2,4-二氯苯酚的电化学氧化降解反应研究

采用循环伏安法和原位红外光谱技术研究了2,4-二氯苯酚在Pt电极上的电化学氧化降解反应,结合Fukui函数值预测了2,4-二氯苯酚在电化学氧化过程中的反应位点. 结果表明,Pt电极对2,4-二氯苯酚有良好的电催化活性,2,4-二氯苯酚在电极表面反应主要有3个途径：直接通过电化学反应脱去氯离子,生成苯酚;在·OH的进攻下,C—Cl键断裂,4位Cl较2位Cl先脱去,生成苯二酚,并可进一步氧化生成苯醌以及不饱和羧酸;在·OH的进攻下发生苯环开环反应,生成含氯不饱和羧酸. 在1700 mV左右,2,4-二氯苯酚可经电化学氧化生成CO₂.     

Degradation of organic pollutants by visible light synergistic electro-Fenton oxidation process

Visible light irradiation combined with homogeneous iron and/or hydrogen peroxide to degrade organic dye rhodamine B (RhB) and small molecular compound 2,4-dichlorophenol (2,4-DCP) in a home-made bottle reactor was assessed. The concen-tration of oxidize species, Fe3+ and Fe2+ were determined during the degradation process. The results demonstrated that visible light irradiation combined with electro-Fenton improved the degradation efficiency. Moreover, both RhB and 2,4-DCP were mineralized during visible light synergistic electro-Fenton oxidation process. 95.0% TOC (total organic carbon) removal rate of RhB occurred after 90 min and 96.7% of COD (chemical oxygen demand) removal rate after 65 min of irradiation. 91.3% TOC removal rate of 2,4-DCP occurred after 16 h of irradiation and 99.9% COD removal rate occurred after 12 h of illumination. The degradation and oxidation process was dominated by the hydroxyl radical ( · OH) generated in the system. Both the impressed electricity and dye sensitization by visible light facilitated the conversion between Fe3+ and Fe 2+ , thus, improving Fenton reaction efficiency.     

新型复合电极与偶氮染料分子的氧化降解反应的研究

介绍了具有合成H_2O_2和光催化性能的双功能型复合电极、双功能复合电极是 将TiO_2/C光催化剂负载在具有合成H_2O_2性能的新型载体上形成的。在光反应器 中,复合电极作阴极,钌-钛不溶性电极作阳极,低压汞灯作光源,实现了光化学 氧化与光催化氧化在同一电极/溶液界面上的联合作用。当反应器工作时,复合电 极中的TiO_2/C光催化层表面进行着光催化反应,在载体的三相界面上进行着O_2的 2电子H_2O_2的电化学反应,电流效率达82%（J = 15 mA/cm~2）,为·OH自由基的 生成提供了物质源,而且氧的2电子还原反应电位使其表面的TiO_2获得相对于平带 电位约+0.5 V的阳极偏压,改善了TiO_2的光催化活性。实验结果表明,复合电极 对提高偶氮染料分子活性艳红（K-2BP）的氧化降解速度起了重要作用。实验发现 偶氮染料分子在复合电极表面的吸附量与反应速度密切相关。文中讨论了复合电极 的作用原理及偶氮染料分子的氧化降解过程。     

Indirect electrochemical oxidation of aliphatic alcohols to carboxylic acids by active oxygen forms in aqueous media

Indirect electrochemical oxidation of aliphatic alcohols (butanol, hexanol, nonanol, decanol) to the corresponding carboxylic acids by active oxygen forms (AOFs) generated in situ in electrochemical cells from O₂, H₂O₂, H₂O is carried out in aqueous electrolyte using anodes of lead dioxide, a nickel oxide electrode, and boron-doped diamond electrode (BDDE). It is found that selectivity of the process of indirect electrosynthesis of carboxylic acids depends on the chemical nature of the anode material and structure of the initial alcohol and is determined by the conditions of AOF generation. Coupled electrosynthesis with simultaneous in situ generation of AOFs on the cathode and anode occurs more effectively with formation of the corresponding carboxylic acids.     

