Ni foam/Cu电极电催化还原硝酸盐氮

采用恒流电沉积法制备了泡沫镍/铜（Ni foam/Cu）电极.以Ni foam/Cu电极为阴极、Ti/RuO₂-Ir₂O₃电极为阳极构建电解体系,对水中硝酸盐氮进行电催化还原处理.并研究了电解质对总氮和氨氮去除率的影响和电极的稳定性.在一定范围内,增大电解质NaCl的浓度可以提高总氮和氨氮去除率.当NaCl浓度为0.5 g·L^-1时,在电解电流密度为8 mA·cm^-2的条件下对100 mg·L^-1 NO₃^--N溶液进行6次重复电解实验,2.5 h后硝酸盐氮去除率均可以达到94.5%以上.当NaCl浓度为1.25 g·L^-1时,在电解电流密度为8 mA·cm^-2的条件下对100 mg·L^-1 NO₃^--N溶液电解2.5 h,出水中氨氮浓度只有2.90 mg·L^-1,总氮去除率达到79....     

漂白废水白腐菌脱色的条件

碳源、氮源、Mn^2 浓度及pH值对F7菌漂白废水脱色有较大的影响，最佳培养基组成为：ρ（葡萄糖）10g/L，ρ（NH4Cl）0．13g/L，ρ（Mn^2 )20mg/L，随葡萄糖和NH4Cl添国量的增加，菌体生物量增加，但高浓度的NH4Cl对F7菌脱色有抑制作用，F7菌适宜生长pH值为4－5，适宜脱色pHwfhgo 3-6,最适脱色pH值为5．0另外，经脱色处理的漂白废水的毒性明显下降。     

采用气体扩散电极降解酸性红B研究

采用Pt/C气体扩散电极(GDE)为阴极,对酸性红B溶液进行单室电解和双室电解.单室电解中,以GDE为阴极,效果远优于石墨阴极,H2O2生成量为石墨阴极的10倍,在pH=1时,具有最好的处理效果,电解40min,脱色率为78.3%.通过分室电解,对酸性红B的降解机理进行了分析,阳极区为阳极的直接氧化,受pH值、Fe2 和O2的影响较小;气体扩散阴极为通过还原O2生成H2O2,然后分解为羟基自由基,氧化有机物,受pH值,Fe2 ,O2的影响较大.当pH=3,Fe2 浓度为50mmol·l-1,空气流量为180L·h-1时,电解80min,阴极区的脱色率为94.2%,COD去除率为66.8%,而阳极区的脱色率为73.3%,COD去除率为56.2%,电流在阳极区和阴极区的利用效率加起来计算的“表观电流效率”达到145.3%.     

非贵金属催化电解无害化去除硝酸盐氮的反应机制

以Ti/Co-Fe-Cu为阴极,Ti/IrO2-RuO2为阳极组成无隔膜电解体系,对非贵金属催化电解无害化去除NO3--N的反应机制进行了实验研究和理论分析.结果表明,NO3--N阴极催化还原过程中,反应物、产物需要通过对流、扩散作用,克服电场力,迁移至目标位置;在非贵金属的催化作用下,NO3--N受还原剂攻击,逐步还原为NH4+-N;还原中间产物NO-N和NH-N直接生成N2-N的过程受抑制,产物NH4+-N难以被再度直接氧化.添加Cl-作为支持电解质,实验电解体系发生阳极析氯、Cl2水解、NH4+-N氯氧化等过程,可将NH4+-N氧化为N2-N,且出水中NO3--N、NO2--N、氯胺类浓度很低.NO3--N无害化去除的反应机制是NO3--N在催化作用下,经传质、吸脱附、电子交换过程,还原为NH4+-N,NH4+-N经由Cl-→Cl2→HOCl→Cl-电解氯氧化循环,最终生成N2-N.     

