非均相催化臭氧氧化反应机制

臭氧催化氧化作为高级氧化技术是目前水处理领域研究的热点,其中非均相臭氧催化氧化技术因其氧化能力强、降低臭氧投加量特别是能显著提高有机物矿化率等优点而备受关注。非均相催化臭氧氧化领域不断研究新的催化剂,但是其反应过程及机制更加复杂。催化臭氧氧化的性能很大程度上取决于催化剂及其表面性质。污染物在催化剂表面形成络合物,或者臭氧在催化剂表面分解产生不同的含氧物种如表面氧原子、过氧化物和羟基自由基等。本文评述了非均相臭氧催化氧化反应中存在的多种机理,主要是自由基理论、氧空位理论、表面原子氧理论、表面络合物理论和臭氧直接氧化理论。催化剂表面的羟基基团是主要的催化活性中心,本文探讨了表面羟基基团催化反应机制,得出催化剂表面性质决定其表面活性位点的特性及含量,对诱导臭氧分解产生含氧活性物种起了关键作用;概述了催化剂改性后的结构形态、比表面积及其性能和作用机制;并讨论了非均相臭氧催化氧化反应催化剂未来的发展趋势,为催化臭氧氧化污水处理技术提供了理论参考。     

臭氧氧化技术处理含抗生素废水*

本文详细介绍了臭氧氧化技术的基本原理,分析了臭氧投加量、反应温度、溶液pH值、UV、H₂O₂及催化剂等因素对臭氧氧化处理抗生素废水效果的影响。根据抗生素的不同分类,综述了近年来关于臭氧氧化技术处理β-内酰胺、大环内酯、磺胺、喹诺酮、四环素、氯霉素六类常见抗生素废水的研究进展,并展望了臭氧氧化处理抗生素等难降解有机废水的发展趋势以及所面临的主要问题。     

臭氧的应用及产生技术

主要阐述了臭氧的性质、用途及产生技术,并重点介绍了臭氧的用途和臭氧产生技术的现状。     

臭氧氧化水中4-氯酚的机理和反应途径

研究了臭氧氧化4-氯酚的去除效果, 探讨了臭氧氧化4-氯酚的反应机理和反应特性. 臭氧氧化涉及两种强氧化剂, 臭氧分子和羟基自由基. 实验结果表明, 当溶液中没有清除剂清除羟基自由基时, 臭氧氧化4-氯酚产生中间产物过氧化氢, pH中性条件下, 过氧化氢和臭氧分子联合作用生成较多的羟基自由基, 113 mg/L的臭氧投加量能完全去除浓度为20 mg/L的4-氯酚以及39%的TOC. 溶液中完全清除羟基自由基后, 臭氧分子也可以高效去除4-氯酚, 4-氯酚先被氧化成黄色的对苯醌, 进而转化成甲酸和乙二酸. 提出了臭氧分子以及O₃/OH&;#8226;联合氧化4-氯酚的两 种反应途径. 臭氧氧化是一种高效去除4-氯酚的方法, 具有良好的应用前景.     

SnO2的制备及催化臭氧氧化活性

采用沉淀法制备了SnO2催化剂,以SnO2催化臭氧氧化降解糖蜜酒精废水脱色为探针反应,对催化剂的活性进行了评价.采用X射线衍射、红外光谱及热分析(TG-DSC)等技术对催化剂进行表征,研究了沉淀剂及焙烧温度等制备参数对SnO2催化臭氧氧化活性的影响.结果表明,SnO2催化剂对臭氧氧化降解糖蜜酒精废水脱色具有较高的催化活性,反应60 min后,糖蜜酒精废水的脱色率从单独臭氧氧化的43.04%提高到60.24%.沉淀剂对SnO2催化剂的活性影响很大,其中以氨水为沉淀剂制备的SnO2催化剂去羟基化反应程度高,所制得的催化剂活性最大.催化剂适宜的焙烧温度为723 K.SnO2吸附吡啶的红外光谱表明,催化剂表面存在L酸中心.臭氧在SnO2表面吸附的红外光谱表明,通过臭氧的末端氧原子与表面羟基及L酸中心成键,生成的活性氧可氧化降解糖蜜酒精废水.     

