电动力学技术去除剩余污泥中铜、锌条件优化

电动力学去除剩余污泥中重金属受到多种因素的影响,其中电解电压、电极面积、电极材料等都有较大的影响,很有必要进行条件优化研究。针对存在的问题,系统的研究了电解电压、电极面积、电极材料对电动力学修复过程的影响。研究表明,影响污泥中重金属Cu和Zn去除率的因素大小顺序为:电压电极面积电极材料;采用等于或低于氢析出电压进行电动力学修复时,更有利于提高污泥中重金属去除率;增大电极面积,提高了电流强度,有利于污泥中重金属的转化、迁移,从而提高污泥中重金属去除率;研究表明,采用低于氢析出电压和惰性电极可以有效避免电极被腐蚀。     

电极改性对电极生物膜反硝化反应器硝酸盐氮去除性能的影响

探究在碳纤维毡电极上利用恒电压电化学聚合聚吡咯(PPy)的聚合效果,并利用傅里叶变换红外线(FTIR)及扫描电镜(SEM)对其进行表征;将聚吡咯覆膜改性后的碳纤维毡电极应用到自养反硝化的电极生物膜反应器(BER)中,考察电极改性对自养反硝化电极生物膜反应器的硝酸盐氮去除性能影响,并研究电极改性对生物膜附着量及生物膜微生物群落的影响。结果表明,恒电压电化学聚合能够在碳纤维电极表面形成均匀稳定的聚吡咯膜,从而实现聚吡咯在炭纤维毡电极上的覆膜改性。改性后的电极应用到自养反硝化电极生物膜反应器中,可使反应器对NO_3~--N的去除效率由对照反应器的67.3%增加到83.9%,处理效果提高了24.7%。对反应器内电极生物膜进行生物量测定和扫描电镜分析,可以看到R2反应器中改性电极生物膜附着量明显多于R1反应器中未改性电极生物膜的附着量,说明电极改性有利于生物膜的附着。电极生物膜微生物16S rDNA分析中R1反应器电极生物膜菌落组成中优势菌属为Dechloromonas sp.,而R2反应器电极生物膜的优势菌为Hydrogenophaga sp.(噬氢菌属)和Thauera sp.(陶厄氏菌属),两者有明显差别,并且R2反应器比R1反应器生物膜的菌落组成更多样化,这说明电极材料的改性对电极生物膜微生物群落的组成产生了影响。     

有毒难降解有机物高级氧化电催化电极

在电催化电极的作用下 ,电化学反应和化学催化作用结合 ,导致有机分子的电催化降解。在分析中 ,综述了电催化高级氧化电极研究现状 ,阐述与评价了过渡金属涂层电极、金属氧化物涂层电极、含掺杂半导体涂层电极、金刚石膜电极、三维电极等几个主要方面的研究成果 ,并对今后工作的重点提出了一些意见。     

三维电极法处理丙烯酸丁酯生产废水的研究

对比了二维电极与三维电极对丙烯酸丁酯生产废水的处理效果,考察了三维电极条件下废水初始COD浓度、曝气强度、极板间距对废水处理效果的影响,并研究了丙烯酸丁酯生产废水中特征污染物的去除过程.结果表明:三维电极对丙烯酸丁酯生产废水COD的去除率明显高于二维电极;三维电极电流效率和能耗受污染物浓度影响较大,污染物浓度越高,电流...     

有毒难降解有机物高级氧化电催化电极

在电催化电极的作用下，电化学反应和化学催化作用结合，导致有机分子的电催化降解。在分析中，综述了电催化高级氧化电极研究现状，阐述与评价了过渡金属涂层电极、金属氧化物涂层电极、含掺杂半导体涂层电极、金刚石膜电极、三维电极等几个主要方面的研究成果，并对今后工作的重点提出了一些意见。     