阴极pH控制对电动去除电镀污泥重金属的影响

采用电动修复装置,选用电镀污泥作为试验材料,试验设计了3个不同pH值的阴极缓冲液处理,施加直流电压32 V,运行7 d,研究了不同pH值阴极缓冲液对电镀污泥电动修复过程的影响.结果表明,阴极缓冲液pH值的变化,影响了电动过程中电流大小,pH较低时,电流较大;pH较高时,电流较小.电动修复后,各处理电镀污泥重金属的电动修复效果不同,其中,pH值控制为3时,Ni、Cu、Zn和Cr的去除率分别达到70%、59%、30%和29%,而Pb的去除率在pH值控制为5时去除率达46%.各处理截面重金属浓度较实验前都有不同程度的降低,其中Cu、Pb和Ni在不同污泥截面分布较均匀,而Cr和Zn在各截面分布波动较大.电动修复对各种形态的重金属都有不同程度的去除,对可交换态和铁锰氧化物态的去除效果较差,对碳酸盐结合态和残渣态有明显去除,有机硫化物态去除效果一般.     

垃圾渗滤液生化出水电化学处理技术

以垃圾渗滤液生化出水为研究对象,利用Ti/RuO_2阳极、铁网双极电极及Cu-Zn阴极组成的Ti/RuO_2-Fe-Cu/Zn电化学体系进行电化学降解研究,讨论了电流密度、氯离子浓度和初始pH值对反应的影响及双极电极的作用.研究结果表明,当电流密度为100 m A·cm-2、初始氯离子浓度为2840 mg·L-1及初始pH值为8.5时,污染物的降解效率最高,电解4 h时,CODCr、NH+4-N、TN和TOC的去除率可分别达到94.12%、99.55%、94.17%和61.65%;在Ti/RuO_2-Fe-Cu/Zn电化学体系中,铁网电极的存在不仅可以强化有机物去除,并且可以有效抑制硝酸盐的积累,提升TN的去除能力;三维荧光分析表明,电解3 h,类蛋白质类物质和类腐殖质类物质荧光强度分别降低53.41%和71.02%,有机物矿化度升高.     

生物吸附剂-海黍子吸附镍

采用生物吸附剂-海黍子对重金属镍离子进行吸附，做了动力学实验，得到了海黍子吸附镍的动力学方程。研究了溶液的pH值，初始Ni^2 浓度等因素对Ni^2 的吸附特性的影响，得到最佳pH值4～6及最大吸附量0．8283mmo1／g，并用Langmuir和Freundlich方程对吸附等温线进行了拟合，用Langmuir方程拟合相关系数R^2达0．999以上。     

间歇反应器内污泥衍生吸附剂去除水溶液中镉、镍离子

利用城市污水厂的污泥化学活化法热解产生的吸附剂 ,在间歇反应器内对水溶液中Cd2 和Ni2 离子进行吸附性能的研究 .考察了溶液的pH值、接触时间、吸附剂的投加量及吸附质初始浓度对吸附效果的影响 ,结果表明 ,Cd2 ,Ni2 离子吸附达到平衡时的接触时间为 60min,pH值为 5 5— 6 0 ,溶液的初始浓度为 40mg·l- 1 和 30mg·l- 1 ,吸附剂的投加量不少于 1 0g·l- 1 和 2 0g·l- 1 .     

硫杆菌浸出废旧MH/Ni电池中重金属研究

生物淋滤法具有对环境友好、反应温和、运行成本低等优点,近年来主要用于回收难浸提矿石中有用金属及城市污泥有毒重金属脱除。应用氧化硫硫杆菌和氧化亚铁硫杆菌对废旧MH/Ni电池电极材料中重金属进行了生物淋滤处理可行性及工艺技术研究,考查了初始pH值、电极材料投加量、温度及底物单质硫添加量对金属Ni、Co浸出率的影响。试验结果表明:硫杆菌可以浸出电极材料中的重金属Ni和Co,初始pH值及温度对生物淋滤过程金属Ni、Co浸出率影响显著。在初始pH值1.0、电极材料质量分数为1.0%、温度30℃、底物单质硫质量浓度为4.0g·L-1条件下,经过20d生物淋滤,废旧MH/Ni电池中金属Ni和Co浸出率分别为95.7%和72.4%。     