空气电极/AC作载体对TiO2光催化性能的影响

The photo catalytic degradation of activated red in the aqueous solution was studied using TiO2 supported on air electrode and active carbon (AC) as photo catalysts. It was found that the photo catalytic reaction rate of TiO2 was obviously increased by the presence of air electrode and AC supported. The air electrode which has functions of synthesizing H2O2 in situ and photocatalysis was reported. The results also implied that biasing of the electrode at +0.5V led to efficient charge separation. The current density of air (oxygen) electrode had effect on the oxidation rate of azo dye molecule, i=15 mA/cm2, and the rate could reach maximum. With AC mass fraction of about 21% the oxidation rate for TiO2/AC was obviously larger than that for TiO2, but the result was contrary to this for higher AC mass fraction (>30%). The experiment results showed that because TiO2 was supported on active carbon, the effective surface area of the photo catalysis and their absorbability for organic molecules can be increased. The pH in solution had effect on the oxidation rate of organic molecules.     

电聚合制备聚苯胺@石墨毡复合电极及其在电芬顿过程中的高效电催化性能

作为一种高级氧化技术(AOPs),芬顿氧化法(Fenton)因其操作简单、绿色高效而备受关注.其基本原理是Fe2+催化H2O2产生的羟基自由基(?OH)进攻有机物使之降解为无机小分子或盐.电芬顿法(Electro-Fenton,E-Fenton)是利用电化学方法原位生成H2O2的Fenton衍生法,其优点在于不需要从外界加入H2O2、高效节能、无选择性、并且易于和其他处理技术耦合,是一种非常有价值和应用前景的新型水处理技术.电芬顿技术的理论探究和工艺优化,是当今高级氧化技术的理论和实践研究的重要内容.E-Fenton过程的关键步骤是阴极材料上氧还原反应(Oxygen reduction reaction,ORR)持续生成H2O2.由于析氢过电位高、稳定性好、性能优异,碳材料成为ORR反应最常用的电催化阴极材料.石墨毡作为一种三维多孔立体材料,具有电化学活性面积大、传质好、导电性强、价格低等优点,是ORR的理想阴极材料.聚苯胺材料作为一种导电高分子材料,价格便宜、加工性好、且含有丰富的N原子,在基础研究和实际应用领域都十分活跃.我们创新性地采用电聚合的方法合成了聚苯胺@石墨毡(PANI@GF)复合电极,并通过降解邻苯二甲酸二甲酯(dimethyl phthalate,DMP)研究了其在电芬顿过程中的电催化性能.通过扫描电镜、X射线光电子能谱分析对电极表面结构和杂原子掺杂性进行了物化表征.结果显示PANI@GF复合电极同时具有宏观和微观的三维多孔结构,这种结构蓬松的多孔结构为氧气提供了合适的传递通道和足够的反应面积.所制备复合电极中N原子含量约为1.9%,且吡啶N和吡咯N的含量相对较高.这些N原子来自聚苯胺分子中含有的大量N原子,并能够促进ORR反应.石墨毡和聚苯胺两种材料的在结构和组分上的特点,使得PANI@GF复合电极具有优异的电芬顿降解DMP的性能.在DMP浓度为50 mg/L、电位0.5 V(vs.SCE)、氧气流速为0.4 L/min的条件下,其DMP降解反应表观动力学常数达0.0753 min-1,是石墨毡电极表观动力学常数(0.0151 min-1)的5倍.PANI@GF复合电极制备的最优聚合时间和碳化温度分别为1 h和900℃.这是因为聚合时间太长,可能导致聚苯胺层厚度大,微孔结构被堵塞,进而降低了反应活性面积和影响氧气传质效果,使得电极性能下降;而聚合时间太短,可能导致电极复合不充分.高温碳化可以使石墨毡表面聚苯胺层形成更多的孔结构,从而有利于ORR过程.DMP降解过程中氧气流速、Fe2+用量以及pH值等工艺条件对电极性能有一定的影响,结果表明其相应的优化值分别为0.4 L/min、1.0 mmol/L和3.0.当氧气流速过低时,溶液中低浓度的溶解氧使ORR过程受传质过程限制,导致电极不能充分反应;当氧气流速过大时,并不会增加已经达到饱和的溶液中的氧气浓度,而过大的氧气速率会冲击电极表面,降低电极稳定性而影响其催化性能.对Fe2+.用量而言,E-Fenton过程有多种Fe循环途径,不同的铁含量对于电极性能影响不明显.因此,1.0 mmol/L的Fe含量足够满足实验需要.pH值对E-Fenton过程至关重要,pH较高时,铁离子会形成配合物,阻碍铁循环,并且会导致H2O2的分解,从而降低电极DMP降解性能;而当pH太低时,较多的酸增加成本,且需要后续处理过程以消除酸的影响.实验结果表明3.0是最优pH值,与传统Fenton方法的最适pH相符.PANI@GF复合电极具有高效催化降解DMP的能力,在电芬顿技术处理有机废水中有潜在应用.     