TiO_2改性钛基SnO_2电极的制备及性能研究

采用热分解法制备了钛基SnO2(Ti/SnO2)电极和TiO2改性钛基SnO2(Ti/SnO2-TiO2)电极。利用扫描电子显微镜(SEM)和X射线衍射(XRD)仪,极化曲线和循环伏安测试等方法对改性前后的电极进行表征,并考察电极的电催化氧化能力。结果表明,Ti/SnO2-TiO2电极膜层中存在锐钛矿型TiO2粒子,引入的TiO2使Ti/SnO2-TiO2电极具有比Ti/SnO2电极更粗糙的表面和更大的比表面积,且使电极的析氧过电位由1.7V提高至2.0V。循环伏安测试结果和电催化氧化4-氯苯酚(4-CP)过程均表明,Ti/SnO2-TiO2电极具有比Ti/SnO2电极更高的电催化氧化能力。     

软锰矿粒子电极的制备及其对SMP的催化降解

针对二氧化锰对废水中氯离子电解生成活性氯具有较好催化活性的特点,以软锰矿为原料制备一种新型粒子电极,将其用于三维电极系统处理油气田高含氯废水,利用活性氯的强氧化性进一步强化废水中难降解有机物SMP的处理;并考察软锰矿粒子电极制备条件对电极性能和电解效果的影响。结果表明:软锰矿与石墨质量比6∶4、PTFE分散液加入量10%、330°C下灼烧2 h为软锰矿粒子电极最优制备条件;与常规活性炭粒子电极相比,软锰矿粒子电极电解活性氯的产生量、COD去除率均显著优于活性炭粒子电极;且软锰矿粒子电极在重复使用多次后,活性组分流失量较小,对SMP的降解效率仍较高,保持了稳定的电催化性能。     

可渗透反应复合电极法对土壤重金属的电动去除

将零价铁(Fe0)、沸石等活性材料附着在电极上形成可渗透反应层并构成可渗透反应复合电极,采用不同的复合电极对Cd2+、Ni 2+、Pb2+和Cu2+等4种阳离子型重金属污染土壤进行了电动力学修复。研究了不同可渗透反应复合电极对土壤pH的控制效果以及对重金属的去除作用,分析了迁移到复合电极中的重金属形态变化。结果表明,复合电极中添加酸、碱性沸石并适时更换,可有效中和、截留阴阳极电解产生的OH-和H+,避免或减缓土壤酸碱迁移带的形成,防止重金属离子的过早沉淀及土壤过度酸化,极大提高了重金属的去除率。复合电极中Fe0可将迁移进来的重金属离子进行还原稳定,实现重金属污染物的捕获与固定,与迁移到沸石复合电极中的4种重金属不稳定态相比,"Fe0+沸石"复合电极中重金属不稳定态分别下降了61.4、60.5、61.4、57.1百分点。结果还显示,阴极采用"Fe0+沸石"复合电极并适时进行更换,施加1.5V/cm的直流电压修复10d后,土壤中Cd、Ni、Pb、Cu的总去除率分别为44.5%、41.5%、33.5%和36.7%,且进一步延长修复时间和持续更换电极可获得更为理想的修复效果。     

浅谈氟电极测定氟化物的体会

氟电极是现有的离子选择电极中性能较好的一种。在1984年全国饮用水水质调查期间,我们对氟电极测定氟化物进行了有关摸索,现分述如下。一、仪器和试剂 1.氟离子选择电极:CSB-F-1型(春花牌)长沙半导体材料厂出品。水洗空白电位为     

剩余污泥中重金属的电动力学修复研究

主要研究了电极材料和电极间距对氢析出电压和电压梯度的影响,以及电极材料、阴极液pH、修复时间对不同形态重金属去除率的影响.实验结果表明,在相同条件下,氢的析出电压和电压梯度受电极材料和电极间距的影响.阳极均为高纯石墨电极,阴极分别为高纯石墨电极、铜电极和铁电极,电极间距在32.5 cm时,高纯石墨为阴极的氢的析出电压最...     

Electrocatalytic reduction of nitrate in water with a palladium-modified copper electrode.

