不同类型GaAs上应用约束刻蚀剂层技术进行电化学微加工

应用约束刻蚀剂层技术(CELT)对GaAs进行电化学微加工. 研究了刻蚀溶液体系中各组成的浓度比例、GaAs类型、掺杂以及阳极腐蚀过程对GaAs刻蚀加工过程的影响. 循环伏安实验表明, Br-可以通过电化学反应生成Br2作为刻蚀剂, L-胱氨酸可作为有效的捕捉剂. CELT中刻蚀剂层被紧紧束缚于模板表面, 模板和工件之间的距离小于刻蚀剂层的厚度时, 刻蚀剂可以对GaAs进行加工. 利用表面具有微凸半球阵列的导电模板, 可以在不同类型GaAs上加工得到微孔阵列. 实验结果表明: 在相同刻蚀条件下, GaAs的加工分辨率与刻蚀体系中各组分的浓度比例有关, 刻蚀结构的尺寸随着刻蚀剂与捕捉剂浓度比的增加而增大; 在加工过程中, p-GaAs相对于n-GaAs和无掺杂GaAs受到阳极氧化过程的影响较为显著, p-GaAs表面易生成氧化物层, 影响电化学微加工过程. X射线光电子能谱(XPS)和极化曲线实验也证明了这一点.     

Ti/nano TiO2-ZrO2 Electrode with High Catalytic Activity for Electro- catalytic Reduction of Maleic Acid to Succinic Acid

采用溶胶-凝胶法制备高活性Ti基纳米TiO2-ZrO2膜电极．通过X射线衍射分析表明,纳米TiO2-ZrO2粉体呈微-纳二级结构．扫描电子显微镜测试表明,颗粒平均尺寸约为30nm．通过循环伏安和恒电流电解技术研究发现,Ti／nanoTiO2-ZrO2电极对马来酸电催化还原制备丁二酸的活性要高于Ti／nanoTiO2电极,反应过程受扩散控制．以钛基氧化钌电极为阳极,Ti／nanoTiO2-ZrO2膜电极为阴极进行恒电流电解实验．结果表明,控制电流密度20mA·cm,温度60℃,丁二酸的产率达到96％．     

Ti/nano TiO_2-ZrO_2修饰电极电催化还原马来酸制备丁二酸

采用溶胶-凝胶法制备高活性Ti基纳米TiO2-ZrO2膜电极.通过X射线衍射分析表明,纳米TiO2-ZrO2粉体呈微-纳二级结构.扫描电子显微镜测试表明,颗粒平均尺寸约为30 nm.通过循环伏安和恒电流电解技术研究发现,Ti/nanoTiO2-ZrO2电极对马来酸电催化还原制备丁二酸的活性要高于Ti/nanoTiO2电极,反应过程受扩散控制.以钛基氧化钌电极为阳极,Ti/nano TiO2-ZrO2膜电极为阴极进行恒电流电解实验.结果表明,控制电流密度20 mA cm-2,温度60℃,丁二酸的产率达到96%.     

微结构化弹性体介电层的制备方法与应用

微结构化弹性体薄膜是指在表面或内部具有多孔或者特殊造型阵列的微纳米尺寸结构的弹性体薄膜,这类薄膜作为功能化介电层在柔性电子器件的制备领域获得了广泛的应用.本文从微结构弹性体介电层的制备和应用两个方面来介绍微结构弹性体介电层的研究进展,首先介绍了可用以制备介电层的弹性体的种类,然后综述了多孔和非多孔阵列两大类微结构弹性体...     

MgCl2-KCI—NaCI—CaCl2熔盐电解镁机理

在725℃温度下,对MgCl2-KCl-NaCl-CaCl2熔盐体系进行电解。研究结果表明,镁电解过程中阴极过电压ηc只有12～51mV,电解过程的过电压主要是由阳极引起的;阴极还原过程的极限扩散电流密度id为1．56A／cm^2;镁离子阴极放电反应的电子转移数为1．98：2个电子转移步骤之前存在着前置转化步骤MgCl^＋→Mg^2＋ ＋Cl^-。应用循环伏安法对4种不同配比下的镁离子行为进行的研究结果表明,CaCl2质量分数从10％增加到40％,维持MgCl2质量分数为10％以及NaCl与KCl的质量比为6：1不变,随着CaCl2质量分数的增加,镁离子结合成不易移动的络合阴离子,镁离子迁移的电流分数减小,镁离子的析出电位从-1．595V逐渐负移至与钙、钠共同沉积,阴极峰值电流Ipc值逐渐增大,阳极峰值电位与阴极峰值电位之差的绝对值｜φpa-φpc｜逐渐增大,阴极放电反应的可逆性逐渐降低。     