示差脉冲吸附伏安法同时测定食品中痕量的镍和钴

本文研究了在NH_3/NH-4Cl中Ni(Ⅱ)、Co(Ⅱ)和丁二肟的螯合物Ni(Ⅱ)A_2、Co(Ⅱ)A_2在示差脉冲吸附伏安法中的特性,在高浓度下Ni(Ⅱ)A_2、Co(Ⅱ)A_2的吸附还原峰均发生变化。Ni(Ⅱ)A_2的吸附峰电势向负方向偏移,前沿变陡,半峰宽度变窄,主峰后出现新峰,血Co(Ⅱ)A_2的吸附峰的变化规律正好相反。在搅拌下富集, Ni(Ⅱ)0.3—20μg/l、Co(Ⅱ)0.03—20μg/l的范围内蜂电流与金属离子浓度有良好的线性关系。在溶液静止下富集,此线性范围可扩展到80μg/l。影响重现性的主要因素是溶液中NH_3浓度的变化及加电压前螯合物的吸附富集。提高NH_3浓度可以消除Zn~(2 )的干扰。提出了高浓度Ni(Ⅱ)存在下同时测定Ni/(Ⅱ)和Co(Ⅱ)的方法,并应用此方法测定了多种食品中的Ni和Co。     

几种萃取剂对土壤中重金属生物有效部分的萃取效果

采用6种萃取剂:pH=7的0.01mol/L CaCl_2、pH=7.3的0.005mol/L DTPA+0.1mol/L TEA(三乙醇胺)+0.01mol/L CaCl_2O.1mol/L NaNO_3、0.43mol/L HOAc、pH=7的0.05mol/L EDTA和pH=4.65的0.5mol/L NH_4OAc+0.02mol/L EDTA浸取液.对污染土壤中的重金属Cu、Zn、Cd、Pb、的进行了萃取,并比较了萃取剂的萃取能力。实验结果表明,HOAc、EDTA以及NH_4OAc-EDTA萃取各种重金属的能力远远大于其它几种萃取剂的萃取能力,是比较理想的萃取剂。     

改性斜发沸石处理高浓度氨氮废水

采用NaOH碱熔法对缙云斜发沸石进行处理,采用正交实验对碱熔法改性沸石的最佳条件进行了选择;并对改性前后的沸石进行粉末X射线衍射(XRD)、电感耦合等离子体发射光谱法(ICP-AES)和扫描电镜(SEM)表征;详细研究了所得改性沸石在氨氮废水处理中的净化性能.结果表明,处理沸石的水热温度对氨氮去除效果的影响最显著;碱熔法处理可使缙云斜发沸石转变为低硅铝比的Na-P型分子筛,它对氨氮废水的NH4+-N具有优异的吸附性能.当改性沸石投加量为5 g,对100 mL浓度为1000 mg.L-1氨氮溶液,氨氮去除率可达77.8%,改性沸石吸附NH4+-N是一快速吸附过程,且能较好地符合Langmuir吸附等温模式,偏向于单分子层的吸附.     

Preparation of nZVI embedded modified mesoporous carbon for catalytic persulfate to degradation of reactive black 5