金属钯纳米颗粒/氮化钛复合材料对水中2,4-二氯苯酚的电催化氢化脱氯（英文）

随着社会经济的快速发展,含氯有机物,特别是含氯苯系物,在农业、化工和医药等领域的使用量逐年增多,而使用过程中不合理的排放和控制致使含氯苯系物对生态环境,特别是水体环境的污染日趋严重.含氯苯系物具有高致毒致癌性,易生物富集,且很难被完全降解矿化,已被国家环保局认定为优先控制污染物.常规的废水处理工艺,如吸附、氧化及生物降解等,效率不高,且具有二次污染风险.电催化氢化脱氯技术是一种新型特别针对废水中含氯有机污染物的处理工艺,是通过在阴极电解还原水,原位生成原子态氢,以进攻苯环上C.Cl键,通过C.Cl键断裂H原子取代,使含氯苯系物完全转化为苯系物,达到去毒去害化的目的,近年来越来越受到研究者的关注.在整个电催化氢化脱氯技术中,高效稳定的电催化剂合成是关键,决定着脱氯效率、脱氯动力学、产物选择性及能量的利用率.本文报道了一种简易、无需添加任何表面活性剂的湿式还原法制备金属钯/氮化钛(Pd/TiN)和金属钯/碳(Pd/C)复合材料.在该复合材料中,金属钯颗粒具有均一的纳米尺寸(约5.0 nm)和球状形貌,且均匀分布在TiN和C载体上.作为针对水体中代表性含氯苯系物2,4-二氯苯酚的电催化氢化脱氯反应催化剂,Pd/TiN所展现的活性和稳定性均优于TiN和Pd/C,这源于TiN载体的促进作用.当TiN与Pd复合时,相应形成的Pd-TiN界面可改变Pd表面的电子结构,进一步优化Pd产活性氢及其吸附活化2,4-二氯苯酚的性能,因而其催化氢化脱氯活性增加.阴极工作电压是该催化反应中一个重要操作参数,决定了电催化氢化脱氯的效率和最终产物的构成.实验表明,.0.80 V vs Ag/AgCl是最佳操作电压,此时2,4-二氯苯酚的电催化氢化脱氯效率最高,可达到93.27%,且可实现最大程度的2,4-二氯苯酚向苯酚转化.脱氯反应路径研究发现,在Pd/TiN催化剂上2,4-二氯苯酚脱氯反应路径为2,4-二氯苯酚→对位一氯苯酚,邻位一氯苯酚→苯酚,但Pd/TiN对邻位和对位的C.Cl键断裂基本没有选择性.本文提供了一种新的有效调控Pd材料电催化氢化脱氯性能的方法,可望用于其他氢化反应体系的高效催化剂的设计合成,同时可推动电催化氢化脱氯技术在环境污染修复中的应用.     