臭氧氧化优尼素红B-B染料废水及脱色动力学研究

研究了在鼓泡反应器中,臭氧氧化优尼素红B-B模拟染料废水在10~70℃范围内的脱色反应动力学.发现并解释了不同温度下出现的反应速率交叉现象,利用紫外可见分光光度法定量分析染料特征颜色(浓度)变化情况.结果表明,在不同温度下,表观脱色反应动力学都符合一级动力学规律,相关系数都达到了0.95以上.40℃下,反应速率常数为0.011 83 s~(-1),臭氧氧化脱色过程符合y=exp(0.521-0.014x+5.02×10~(-6)x~2)方程.随着温度的升高,臭氧在高温下氧化染料的反应速率小于臭氧的分解速率,低温时臭氧氧化的速率高于臭氧的分解速率,导致高温下氧化速率变慢.在40~50℃时,臭氧氧化优尼素红B-B染料废水脱色率最高,利用紫外可见分光光度法对氧化后废水进行分析,结果表明脱色率达到了99.5%.     

臭氧的制备与性质研究实验设计与实践

在自行研制的臭氧分流式供气实验装置上,以有机磷农药草甘膦为对象,设计了一套研究臭氧氧化性能的教学实验方案。实验内容包括臭氧发生量的测定、草甘膦降解产物正磷酸根离子的测定、草甘膦的转化率计算以及草甘膦转化率随氧化反应时间的变化曲线的绘制。通过实验,学生能深刻认识和掌握臭氧的氧化性能及其研究方法。该研究型实验设计新颖、实用,已经成功用于本科生环境化学教学实验。     

球形氧化铝负载锰基双金属氧化物催化剂催化臭氧深度氧化NO

在工业锅炉烟气处理领域,由于锅炉容量低,烟气温度往往无法满足传统选择性催化还原(SCR)所需温度窗口.工业锅炉烟气成分的复杂性也给氮氧化物治理带来了严峻考验.臭氧深度氧化NO结合湿法洗涤同时脱硫脱硝技术具有独特的应用优势.传统臭氧氧化技术中,NO被臭氧氧化为NO2,进而在脱硫塔中实现一体化脱硫脱硝.但由于NO2溶解度相对较低,需要在脱硫浆液中加入添加剂提高脱硝效率,造成运行成本增加.NO经臭氧深度氧化后,NO2进一步转化为溶解度高的N2O5,传统脱硫石膏浆液即可实现高效吸收N2O5,从而有效提高氮氧化物吸收效率.但由于N2O5生成反应速率低,深度氧化存在臭氧投入量大、反应时间长及臭氧残留多的缺点.臭氧耦合催化剂深度氧化NO可有效解决以上问题.首先,本文采用溶胶-凝胶法合成一系列单金属氧化物(Mn,Co,Ce,Fe,Cu,Cr)作为臭氧深度氧化NO的催化剂.结果发现锰氧化物表现出最高的催化活性,在70oC下,O3/NO摩尔比为2.0时经过0.12 s的反应时间催化剂即可实现80%以上的转化效率.但根据N2O5生成的总包反应(2NO+3O3=N2O5+3O2)可以看出,O3/NO摩尔比为1.5时即可实现N2O5的完全转化.由于催化臭氧氧化反应温度较低,中间产物在催化剂表面聚集,占据大量活性位,进而导致无法实现1.5摩尔比的高效转化.通过采用球形氧化铝作为载体,避免粉末状催化剂紧凑型布置,增加换热面积,可有效降低催化剂表面中间产物聚集;同时延长了气体与催化剂的接触时间,提高反应效率.在球形氧化铝载体上负载锰基双金属氧化物(Ce-Mn,Fe-M,Cr-Mn,Cu-Mn和Co-Mn),在初始NO浓度为410 mg/m3,反应温度100oC,O3/NO摩尔比1.5,催化反应时间0.12 s的工况下,催化剂最终实现95%(Fe-Mn)和88%(Ce-Mn)的转化效率,剩余NO和NO2的浓度分别低于20 mg/m3(Fe-Mn)和50 mg/m3(Ce-Mn),臭氧残留浓度低于25 mg/m3.同负载单一锰氧化物(83%转化率)相比,双金属氧化物进一步提高了N2O5生成效率.因此,臭氧耦合催化剂深度氧化NO结合湿法吸收在工业锅炉超低排放(NOx<50 mg/m3)领域具有广泛应用前景.通过XRD、氮气吸附、H2-TPR和XPS等手段研究了催化剂的晶体结构、孔结构参数、氧化还原性能和表面原子价态.催化臭氧深度氧化NO主要与催化剂对臭氧的分解性能和对NO的氧化性能有关.较大的比表面积和孔容有利于催化剂的吸附.氧空位有利于臭氧的吸附和分解.Mn4+和Mn3+的均衡分布既有利于NO的吸附氧化又有利于臭氧的吸附分解,最终提高了N2O5生成效率.     