• The MCNZVI is prepared as an interesting material for PS activation. • Graphitized carbon shells facilitate electron transfer from Fe⁰. • The MCNZVI exhibits excellent performance to degrade RB5 by ¹O₂. • The MCNZVI has high stability and reusability in the oxidation system. High-efficiency and cost-effective catalysts with available strategies for persulfate (PS) activation are critical for the complete mineralization of organic contaminants in the environmental remediation and protection fields. A nanoscale zero-valent iron-embedded modified mesoporous carbon (MCNZVI) with a core-shell structure is synthesized using the hydrothermal synthesis method and high-temperature pyrolysis. The results showed that nZVI could be impregnated within mesoporous carbon frameworks with a comparatively high graphitization degree, rich nitrogen doping content, and a large surface area and pore volume. This material was used as a persulfate activator for the oxidation removal of Reactive Black 5 (RB5). The effects of the material dosage, PS concentration, pH, and some inorganic anions (i.e., Cl⁻, SO₄²⁻) on RB5 degradation were then investigated. The highest degradation efficiency (97.3%) of RB5 was achieved via PS (20 mmol/L) activation by the MCNZVI (0.5 g/L). The pseudo-first-order kinetics (k = 2.11 × 10⁻² min⁻¹) in the MCNZVI/PS (0.5 g/L, 20 mmol/L) was greater than 100 times than that in the MCNZVI and PS. The reactive oxygen species (ROS), including ¹O₂, SO₄^·−, HO^·, and ·O₂⁻, were generated by PS activation with the MCNZVI. Singlet oxygen was demonstrated to be the primary ROS responsible for the RB5 degradation. The MCNZVI could be reused and regenerated for recycling. This work provides new insights into PS activation to remove organic contamination.     

EDTA对微电解体系降解对硝基酚的影响

考察了EDTA对微电解体系降解对硝基酚的影响及作用机制,结果表明,EDTA能够提高微电解处理对硝基酚的效果;单因素试验法确定了微电解/EDTA体系处理1000mg·l~(-1)对硝基酚的最佳条件:铁屑量120g·l~(-1),碳量20g·l~(-1),pH值为3,EDTA浓度1mmol·l~(-1).在此条件反应60min,对硝基酚去除率为89.7%,而常规微电解在最佳条件下对硝基酚的去除率仅为53.8%.值得关注的是EDTA不仅提高了对硝基酚的去除率,而且拓宽了微电解体系对pH值的适应范围,在中性条件下微电解/EDTA体系对硝基酚的去除率达到了63.5%,而相同条件下传统微电解法仅为19.5%.同时,通过对降解产物的鉴定,分析了对硝基酚在微电解/EDTA体系的降解途径.     

Efficient removal of heavy metals from electroplating wastewater using polymer ligands

Poly(hydroxamic acid)-poly(amidoxime) chelating ligands were synthesized from poly(methyl acrylate-co-acrylonitrile) grafted acacia cellulose for removing toxic metal ions from industrial wastewaters. These ligands showed higher adsorption capacity to copper (2.80 mmol?g⁻¹) at pH 6. In addition, sorption capacities to other metal ions such as iron, zinc, chromium, and nickel were also found high at pH 6. The metal ions sorption rate (t_1/2) was very fast. The rate of adsorption of copper, iron, zinc, chromium, nickel, cobalt, cadmium and lead were 4, 5, 7, 5, 5, 8, 9 and 11 min, respectively. Therefore, these ligands have an advantage to the metal ions removal using the column technique. We have successfully investigated the known concentration of metal ions using various parameters, which is essential for designing a fixed bed column with ligands. The wastewater from electroplating plants used in this study, having chromium, zinc, nickel, copper and iron, etc. For chromium wastewater, ICP analysis showed that the Cr removal was 99.8% and other metal ions such as Cu, Ni, Fe, Zn, Cd, Pb, Co and Mn removal were 94.7%, 99.2%, 99.9%, 99.9%, 99.5%, 99.9%, 95.6% and 97.6%, respectively. In case of cyanide wastewater, the metal removal, especially Ni and Zn removal were 96.5 and 95.2% at higher initial concentration. For acid/alkali wastewater, metal ions removing for Cd, Cr and Fe were 99.2%, 99.5% and 99.9%, respectively. Overall, these ligands are useful for metal removal by column method from industrial wastewater especially plating wastewater.     