F-和Fe3+掺杂对Ti基PbO2阳极性能的影响

采用热分解-电镀法制备了Ti基PbO2,阳极(Ti/PbO2),F-掺杂PbO2阳极(Ti/F-PbO2),Fe3+掺杂PbO2阳极(TiP/Fe-PbO2)和F-,Fe3+共掺杂PbO2,阳极(Ti/F-Fe-PbO2).采用XRD和EDX测试对电极进行了表征,应用加速电解寿命测试和电催化降解4-氯苯酚(4-CP)污水,考察了F-掺杂,Fe3+掺杂和F-,Fe3+共掺杂对PbO2阳极稳定性及电催化活性的影响.结果表明,Ti/F-PbO2和Ti/FePbO2阳极有相近的电催化降解活性,但与Fe3+掺杂相比,F-掺杂大大提高了PbO2阳极的加速电解寿命.对Ti/F-Fe-PbO2阳极,Fe3+掺杂改善了其导电性能.同时F-掺杂提高了阳极的稳定性能,使其有较长的电解寿命.与Ti/PbO2,Ti/F-PbO2和Ti/Fe-PbO2阳极相比,Ti/F-Fe-PbO2阳极的电催化降解活性显著提高,这不仅与其导电性能的改善有关,更与F-掺杂和Fe3+掺杂对4-CP降解的表面协同作用有关.     

TiO2的低温制备及其对有毒有机污染物的降解

溶胶水热法制备了TiO₂粉末,用X射线衍射仪(XRD)、比表面积及孔径分析仪(BET)和透射电镜(TEM)对TiO₂进行了初步表征,结果显示:纳米TiO₂主要为锐钛矿相(含板钛矿相(121)),比表面积为106.2 m²/g.在紫外光(λ≤387 nm)照射条件下,以有机染料罗丹明B(Rhodamine B,RhB)和无色小分子2,4-二氯苯酚(2,4-dichlorophenol,2,4-DCP)的紫外光(λ≤387 nm)光催化降解试验为探针反应,低温(50℃)下制备的TiO₂粉末具有较高光催化活性,对RhB和2,4-DCP有较好的降解效果.通过分析紫外-可见光谱(UV-Vis)、红外光谱(FTIR)和总有机碳(TOC)测定,发现TiO₂/UV体系能使RhB和2,4-DCP发生有效的降解,反应5 h后RhB和7 h后2,4-DCP的矿化率分别达到81.2%和86.8%.同时,采用辣根过氧化物酶(POD)、N,N-二乙基对苯二胺(DPD)分光光度法和苯甲酸荧光光度法分别测定了在降解过程中H₂O₂和羟基自由基(.OH)的变化,表明TiO₂光催化机理涉及到.OH历程.     

钌-钯掺杂Ti/TiO2阳极电催化降解甲基橙研究

以偶氮染料甲基橙为处理对象, 分别考察了Ru, Pd及Ru-Pd掺杂的Ti/TiO2阳极的光、电催化活性, 并与Ti/RuOx-PdO阳极的电催化活性进行了比较; 利用XPS分析了Ru-Pd掺杂的Ti/TiO2阳极表面Ru, Pd及Ti的化学形态. 实验发现, Ru, Pd及Ru-Pd掺杂的Ti/TiO2阳极的光催化活性都有所降低, 而其电催化活性却都有大幅提升, 特别是Ru-Pd掺杂的Ti/TiO2阳极, 其电催化活性明显地优于Ti/RuOx-PdO阳极. XPS分析表明, Ru-Pd掺杂的Ti/TiO2阳极其光、电催化活性的变化可能与该阳极表面Ru, Pd及Ti的化学形态变化有关.     

新型复合电极对偶氮染料分子的光催化降解

介绍了具有合成H2O2和光催化性能的双功能新型复合电极,并用X射线衍射、扫描电镜等方法进行了表征.双功能复合电极是将TiO2光催化剂负载在活性碳(AC)和具有合成H2O2性能的新型载体空气电极上形成的.在复合电极作阴极的光反应器中,* OH和TiO2光催化剂的存在实现了光化学氧化与光催化氧化在同一电极/溶液界面上的联合作用.实验结果表明,复合电极对提高偶氮染料分子活性艳红(K-2BP)的氧化降解速度起了重要作用,仅反应3 min,脱色率可达49%;反应80 min,偶氮染料分子COD去除率可达47%.     