MgCl2-KCl-NaCl-CaCl2熔盐电解镁机理

在725℃温度下,对MgCl2-KCl-NaCl-CaCl2熔盐体系进行电解.研究结果表明,镁电解过程中阴极过电压ηc只有12～51 mV,电解过程的过电压主要是由阳极引起的;阴极还原过程的极限扩散电流密度id为1.56 A/cm2;镁离子阴极放电反应的电子转移数为1.98;2个电子转移步骤之前存在着前置转化步骤MgCl+ Mg2++C1-.应用循环伏安法对4种不同配比下的镁离子行为进行的研究结果表明,CaCl2质量分数从10%增加到40%,维持MgCl2质量分数为10%以及NaCl与KCl的质量比为6: 1不变,随着CaCl2质量分数的增加,镁离子结合成不易移动的络合阴离子,镁离子迁移的电流分数减小,镁离子的析出电位从-1.595 V逐渐负移至与钙、钠共同沉积,阴极峰值电流Ipc值逐渐增大,阳极峰值电位与阴极峰值电位之差的绝对值|φpa-φpc|逐渐增大,阴极放电反应的可逆性逐渐降低.     

稀土铁合金电解槽电热场数值模拟

固体自耗阴极电解法制备稀土铁合金,自耗阴极不断被消耗,阴极形状发生变化,对电解槽的生产造成影响。针对此现象,利用ANSYS有限元软件建立了不同阴极形状、极距及插入深度的稀土电解槽模型,进行了电场温度场的数值模拟,研究发现:阴极端部变尖,电流密度及电场强度减小,温度和热流密度下降,降低了生产效率。在自耗阴极电解槽模型下,极距的减小及插入深度的加深,使电流分布更均匀,发热量增加,温度升高,提高了电解效率。并采用热电偶测量温度对数值模拟进行验证,比较可知实测值与模拟值大体相同,表明了模拟的准确性。     

一维阵列电极法研究钢筋在混凝土中的腐蚀行为

建立一维阵列微电极技术,通过对阵列电极腐蚀电位、极化曲线以及微电极之间宏电流的测量,研究在腐蚀环境作用下钢筋混凝土腐蚀过程中宏电池电流和微电池电流的形成、发展及其相互作用.结果表明,腐蚀发生早期,腐蚀宏电池和微电池在不同区域优先形成而且并存.随着腐蚀的发展,受氧扩散控制,在腐蚀宏电池区域出现微电池,而某些腐蚀微电池区域与阴极区耦合,也形成腐蚀宏电池.腐蚀宏电池与微电池电流大小最终趋于一致.     

电解精炼铜实验的改进

以铜丝为电极、以聚丙烯酸钠（一种高吸水性聚合物）和氨的水溶液为电解质进行铜电解实验,电解过程中可明显观察到阳极的铜溶解、铜离子从阳极向阴极移动、单质铜在阴极析出等实验现象。该实验具有彰显原理、操作简单、现象明显、安全环保等优点。     

电解-电化学混合电容器的制备与性能

为解决电化学电容器工作电压过低的问题, 本文以钽电解电容器的烧结型钽块为阳极, 聚苯胺(PANI)/TiO₂电化学电容器复合电极为阴极, 成功制备了高能量密度、高工作电压的电解-电化学混合电容器. PANI/TiO₂复合电极是通过在多孔阳极氧化钛纳米管阵列中电化学聚合PANI 制得. 该阴极具有优良的倍率特性, 当平均功率密度为0.55 mW·cm^-2时, 对应的比容量仍达到10.0 mF·cm^-2. 由于与电解电容器复合, 该混合电容器的单元工作电压可高达100 V. 而且电化学电容器阴极的比容量远大于阳极, 故阴极所需尺寸远小于阳极, 节省的空间可用于增大阳极尺寸, 从而使混合电容器的比容量极大提高. 所制备的混合电容器体积能量密度和质量能量密度分别是钽电解电容器的4 倍和3 倍. 将该混合电容器在100 V下进行短路充放电实验, 循环10000 次后发现容量未衰减, 等效串联电阻未增加, 显示出极好的循环稳定性和功率特性. 计算表明其最大功率密度高达847.5 W·g^-1. 电化学阻抗谱显示其具有优良的阻抗特性和频率特性.     