TAR柱前络合、毛细管电泳分析痕量金属离子

1　IntroductionTransitionmetalswereamongthemostconcernelementsinenvironmentalanalysisduetotheirpotentialrolestoplantandanimals[1 ].Theserolesoftransitionmetalsinenvironmentdependedontheirconcentrationinthesoil,waterandlivingthings.Currently ,themostutiliz…     

Effect of iron addition on the performance of anoxic-oxic membrane process and biological phosphorus removal北大核心CSCD

In order to solve the problem of poor treatment of phosphorus in membrane bioreactor (MBR) with long sludge retention time (SRT), a ferric salt was added to enhance phosphorus removal; FeCl36H2O (Fe/P = 2.0) was added to the reactor. The removal efficiency of nitrogen, organic matters, and phosphorus in the MBR was investigated systematically. Moreover, this study focused on the membrane performance, the change of active sludge flora, and the effect of adding a ferric salt on membrane fouling before and after the addition. It was seen that adding the ferric salt could not affect the removal of COD and NH4 +-N and the removal rate of COD and NH4 +-N reached over 90%. However, the average removal rate of phosphorus was 52%, while the removal rate increased by nearly 40% after adding the ferric salt. The effects of adding ferric salts on the dominant bacteria and biological phosphorus removal of activated sludge were further studied. The results showed that the addition of ferric salt (Fe/P = 2.0) decreased the diversity of active sludge flora and relative abundance of some phosphorusaccumulating organisms and had a negative effect on biological phosphorus removal. The analysis of transmembrane pressure difference (TMP) recording revealed that the concentration of iron salts did not exacerbate membrane fouling. The results showed that the concentration of iron salts entering the membrane bioreactor would reduce the relative abundance and phosphorus removal efficiency of the activated sludge in the system to a certain extent, but it had no obvious effect on membrane fouling. It allowed the effluent to attain acceptable standards, especially with respect to phosphorus removal efficiency. © 2018 Science Press. All rights reserved.     

Recovery of Ni(II) from real electroplating wastewater using fixed-bed resin adsorption and subsequent electrodeposition

Resin adsorption and subsequent electrodeposition were used for nickel recovery. Treated wastewater can meet the Electroplating Pollutant Discharge Standard. The spent resin is completely regenerated by 3 BV of 4% HCl solution. 95.6% of nickel in concentrated eluent was recovered by electrodeposition. Effective recovery of high-value heavy metals from electroplating wastewater is of great significance, but recovering nickel ions from real electroplating wastewater as nickel sheet has not been reported. In this study, the pilot-scale fixed-bed resin adsorption was conducted to recover Ni(II) ions from real nickel plating wastewater, and then the concentrated Ni(II) ions in the regenerated solution were reduced to nickel sheet via electrodeposition. A commercial cation-exchange resin was selected and the optimal resin adsorption and regeneration conditions were investigated. The resin exhibited an adsorption capacity of 63 mg/g for Ni(II) ions, and the average amount of treated water was 84.6 bed volumes (BV) in the pilot-scale experiments. After the adsorption by two ion-exchange resin columns in series and one chelating resin column, the concentrations of Ni(II) in the treated wastewater were below 0.1 mg/L. After the regeneration of the spent resin using 3 BV of 4% (w/w) HCl solution, 1.5 BV of concentrated neutral nickel solution (>30 g/L) was obtained and used in the subsequent electrodeposition process. Using the aeration method, alkali and water required in resin activation process were greatly reduced to 2 BV and 3 BV, respectively. Under the optimal electrodeposition conditions, 95.6% of Ni(II) in desorption eluent could be recovered as the elemental nickel on the cathode. The total treatment cost for the resin adsorption and regeneration as well as the electrodeposition was calculated.     

无花果曲霉对Cu^2＋吸附的研究

采用生物吸附法，研究了经过预处理的无花果曲霉对Cu^2 吸附行为与影响吸附的主要因素，具体包括菌丝球与Cu^2 接触反应时间、Cu^2 浓度、原初pH值3个方面。结果表明：该菌丝球在吸附进行5min时，吸附量已达量2．855mg/g，在吸附进行4h以后趋于平衡。最佳pH范围为4．0－5．0，Cu62 浓度在20－100mg/L范围内吸附量为2．763－4．713mg/g，而吸附率却为32．31％－9．54％。其吸附行为在一定的温度和一定浓度范围内较好地符合Langmuir吸附等温模型。