臭氧催化氧化脱除低浓度甲醛的新方法

甲醛作为一种典型的室内挥发性有机污染物,对人体健康危害很大.目前,在可用于室内甲醛脱除的诸多方法之中,臭氧催化氧化法因可于室温下使用廉价的金属氧化物催化剂实现对甲醛的高效脱除,从而受到了科研工作者的广泛关注.然而,考虑到室内甲醛的浓度极低,且存在着长期缓慢释放的特点,传统的臭氧催化氧化法应用于实际的室内甲醛脱除不仅会造成能量的浪费,而且还易因未完全分解臭氧的连续释放带来二次污染问题.为了提高臭氧催化氧化脱除甲醛过程的臭氧利用率,降低能耗,并有效缓解未分解臭氧引起的二次污染,本文将一种循环的甲醛存储-臭氧催化氧化新方法应用于室内低浓度甲醛的脱除.该新方法包含甲醛存储与臭氧催化氧化两个过程,在存储阶段低浓度甲醛吸附存储于催化剂表面,而在臭氧催化氧化阶段臭氧将存储的甲醛氧化为CO2与H2O,并重新释放催化剂表面的吸附位.因负载型氧化锰具有优良的臭氧分解能力,本研究以Al2O3负载的MnOx为催化剂,通过研究前驱体及担载量对甲醛脱除反应的影响,筛选出了最优的MnOx/Al2O3催化剂,并对相对湿度的影响规律进行了考察,最后通过低浓度甲醛存储-臭氧催化氧化循环实验验证了该甲醛臭氧催化氧化新过程的可靠性.我们采用传统的等体积浸渍法,基于不同的前驱体制备MnOx/Al2O3催化剂.XRD表征结果表明,乙酸锰为前驱体制得的MA/Al2O3催化剂中MnOx相主要为Mn3O4(粒径约为6.0 nm);而硝酸锰前驱体所得MN/Al2O3催化剂中则含有MnO2与Mn2O3相,且其MnOx颗粒粒径较大,约为9.5 nm.XPS测试结果表明,MA/Al2O3催化剂含有Mn2+,Mn3+及Mn4+,其中Mn3+与Mn4+的含量分别为75%与12%;而MN/Al2O3催化剂则仅含有Mn3+与Mn4+,含量分别为35%与65%.上述XRD与XPS结果相一致,说明以乙酸锰为前驱体所得催化剂的分散度较高且易形成低氧化态的Mn.甲醛存储-臭氧催化氧化实验结果表明,与Al2O3及MN/Al2O3相比,MA/Al2O3催化剂具有更高的甲醛存储与催化氧化脱除性能.基于MA/Al2O3催化剂,不同Mn负载量下的甲醛存储与臭氧催化氧化实验结果表明,Mn负载量为10 wt%时MA/Al2O3的性能最佳.因而,进一步的实验中我们均选用最优的10 wt%MA/Al2O3为催化剂,其在50%相对湿度下的甲醛存储量为26.9μmol/mL,臭氧催化氧化阶段碳平衡为92%,CO2选择性为100%.相对湿度的影响结果(23℃)则表明,由于水分子与甲醛分子间存在着竞争吸附作用,甲醛存储容量随相对湿度的增加而降低;但因相对湿度增加可建立利于甲醛氧化的新途径,故臭氧催化氧化性能随相对湿度增加而增强.综合考虑,10 wt%MA/Al2O3上甲醛存储-臭氧催化氧化的最优相对湿度为50%.为验证所提出新方法的实用性,我们基于10 wt%MA/Al2O3开展了甲醛存储-臭氧催化氧化的4次循环实验.4次循环实验中的甲醛存储以及臭氧催化氧化处理的规律可基本保持一致.50%相对湿度下,低浓度甲醛(15×10-6)在空速为27000 h-1时的穿透时间为110 min,而在臭氧催化氧化阶段(150×10-6臭氧,空速15000 h-1)仅需约50 min即可实现对存储甲醛的氧化脱除(碳平衡大于92%,CO2选择性100%),表明该新方法较传统的臭氧催化氧化方法臭氧用量可节省60%.     

