碳纳米管电极原位产生过氧化氢及其对亚甲基蓝脱色效果

将碳纳米管固定化制成多孔疏水性导电薄膜构建电化学阴极还原体系，实现过氧化氢在阴极的原位产生。电极特性研究表明，电极在较宽的电压范围内均具有较好的活性。考察了阴极电位、电极成分、氧气流量和电解质浓度对过氧化氢原位产生的影响，在优化条件下经过120min后过氧化氢达到66．17mg／L，并探讨过氧化氢原位产生的机理。在此基础上考察原位过氧化氢氧化工艺下对亚甲基蓝的脱色效果，并分析其脱色机理。     

活性黑KN-B染料模拟废水电化学脱色

为进一步明确活性染料在可溶性阳极电化学体系中的脱色机理，以铝为牺牲阳极，不锈钢为阴极，在恒电流操作模式下，针对活性黑KN-B模拟废水，考察了电流密度、初始pH值、电解质种类及浓度、温度、染料浓度因素对染料脱色过程的影响。结果表明：(1)电流密度、电解液初始pH值、氯化钠电解质浓度、温度、染料浓度对染料溶液脱色效率影响显著，在一定实验条件下，染料溶液脱色率可达到88%；(2) 在不同pH的范围内，活性黑KN-B表现的脱色机理不同，pH 4～9为混凝与阴极还原脱色共同作用；pH＜4和＞9则表现为阴极还原脱色为主； (3) 氯化钠的加入在增强染料脱色的同时，也有助于芳环类物质的后续混凝去除。     

隔膜槽中ACF电极成对电解脱色活性艳蓝KN-R

同时以活性炭纤维(ACF)为阳极和阴极,在隔膜电解槽中研究了不同电流密度下蒽醌染料活性艳蓝KN-R的电化学脱色.考察了ACF阳极和ACF阴极各自对染料的脱色性能.结果表明,当电流密度为1.0～1.5 mA/cm2时,电解槽中发生阳极电氧化和阴极电还原同时进行的成对电解脱色.在ACF电极上,活性艳蓝KN-R的电氧化脱色比电还原脱色容易进行,1.0 mA/cm2时,阴阳两极室脱色率分别为69%和93%,而1.5 mA/cm2时,阳极室脱色率保持在93%,阴极室脱色率达到79%.     

铁阳极电凝聚处理活性黑KN-B染料废水

对铁阳极电凝聚处理活性黑KN-B染料废水过程进行了实验研究.考察了电流密度、染料溶液初始pH值、电介质浓度及种类、温度、染料浓度等因素对脱色效率的影响.结果表明,在一定实验条件下,活性黑KN-B模拟废水的脱色效率达93%;电流强度、染料浓度、电解液初始pH值及电解质的种类对染料溶液脱色效率影响显著,电解液温度、电解质的浓度对脱色效率的影响不明显;以铁为阳极的原位电凝聚处理活性黑KN-B模拟废水混凝过程中主要作用机理以吸附电性中和为主;电凝聚过程中活性黑KN-B在阴极上发生了还原反应.     

石墨烯泡沫包裹铁电极的制备及其在电解脱色染料中的应用研究

通过水热还原氧化石墨烯在铁电极表面原位生长石墨烯泡沫的方法制得了石墨烯泡沫包裹铁电极(GS-Fe电极),并将其应用于多种染料的电解脱色。结果表明:在相同电流密度下,GS-Fe电极的电解反应速率常数是铁电极的5倍;加入电解质对电解效率至关重要,其中NaCl是最有效的电解质;对甲烯蓝而言,最佳的电解条件为甲烯蓝初始质量浓度30mg/L、pH 5~7;GS-Fe电极可用于电解脱色刚果红、酸性蓝92和活性蓝R。电解脱色的机制推测主要为间接氧化,Cl~-被氧化成ClO~-,而后ClO~-氧化染料。GS-Fe电极可通过简单清洗再生,电解的脱色率几乎不受影响。     

PTFE/C三相电极氧阴极还原法生产过氧化氢

设计了隔膜体系电解槽,制作了聚四氟乙烯(PTFE)/碳黑三相气体扩散电极,系统研究了隔膜、电流密度、电极间距、初始溶液酸度、电解质、空气量和时间等因素对过氧化氢累积产生浓度和电流效率的影响。结果表明,在有隔膜体系,电流密度为70 m A/cm2,电极间距为1 cm,初始p H=0.5,电解质为0.10 mol/L Na2SO4溶液,空气量为40 m L/min的条件下,电解时间1 h时过氧化氢累积浓度最高可至20 096.05 mg/L,此时对应的电流效率为63.37%。在确定的最佳条件下,进行电解液循环实验,1 h时电流效率升高到98.4%,12 h之后,过氧化氢累积浓度为46 042.43 mg/L。实验原位产生的高浓度酸性过氧化氢溶液可以直接应用于Fenton试剂。     