Electrochemical water oxidation by photo-deposited cobalt-based catalyst on a nano-structured TiO2 electrode

A cobalt-based catalyst was directly photo-deposited on the surface of a widely used n-type nano-structured semiconductor(TiO 2).Different thicknesses of the TiO 2 films as well as different time of photo-deposition of the Co-based catalyst on TiO 2 films have been optimized.It was found that the electrode with 3 layers of TiO 2 film(in 8 m thickness) and 1 hour photo-deposition of the cobalt-based catalyst by light irradiation from a 500 W Xenon lamp gave the highest current density(～5 mA/cm 2).Using this cobalt-modified TiO 2 film as a working electrode in an electrochemical device,highly efficient water oxidation has been demonstrated in a pH 7.0 aqueous solution with low overpotential.     

Destruction of cyanide in aqueous waste by electrochemical oxidation

A laboratory study was carried out by electrochemical oxidation to destroy cyanide in aqueous waste. The electrode used in this study was a triple oxide coated titanium based mesh type anode and a carbon cathode. Direct and indirect methods were both carried out at alkaline conditions and indirect oxidation method in the presence of chloride was found to be more efficient.     

Electrochemical oxidation of chlorinated benzenes

The electrochemical oxidation of benzene and its chloro derivatives (n=1–3) has been studied in acetonitrile, water, and an aqueous emulsion at both metallic electrodes and dimensionally stable anodes. In acetonitrile all substrates underwent a six-electron oxidation near +3 V versus the standard hydrogen electrode. Low yields of organic products, principally phenols, were obtained; electrochemical combustion to CO₂ was a major reaction pathway, but current efficiencies were low.     

The removal of chlorinated organic herbicide in water by gamma-irradiation

In this study, the radiation-induced degradation of 2,4-dichlorophenoxyacetic acid (2,4-D) herbicide in aqueous solution was studied under various conditions as a function of irradiation dose in the absence and presence of hydrogen peroxide. The obtained data confirmed that largest yield of radiolytic degradation is obtained in oxidation processes/ionizing radiation, where oxidation is carried out with hydroxyl radicals. For complete degradation of 50?ppm 2,4-D, a required dose was lower in the presence of hydrogen peroxide. The formed major toxic phenolic intermediates were 2,4-dichlorophenol (2,4-DCP) and 4-chlorophenol (4-CP). The chemical analysis of the 2,4-D and the intermediates resulted from the radiolytic degradation were performed using a gas chromatography associated to mass spectrometry (GC?CMS) with ion trap dedector (ITD) and ion chromatography (IC). The formation of chlorophenols in addition to chloride, formaldehyde and carboxylic acids was studied as a function of absorbed dose.     

A comparative study on direct and indirect electrochemical oxidation of polyaromatic compounds

This study has been performed to investigate the treatment of an industrial wastewater containing naphthalene- and anthraquinone-sulfonic acids, by direct and indirect electrolyses. The direct electrochemical oxidation has been carried out using boron-doped diamond and lead dioxide anodes, while the indirect electrolyses has been mediated by active chlorine electrogenerated on a platinum anode, or by hydrogen peroxide electrogenerated on a graphite felt cathode. For each type of electrolyses the effects of operating parameters, such as anode material, current density, chloride concentration, ferrous ions concentrations have been also investigated. Measurements of Chemical Oxygen Demand (COD) and colour fading have been used to compare the results of different electrolyses. Experimental data showed that the complete COD and colour removals have been obtained only by direct oxidation or by active chlorine mediated electrolyses. On the contrary using electrogenerated hydrogen peroxide the solution has been presented a residual COD and colour. In particular, it found that faster oxidation rate has been obtained by direct oxidation using a boron-doped diamond anodes at low current density.     