Fe2+/UV催化臭氧-曝气生物滤池降解腈纶废水研究

腈纶废水是一种难降解的有毒有机废水。本文采用Fe2+/UV催化臭氧-曝气生物滤池降解腈纶废水,探讨了臭氧浓度和紫外光辐射强度等影响因素对腈纶废水的COD去除效果的影响,并考察了紫外催化臭氧氧化单元和曝气生物滤池单元对COD去除的协同作用。结果表明,臭氧浓度对COD的去除率影响较大,臭氧浓度下降25%时,臭氧催化氧化和曝气生物滤池单元处理的COD去除率分别下降了12.53%和15.98%。紫外光强度对臭氧催化氧化单元的COD去除率影响较小,但对曝气生物滤池单元影响较大。臭氧催化氧化单元和曝气生物滤池单元COD去除率之比为1∶2,其协同作用使总出水COD值稳定在较低水平。     

REMOVAL AND RECOVERY OF DYESTUFFS FROM DYEING WASTEWATERS

The toxic nature of some dyestuffs (DSs) has long been recognized. Accordingly, dyeing wastewaters represent a source of water contamination, and should be treated in some way so as to reduce the concentration of the polluting DSs to permissible limits, prior to dumping its wastewater. In addition, some DSs can be recovered for reuse, a point which should represent saving in the overall cost of the dyeing process. Extensive publications on the removal of DSs from dye house wastewaters have been cited in the literature in which many techniques have been applied, biological treatment being the method most widely used as a primary treatment. However, only few publications have been concerned with recovery of DSs from their wastewaters. In the present paper, numerous techniques, if not all, that are presently used for either removal or recovery of DSs have been reviewed, evaluated and compared.     

Determination of Cotinine in Urine and Wastewaters by High Performance Liquid Chromatography Coupled with Tandem Mass-Spectrometric Detection

A technique of extracting cotinine in urine and wastewaters, followed by its quantitative determination, using high performance liquid chromatography combined with tandem mass-spectrometric detection is presented. The method is characterized by low detection limits and high levels of efficiency and sensitivity. The optimal conditions for the solid-phase extraction of cotinine from urine and wastewaters are found. This technique makes it possible to reliably estimate the content of cotinine in the urine of active and passive smokers and in wastewaters.     

Electrochemical treatment of slaughterhouse and dairy wastewater: Toward making a sustainable process

The industrial processing of meat and dairy production uses large amounts of fresh water, therefore, generates a significant volume of wastewaters. The treatment of these effluents has been performed using different technologies from biological to electrochemical advanced oxidation processes. Under the circular economy concept, the lack of available freshwater resources has increased the interest in reusing wastewater from slaughterhouses, and even in the recovering of by-products.This article reviews the application of electrochemical treatments to slaughterhouse and dairy wastewaters. In addition, an overview of added-value products and energy recovery from these industrial wastewaters is also presented with future perspectives.     

Adsorption of Cr(VI) on ureolytic mixed culture from biocatalytic calcification reactor

Ca-rich water and wastewater have caused problems in water use, wastewater reuse and the operations of reactors treating Ca-rich wastewater. Nowadays, reuse of wastewaters is fast gaining importance as water sources have been polluted. Therefore, the concept of biocatalytic calcification reactors (BCR) based on urea hydrolysis, pH increase and calcite production has been studied to remove Ca from wastewaters. This biological process produces significant amounts of waste sludge. In the present study, Cr(VI) adsorption on the ureolytic mixed culture (UMC) waste by-product from BCR was investigated to evaluate its potential for metal removal. The biosorption process was investigated using equilibrium batch tests and the data were fit to the Langmuir, Freundlich and Temkin isotherm models. The Cr(VI) ion concentration dependence of sorption (1-100 mg/L) could be fit to the Langmuir isotherm model. Monolayer adsorption capacity, qm (mg/g), of the adsorbent was 8.67 and the Langmuir constant b (L/mg) was 0.881. Based on the obtained results, the waste UMC appears to be a potential biosorbent for the removal of Cr(VI) from wastewater, although its adsorptive capacity is lower than those of other biosorbents.     