石墨棒阳极电化学氧化降解甲基橙

以石墨棒为阳极,采用电化学氧化法降解水溶液中甲基橙。通过紫外可见光谱和HPLC分析初步鉴定了甲基橙降解过程中的部分中间产物;通过硝酸银滴定法证明了使用的支持电解质氯化钠能参与并促进氮氮双键和苯环的破坏;通过紫外可见光谱、COD的变化考察了电解质的种类及浓度、电极种类、修饰及形状、槽电压和酸碱度等参数对石墨棒阳极降解甲基橙能力的影响。实验结果表明,以石墨棒为阳极、以石墨棒或者铜环为阴极组成的二维电极体系,和以石墨棒为阳极、以铜环为阴极并填充活性炭组成的三维电极体系,在氯化钠水溶液中均能有效降解甲基橙,20 min后脱色率超过95%,3 h后COD去除率超过90%。     

AC/PTFE微生物燃料电池阴极去除罗丹明B及同步产电性能

采用辊压成型法制备了活性炭(AC)/聚四氟乙烯(PTFE)质量比分别为6、5和3的AC/PTFE电极,并利用SEM对电极表面进行表征。结果表明,随着质量比的降低电极表面活性炭颗粒间的连接更为紧密。以制得的AC/PTFE电极,碳毡分别为微生物燃料电池(MFC)的阴极、阳极,利用AC/PTFE阴极在曝气条件下产生的过氧化氢在阴极处理模拟的罗丹明B废水。研究了不同质量比AC/PTFE阴极对罗丹明B的去除效果及同步产电情况,结果表明以AC/PTFE质量比为6的AC/PTFE阴极在96 h内对罗丹明B的去除率达到96%,MFC获得的最大功率密度为105 mW·m~(-2);同时研究了在阴极液加入0.2 g·L-1Fe~(2+)的条件下,阴极液为不同pH值时,阴极对罗丹明B的去除效果及MFC产电情况。结果表明在阴极液pH=3的情况下,罗丹明B的去除率在36 h内达到了98.9%,MFC的最大功率密度达到210 mW·m~(-2),罗丹明B的去除速率及MFC能量的输出得到了明显提高。     

开放静置体系中白地霉Y1对染料脱色降解研究

采用白地霉Y1对染料进行脱色，考察了染料初始浓度、接种量、pH值、C/N比和温度等因素对白地霉降解溴酚蓝的影响，并对其降解机理进行了探讨。实验结果表明：白地霉能在开放静置条件下对部分染料进行有效的脱色，对溴酚蓝尤其有效。开放静置体系下，白地霉能对300 mg/L的溴酚蓝进行脱色，脱色pH和温度分别为2～8、25～40℃，高碳低氮环境中更有利于脱色，接种量对染料脱色影响不大。通过对胞外液絮凝及脱色作用、葡萄糖代谢情况及染料脱色扫描图谱分析表明，白地霉主要通过分泌胞外液对溴酚蓝进行作用，且能对溴酚蓝有效降解。     

电絮凝处理牛仔布印染废水

用铁分别作为电絮凝反应系统的阴极和阳极,研究电絮凝法对牛仔布印染废水的处理效果。考察了电极电压、反应时间和pH等因素对电絮凝法去除实验所用废水中COD和色度效果的影响。结果表明,电极电压和反应时间是主要的影响因素,pH次之。电极电压24 V,反应时间35 min,pH为7.4时,脱色率可达99%,COD去除率在70%左右,处理效果最佳。因此,电絮凝法可以作为印染废水的预处理工艺,有效降低废水COD和色度。     

Mechanism and kinetic model for the decolorization of the azo dye Reactive Black 5 by hydrogen peroxide and UV radiation

A kinetic model for the decolorization of C.I. Reactive Black 5 by the combination of hydrogen peroxide and UV radiation was developed based on experimental results and known chemical and photochemical reactions. The observed kinetic reaction coefficient was determined and correlated as a function of hydrogen peroxide concentration and UV intensity. The validity of the rate expression was tested experimentally in a parameterization study. The decolorization rate follows pseudo-first order kinetics with respect to dye concentration. The rate increases linearly with UV intensity and nonlinearly with increasing hydrogen peroxide concentration, going from a linear relationship at low H(2)O(2) concentrations to a maximum as hydrogen peroxide concentration continues to increase. The decolorization rate expression derived from the proposed reaction mechanism was reconciled with that used for correlating the experimental data.     

类Fenton反应对偶氮染料橙黄II的脱色研究

以橙黄II染料溶液为研究对象,通过正交实验确定了Fe-NTA/H2O2构成的类Fenton反应中各影响因子的最佳操作条件为:[H2O2]=20 mmol/L,[Fe-NTA]=2.5 mmol/L,pH=3。同时考察了反应时间、溶液pH值、H2O2浓度、Fe-NTA浓度对脱色效率的影响。实验表明脱色反应在30 m in内基本完成,类Fenton试剂能在较宽的pH范围内保持较好的脱色效果,而且在pH=6时,类Fenton试剂比传统Fenton试剂的脱色效率提高约75%。增加双氧水浓度可以提高橙黄II溶液脱色率,但超过20 mmol/L后效果提高不明显。在0.5~2.5 mmol/L的范围内,Fe-NTA浓度对脱色效果的影响不显著。     