应用于水溶液介质中喹啉氧化的电芬顿工艺实验设计方法(英文)

采用碳毡阴极和铂阳极的电芬顿工艺研究了喹啉模型分子8-羟基喹啉硫酸盐（8-HQS）在水溶液介质中的降解行为. 由于电化学诱导芬顿药剂（H2O2,Fe2+）产生大量的羟基活性基（OH）,成为与有机物发生反应直到有机物完全矿化的强有力氧化剂,因此,电芬顿工艺具有很强的氧化能力. 采用正交实验设计确定了水溶液介质中8-HQS降解的操作参数. 结果表明,电流密度和8-HQS的初始浓度是影响降解速度的主要因素. 8-HQS浓度随着电解时间而减少,说明8-HQS的氧化遵循准一级反应动力学. 通过竞争动力学方法确定的由OH引起8-HQS氧化的绝对反应速度常数为1.62×109 mol^-1·L·s^-1. 通过Doehlert 矩阵研究了8-HQS矿化的最佳实验参数,由此确定最佳条件下电芬顿工艺能导致8-HQS在水溶液中的准完全矿化（总有机成分去除率95%）. 对8-HQS水溶液的处理,使得8-HQS矿化前的最终产物为短链羧酸. 同时研究了电芬顿处理中短链羧酸的演变行为. 溶液毒性演变的跟踪研究发现,中间产物的毒性比8-HQS强,但溶液的毒性在中间产物矿化后可以完全消除.     

Fe2O3/TiO2纳米管的制备及其光电催化降解染料废水性能

采用阴极电沉积和阳极氧化法制备了Fe2O3改性TiO2纳米管(Fe2O3/TiO2-NTs)电极,运用场发射扫描电子显微镜、透射电子显微镜、X射线衍射和紫外-可见漫反射光谱等手段对其进行了表征,考察了其光电化学性能,并研究了复合电极光电催化降解甲基橙染料废水的反应性能.结果表明,Fe2O3的负载成功地将TiO2-NTs的光响应区间拓宽到可见光区域,Fe2O3/TiO2-NTs复合电极的光电流密度达到TiO2-NTs电极的3倍.在光电催化反应中,Fe2O3/TiO2-NTs复合电极对甲基橙的脱色效果明显优于TiO2-NTs电极,以Fe2O3/TiO2-NTs为阳极,光照5min,甲基橙溶液的脱色率可达90%以上.     

利用钐掺杂的氧化铈夹层提高燃料电池阳极的活性

考察了Ni-钐掺杂的氧化铈(Ni-SDC)复合阳极与La0.9Sr0.1Ga0.8Mg0.2O3(LSGM)电解质中间加入的SDC 中间层对阳极及整个电池性能的影响.结果表明，SDC中间层的加入显著减小了阳极极化过电位，但同时引入了欧姆降，降低了电池的功率输出密度.氢在Ni-SDC电极的氧化主要由两个过程控制，分别对应于交流阻抗谱的两个阻抗半圆，高频环随着SDC中间层的加入显著减小，可能对应于H2在Ni-SDC/SDC/H2三相界的电化学氧化或氧从LSGM向SDC的传输，低频环与SDC中间层无关，可能对应于氢在电极表面的解离吸附及吸附物种的扩散过程.使用Ni-SDC/SDC夹层阳极可以明显地提高电池的稳定性.     

Reductive dechlorination of 2,4-dichlorophenol using nanoscale Fe~0: influencing factors and possible mechanism

Nanoscale Fe0 was synthesized through a reductive method in this paper. The experiments were per-formed to investigate the reduction of 2,4-dichlorophenol (2,4-DCP) by nanoscale Fe0 under different conditions. The pathways for the reduction of 2,4-DCP by nanoscale Fe0 were discussed. Batch studies demonstrated that the mechanism includes adsorption, dechlorination and cleavage of the benzene ring. Dechlorination, which occurs after 2,4-DCP molecule is adsorbed on the interface of Fe particle, is an interfacial reaction. One or two chlorine atom can be removed from 2,4-DCP to form 2-chlorophenol, 4-chlorophenol or phenol. As the concentration of 2,4-DCP increased, the relative dechlorination ratio decreased. However, the reduced quantities of 2,4-DCP increased. Temperature can influence dechlo-rination rate and pathway. Dechlorination is prior to cleavage of the benzene ring at a higher tempera-ture, but at a lower temperature, adsorption may be the main pathway, and cleavage of the benzene ring may be prior to dechlorination.