Sorption of heavy metal from aqueous solution by volcanic ash

Lava ash from Mt. Etna volcano has been tested in a series of batch experiments in order to find out its suitability to act as metal ion sorbent from wastewaters. The results show that the removal of Cd, Cu and Cr elements reaches a suitable level. Various experimental parameters have been tried to verify their influence on the metal sorption. Each ionic species in solution can be removed only in its own range of optimal pH. No competitive effects have been found. The equilibrium data are satisfactorily fitted by the Freundlich isotherm. Desorption experiments by acid aqueous solutions result in leaching of negligible amounts of metal ions.     

Application of boron-doped diamond electrodes for electrochemical oxidation of real wastewaters

Recently, the synthesis of boron-doped diamond electrodes on different substrates and shapes have reached a promising development stage. Now, these electrodes can also be effectively used to destroy toxic or biorefractory organics in real effluents, such as municipal wastewaters effluents, hospital wastewaters, groundwater, petrochemical effluent, wastewaters from agri–food activities, and so on. The results of this mini-review show that BDD is effectively even for such real effluents, allowing the removal of pollutants under several different conditions. Nevertheless, further efforts are necessary to reach a wider market; in particular, the next stages must face the optimization of cell design and the integration of the electrochemical system with other water treatment and renewable energy sources.     

On the Performance of Free Radicals Combined Electrocoagulation Treatment Processes

The electrocoagulation (EC) combined treatment processes have shown promising performances in which the removal of pollutants from industrial wastewater was greatly enhanced. The integration of a free radical producing step with EC has been considered as one of these new combinations that show synergy and improvements in the overall cleaning process performance. This review is devoted to discuss and analyze references on free radicals-assisted EC processes. Different combinations of free radical mechanisms were cited in the literature during the last two decades. They included ozone, advanced oxidation and ultrasound energy-assisted EC. It was noted that most of those studies were lab-scale processes that used synthetic wastewaters rather than real wastewaters. In addition the performances of those combined processes were improved compared to the EC process alone. This review considers the main parameters of free radical EC processes such as mechanisms, kinetic models, scale-up and cost estimation. Many concluding remarks were stated to give insights for possible future investigations. It seems from the results that the ozone-assisted EC is the most efficient combination since its removal efficiency is high in most applications. On the other hand, the combination of ultrasonic energy with EC was reported to reduce electrode passivation.     

Electricity Production and Characterization of High-Strength Industrial Wastewaters in Microbial Fuel Cell

Microbial fuel cells (MFCs) convert electrochemical energy into electrical energy immediately and have a big potential usage for the same time wastewater treatment and energy recovery via electro-active microorganisms. However, MFCs must be efficiently optimized due to its limitations such as high cost and low power production. Finding new materials to increase the cell performance and reduce cost for MFC anodes is mandatory. In the first step of this study, different inoculation sludges such as anaerobic gum industry wastewater, anaerobic brewery wastewater and anaerobic phosphate were tested, and MFC that was set up with anaerobic gum industry wastewater inoculation sludge exhibited the highest performance. In the second step of this study, various wastewaters such as chocolate industry, gum industry and slaughterhouse industry were investigated for anode bacteria sources. Several electrochemical techniques have been employed to elucidate how wastewaters affect the MFCs’ performance. Among all the mentioned wastewaters, the best performance was achieved by the MFCs fed with slaughterhouse wastewater; this device produced a maximum power density of 267 mW·m^?2.     

连续光催化净化染料废水放大实验的研究

本文设计研制了一套连续光催化净化染料废水的放大实验工艺流程并选用国产二氧化钛利用悬浮分散体系对染料酸性红G溶液和直接耐晒大红4BS工业废水进行连续降解。结果表明放大装置可使染料废水COD_cr降低并可脱色,催化剂能够良好分离并可回收再利用。     

Determination of heavy metals in industrial wastewaters and their influence on activated sludge biocenose

Radionuclide X-ray fluorescence method with a Si/Li semiconductor detector and²³⁸Pu exciting source was used in the determination of Cr, Fe, Ni, Cu, and Zn content in industrial wastewaters. Simultaneously, the effects of the wastewaters on activated sludge biocenose were evaluated.