A highly active electrocatalytic electrode for nitrate reduction was prepared by the electro-deposition of palladium onto a copper electrode. The capacity of nitrate reduction by a palladium-modified copper electrode has been studied using cyclic voltammetry (CV). The existence of a reduction peak at -0.605 V versus saturated calomel electrode in 0.1-M sodium nitrate + 0.1-M perchloric acid solution (pH = 0.86) can be found in the CV measurement. The influence of solution properties, such as pH, nitrate concentration, and other anions in solution, on nitrate reduction was determined in detail. Results showed that nitrate reduction was suppressed in alkaline solution, while it was beneficial to nitrate reduction in acid or neutral solution. At low nitrate concentrations (0.01 to 0.5 M), nitrate reduction current increased with increasing nitrate concentration, but was hindered by sulfate. At high nitrate concentrations (1 to 5 M), no significant difference on nitrate reduction was observed. Compared with other different electrodes prepared in our work (copper, titanium, and palladium-modified titanium electrodes), the palladium-modified copper electrode showed the highest electrocatalytic capacity and stability in the nitrate-reduction process.     

Comparison of the adsorption of lead,cadmium, copper,zinc and barium to freshwater surface coatings

Measurements were made regarding the adsorption of lead, cadmium, copper, zinc and barium to freshwater surface coatings (biofilms and associated minerals), which were collected in Nanhu Lake in Jilin Province, PR China, in order to investigate the variability of adsorption capacities of these heavy metals mentioned in the above surface coatings. The adsorption of lead and other heavy metals to the biofilms was observed to decrease in the following order: copper, lead, zinc, cadmium, and barium. Generally, the values of Gamma(max) (the maximum adsorption, micromol/m(2)) increased with the standard electrode potential of metal elements used and were recorded as 166.7, 40.0, 29.4, 10.8, and 1.8 for copper, lead, zinc, cadmium and barium, respectively. The values of 1/Gamma(max) increased linearly with the decrease in values of the standard electrode potential of metal elements with a significant correlation (n=5, p=0.01) and increased linearly with the increase in values of covalent radius of metal elements with a significant correlation (n=5, p=0.05). This indicates that standard electrode potential and covalent radius were two of the principal characteristics of metals employed, causing the variation of lead and other heavy metal adsorption to the surface coatings.     

A combined photolytic-electrolytic system for the simultaneous recovery of copper and degradation of phenol or 4-chlorophenol in mixed solutions

The effects of the presence of copper on the photooxidation of phenol and 4-chlorophenol and of the presence of the phenols on the recovery of copper by electrodeposition are studied in three systems: a photolytic cell in the presence and absence of TiO2 as a catalyst or H2O2 as an oxidant; an electrolytic cell and a combined photolytic-electrolytic system. The optimum system for the simultaneous removal of copper and destruction of the phenols which overcomes the effects of copper-phenol reactions is a combined system with concentrator electrode technology incorporated into the electrolytic cell. This combined system achieves >99% removal of copper and destruction of phenol or 4-chlorophenol in an 8 h period.     

铜污染土壤电动修复研究

应用实验方法研究了土壤重金属污染的电动力学修复方法,分析了土壤重金属污染物的迁移和变化特征。实验结果表明,在电场作用下土壤中重金属的浓度分布发生明显变化,使得大部分重金属能在电极附近富集而被去除。当实验的电场强度为0.5 V/cm时,在阳极附近土壤中铜的去除效率达到71.1%。阳极附近的pH值由开始时的6.8逐渐变小到4.4,而阴极附近则相反,由开始时的6.6逐渐增大到9.1,此外电动修复过程中电极附近的温度会发生相应的变化。     

Copper-binding efficacy of water-soluble chitosans: characterization by aqueous binding isotherms

The major objective of the study is to measure directly the isotherms of copper binding onto soluble chitosan preparations, using ion-selective electrode technique. Copper uptake is found to decrease strongly when chitosan acetylation degree or chitosan concentration increased. When relating the bound copper concentrations to content of non-acetylated amine groups in a chitosan, differences between copper uptake on different chitosan preparations become reduced but not disappear. Other effects, in addition to the contents of non-acetylated amine groups, can involve differences in the copper binding by different chitosans. Due to isotherm non-linearity, the distribution coefficient K(d) of copper between a water-soluble chitosan and an aqueous solution may vary by two orders of magnitude as the free copper concentration C(free) varied. Linear relation between logK(d) normalized by free amine group content of chitosans and logC(free) may help in preliminary estimating of the copper binding by water-soluble chitosans at a certain pH.     

