of antimicrobial alkylammonium cations and lacunary polyoxometalate anions with heavy‐metal binding sites. The lipophilicity of the POM‐IL enables adsorption of organic contaminants. The silica support can bind radionuclides. Using the POM‐SILP in filtration columns enables one‐step multi‐contaminant water purification. The results show how multi‐functional POM‐SILPs can be designed for advanced purification applications.     

Adsorption of Sr by immobilized microorganisms

Wastewaters from numerous industrial and laboratory operations can contain toxic or undesirable components such as metal ions, which must be removed before discharge to surface waters. Adsorption processes that have high removal efficiencies are attractive methods for removing such contaminants. For economic operations, it is desirable to have an adsorbent that is selective for the metal contaminant of interest, has high capacity for the contaminant, has rapid adsorption kinetics, can be economically produced, and can be regenerated to a concentrated waste product or decomposed to a low-volume waste. Selected microorganisms are potentially useful adsorbents for these applications because they can be inexpensive, have high selectivities, and have high capacities for adsorption of many heavy metals, which are often problems in a variety of industries.     

Biochar derived from waste bamboo shoots for the biosorptive removal of ferrous ions from aqueous solution

With the ongoing global demands for modern commodities, anthropogenic activities by industries and humans have brought a colossal pressure to the natural water bodies. Though numerous scientific interventions or treatment techniques have been proposed, the need for a viable low-cost method has been a quest for many researchers. Adsorption as such has been in the limelight as an effective method in recent times using various feedstock biomass waste. Our present piece of research aims to use the non-edible biomass waste generated from bamboo shoots as a sustainable low-cost biochar adsorbent and examine its efficiency in the removal of ferrous (Fe²⁺) ions from an aqueous solution. The batch adsorption study was conducted and the optimum dose and concentration were found to be 0.2 g and 7 mg L^?1 with the Langmuir isotherm model best describing the experimental data. Furthermore, kinetic study suggests that the overall sorption rate predominantly follows the chemisorption pathway. Multiple studies suggest bamboo is an excellent adsorbent for treating various inorganic & organic contaminants; here we have highlighted the multifaceted applications of waste bamboo shoots as an effective adsorbing material. The obtained results can lead to additional benefits and usage of bamboo shoots (waste) with future research prospects.     

Ionic liquid modification of zeolite and its removal of chromate from water

This study focused on using imidazolium of different chain lengths to modify the negatively charged zeolite. The modification involves a cation exchange process of the organic cations of ionic liquids (ILs) for the alkali and alkaline earth elements on zeolite surfaces. X-ray diffraction analyses revealed that the uptake of ILs was on the external surfaces. Fourier transform infrared analyses showed that different mechanisms were attributed to IL uptake on zeolite at below and above the external cation exchange capacity. After modification, the zeolite reversed its surface charge to positive, thus enhancing adsorptive removal of anionic contaminants such as chromate from water. At the same time, the modified zeolite increased their total organic carbon content, and thus could promote better adsorptive removal of hydrophobic organic contaminants from water, too. These features enable IL-modified zeolite to be used as inexpensive sorbents for the removal of multi-types of contaminants from water simultaneously.     

Removal of some nitrophenol contaminants using alginate gel beads

Biopolymers such as alginates are commonly used to remove the cationic contaminants from wastewaters. The major component of the alginate is the alginic acid, a linear, binary heteropolymer of β-d-mannuronate and -l-guluronate residues. In this study the fundamental aspects in the preparation of alginate beads and the effects of salt, sodium alginate concentrations and two cationic surfactants (dodecyltrimethylammonium bromide, cetyltrimethylammonium bromide) on the domains of binding isotherms were investigated. The alginate cross-link complexes with metal ions can exist either as homogeneous clear solutions or precipitates or as spherical beads. The applicability of the calcium and calcium–iron alginate gel beads for removal of some nitrophenols from aqueous solutions was studied. The sorption and kinetic experiments were conducted under different values of pH, initial concentration of nitrophenols and the amount of alginate gel beads. The removal efficiency of contaminant increases with the increasing of the pH and the quantity of alginate beads and decreases with the increasing of initial contaminant concentration. The uptake of nitrophenols occurs rapidly in the first 12 h, followed by a slow process that takes about 72 h. According to the egg-box model of gelation mechanism the cavities formed in the alginate gel capture the cationic contaminants. The adsorption equilibrium data obtained for nitrophenols derivatives at various pH and initial solid sorbent amount were applied to the two classical models, i.e. Langmuir and Freundlich, and the isotherm parameters were calculated.