Decolorization of structurally different synthetic dyes using cobalt(II)/ascorbic acid/hydrogen peroxide system

The cobalt(II)/ascorbic acid/hydrogen peroxide system was used for decolorization of azo, acridine, anthraquinone, thiazine and triphenylmethane dyes. More than 90% decolorization was obtained with all dyes except Remazol Brilliant Blue R (75%). With other transition metals the system was less efficient. With copper, higher concentration and prolonged incubation time was necessary to obtain the same extent of decolorization. The rate of decolorizaton was not affected by pH in the range of 3-9. The reaction is very fast, with more than 90% decolorization being attained within 15 min. The system produces hydroxyl radicals which are responsible for the decolorization.     

Treatment of polychlorinated biphenyls in two surface soils using catalyzed H₂O₂ propagations

Two surface soils contaminated with polychlorinated biphenyls (PCBs) collected from Superfund sites in the New England region of the United States, Fletcher Paints and Merrimack Industrial Metals, were evaluated for field treatment at the bench level using catalyzed H₂O₂ propagations (CHP—modified Fenton’s reagent). The two soils were first evaluated for the potential for in situ treatment based on two criteria: (1) temperature (<40 °C after CHP reagent addition), and (2) hydrogen peroxide longevity (>24 h). In situ CHP remediation was more applicable to the Fletcher soil, while the Merrimack soil was better suited to ex situ treatment based on temperature increases and hydrogen peroxide lifetimes. Using the highest hydrogen peroxide concentrations appropriate for in situ treatment in each soil, PCB destruction was 94% in the Fletcher soil but only 48% in the Merrimack soil. However, 98% PCB destruction was achieved in the Merrimack soil using conditions more applicable to ex situ treatment (higher hydrogen peroxide concentrations with temperatures >40 °C). Analysis of degradation products by gas chromatography/mass spectroscopy showed no detectable chlorinated degradation products, suggesting that the products of PCB oxidation were rapidly dechlorinated and degraded. The results of this research document that the two PCB-contaminated soils studied can be effectively treated using aggressive CHP conditions, and that such a detailed bench study provides important information before implementing field treatment.     

菱铁矿催化过氧化氢-过硫酸钠修复地下水中1,2-二氯乙烷污染

采用菱铁矿催化过氧化氢-过硫酸钠双氧化剂体系去除地下水中的1,2-二氯乙烷,通过研究菱铁矿催化机理以及氧化剂浓度两方面探讨双氧体系较单氧体系有较高去除率的原因,探讨了双氧体系1,2-DCA降解动力学和氯离子平衡。研究结果表明,菱铁矿催化双氧体系可以有效去除溶液中的1,2-DCA,本体系条件下去除率可达到95%以上。其较低的pH,较高Fe2+浓度,较高自由基生成量和氧化剂浓度,使得双氧体系较Fenton-Like体系有较高1,2-DCA去除率。菱铁矿催化双氧体系去除1,2-DCA反应过程中有中间产物生成,但最终完全脱氯,没有中间产物残留。     

Design of a novel non-equilibrium plasma-based water treatment reactor

A novel non-equilibrium plasma-based water treatment reactor consisting of high voltage multi-needle electrode submerged in aqueous phase and reticulated ground electrode suspended in gas phase above water was developed and applied to treat low concentrations of methyl orange (MO). The electrode configuration was optimized. Higher number and more uniform distribution of streamers were produced in gas phase when parallel five-needle configuration with needle spacing of 10mm for high voltage electrode, macroporous ground electrode with mesh size of 0.42mm, and electrode gap of 17mm were adopted. This case corresponds to the largest amount of hydrogen peroxide and ozone produced in aqueous phase and gas phase, respectively, and air flow rate presents an economical value. The injection of wastewater above ground electrode for pretreatment and the design of fixed mesh barriers further increase the amount of ozone dissolved in aqueous solution. The conversion of MO presents a positive correlation with input voltage and the increase of pulse repetition rate is conducive for the conversion. In addition, the effect of initial solution concentration and treating volume on the conversion, energy yield and COD removal was evaluated.     

Copper-ligand complex for the decolorization of synthetic dyes

The reaction system containing Cu(II), hydrogen peroxide and D-arabinono-1,4-lactone was found to be effective in the decolorization and reduction of toxicity of azo, thiazine-, triphenylmethane- and anthraquinone-based synthetic dyes. More than 85% decolorization was obtained with 100ppm Acridine Orange, Azure B, Chicago Sky Blue 6B, Crystal Violet, Evans Blue, Poly B-411, Reactive Blue 2, Reactive Blue 5, and Remazol Brilliant Blue R incubated for 24h in the presence of 10mM CuSO(4), 20mM D-arabinono-1,4-lactone and 80 mM H(2)O(2). The rate of decolorization was not affected by pH in the range of 3-9. The rapid decolorization was accompanied by a fast decomposition of H(2)O(2) in the reaction mixture and by a fast production of hydroxyl radicals.