The effect of pH, ion strength and reactant content on the complexation of Cu2+ by various natural organic ligands from water and soil in Hong Kong

The complexation constants for copper associated with different natural organic ligands, including dissolved organic carbon (DOC) extracted from water, water soluble organic carbon (WSOC), fulvic acid (FA) and humic acid (HA) from soil, were determined and then compared based on discrete single site model. Both ion-selective electrode (ISE) and anodic stripping voltammetry were used to determine the content of free copper ions, while the relative number of complexation sites was estimated using a fluorescence quenching (FQ) at the same time. ISE proved to be the most applicable technique when the concentration of copper was above 10(-7) moll(-1). The logk values for two WSOC sample sites (Song Ziyuan and Xin Niangtan) were 4.64 and 4.66; higher than both the DOC and HA values yet lower than the FA values, which were unusually high due to unavoidable pollution from the cation exchange resin used during the purification process. Binding affinities between the copper ions and the organic ligands obtained from streams in Yong Wei (DOC) and Song Ziyuan (WSOC) were influenced by pH, ion strength, and reactant concentration. Values for logk increased with increases in pH (ion strength of 0.1 N). At pH 4, the logk values decreased with increases in the supporting electrolyte concentration and total copper ion additions.     

铜污染土壤电动修复研究

应用实验方法研究了土壤重金属污染的电动力学修复方法，分析了土壤重金属污染物的迁移和变化特征。实验结果表明，在电场作用下土壤中重金属的浓度分布发生明显变化，使得大部分重金属能在电极附近富集而被去除。当实验的电场强度为0.5 V/cm时，在阳极附近土壤中铜的去除效率达到71.1%。阳极附近的pH值由开始时的6.8逐渐变小到4.4，而阴极附近则相反，由开始时的6.6逐渐增大到9.1，此外电动修复过程中电极附近的温度会发生相应的变化。     

Treatment of chemical mechanical polishing wastewater by electrocoagulation: system performances and sludge settling characteristics

Treatment of copper chemical mechanical polishing (CMP) wastewater from a semiconductor plant by electrocoagulation is investigated. The CMP wastewater was characterized by high suspended solids (SS) content, high turbidity (NTU), chemical oxygen demand (COD) concentration up to 500 mgl(-1) and copper concentration up to 100 mgl(-1). In the present study, electrocoagulation was employed to treat the CMP wastewater with an attempt to simultaneously lower its turbidity, copper and COD concentrations. The test results indicated that electrocoagulation with Al/Fe electrode pair was very efficient and able to achieve 99% copper ion and 96.5% turbidity removal in less than 30 min. The COD removal obtained in the treatment was better than 85%, with an effluent COD below 100 mgl(-1). The effluent wastewater was very clear and its quality exceeded the direct discharge standard. In addition, sludge settling velocities after electrocoagulation were measured and the data were employed to verify the empirical sludge settling velocity models. Finally, the sludge settling characteristic data were also utilized to establish the relation between the solids flux (G) and the initial solids concentration.     

Field application of electrokinetic remediation for multi-metal contaminated paddy soil using two-dimensional electrode configuration

In this study, we evaluated the feasibility of in situ electrokinetic remediation for arsenic (As)-, copper (Cu)-, and lead (Pb)-contaminated soil, in a pilot-scale field application with two-dimensional electrode configurations. Square and hexagonal configurations with different electrode spacing, 1 m and 2?m, were investigated under a constant 100 V. A square configuration with electrode spacing of 2 m removed 61.5 % of As, 11.4 % of Cu, and 0.9 % of Pb, respectively, and a hexagonal configuration with the same spacing showed a higher removal efficiency in top (59 % of As, 0–0.5 m) and middle (53 % of As, 0.5–1.0 m) layers, but much lower removal efficiency in the bottom layer (1–1.5 m), which was thought to be due to groundwater flow through periodic rise and fall of tides. Fractionation analysis showed that As bound to Fe–Mn oxyhydroxide was the main form of As removed by the electrokinetic process. The two-dimensional configuration wasted less electrical energy by Joule heating, and required fewer electrode installations, compared to the one-dimensional electrode configuration.