Study on the Uniformity of Microgrooves in Through-Mask Electrochemical Micromachining with Moving Cathode北大核心CSCD

As a typical surface texture, microgrooves have broad prospects in the fields of mechanical engineering, bio-medicine, new energy and efficient heat dissipation of electronic products. Through-mask electrochemical micromachining (TMEMM) is widely used in the fabrication of micro-structures because of high processing efficiency and no residual stress. However, due to the edge effect of current distribution, there is often a serious dimension discrepancy problem in electrochemical machining of micro-structures. In order to weaken the influence of edge effect on the uniformity of microgrooves, the method that TMEMM with a moving cathode is presented. The current distribution in the electrochemical machining is constantly changed by the movement of the cathode. Thus, the uniformity of the micro-structure is improved. The method is studied through the combination of simulation and experimental verification. Firstly, the electrochemical machining process of TMEMM was analyzed theoretically. The theoretical analysis results show that the depth of electrolytic etching is proportional to the current density of electrolytic machining. To change the uniformity of the electrochemical machining, the most important thing is to improve the uniformity of the current distribution. On this theoretical basis, the current distribution and anodic contour of microgroove array during TMEMM are simulated by using the COMSOL finite element analysis software. The simulation results indicate that, compared with the conventional TMEMM, the TMEMM with moving cathode can obtain the microgrooves array with more uniform size. Secondly, on the basis of numerical simulation, the TMEMM experiment was carried out. The experimental results indicate that the TMEMM method of moving cathode can effectively improve the size uniformity of microgroove array. It can be observed by microscope that the microgroove array obtained by TMEMM with a moving cathode had good structural morphology and higher uniformity. Compared with conventional TMEMM, the uniformity of TMEMM with moving cathode has been improved by 68.3%. At the same time, under different experimental conditions, the trend of unevenness of microgroove array was calculated. With the increase of the distance between the cathode and anode, the microgroove depth heterogeneity showed a tendency of first decreasing and then increasing, when the distance between anode and cathode is about 1.3 mm, the unevenness of microgroove array reaches the minimum point. With the increases of cathode width and cathode speed, the depth inhomogeneities of microgroove increase and decrease gradually, respectively. The simulation results are basically consistent with the experimental results. It can be seen that the TMEMM with the moving cathode method can greatly improve the size uniformity. © 2021 Authors. All rights reserved.     

H型电解池中CO2电化学还原的阳极电解液问题

采用自制的H型电解池开展了KHCO₃溶液中电化学还原CO₂制甲酸的研究. 研究发现,在电解池中长时间电解时阴阳两极间的电压（槽电压）会持续升高,导致电解过程不可持续. 经过恒电位电解、恒电流电解、pH测试以及电解前后阳极室KHCO₃浓度分析等实验研究,作者发现,这是由以下过程引起的：阳极上的析氧反应产生的H⁺与电解液中的HCO₃^-反应生成水和CO₂,导致阳极室的HCO₃^-的消耗,之后阳极室的K⁺被迫扩散进入阴极室而导致阳极室电解质浓度下降. 因此,阳极室电解液导电性下降,进而引起阳极电位的升高. 研究发现,阳极电解液具有碱性时,都可能发生此种现象,因此,为了保证电解过程可持续且保持高的能量转换效率,阳极液的电解质不能是任何具有碱性的物质.     

用于镁硫电池的原位生长NiS的泡沫镍正极集流体

采用原位生长NiS的泡沫镍NiS@Ni(NNF)和铜箔分别作为硫@微孔碳(S@MC)正极材料的集流体, 0.4 mol/L(PhMgCl)₂-AlCl₃+1.0 mol/L LiCl “二代镁锂混合”作为电解液, 测试了镁硫电池恒电流和不同倍率下的充放电性能, 分析了2种不同的集流体在涂覆相同正极材料下对镁硫电池性能影响的原因. 研究发现, 采用铜箔集流体的镁硫电池循环后正极极片上观察到明显的裂缝, 镁负极表面有分布不均匀的附着物, 硫含量略高. 采用NNF为集流体时, 由于泡沫镍具有缓冲硫正极体积变化的孔道结构, 正极极片能基本保持原本的形貌; 特别是在NNF上原位生长的NiS可电催化加速多硫化物中间体的转化, 减少多硫化物的生成并减缓其穿梭, 不干扰镁负极上发生的电化学反应, 使镁负极极片表面更为均匀, 明显改善了镁硫电池的循环稳定性和倍率性能.     

Electrolysis of ammonia for hydrogen production catalyzed by Pt and Pt-Ir deposited on nickel foam

Electrolysis of ammonia in alkaline electrolyte solution was applied for the production of hydrogen. Both Pt-loaded Ni foam and Pt-Ir loaded Ni foam electrodes were prepared by electrodeposition and served as anode and cathode in ammonia electrolytic cell, respectively. The electrochemical behaviors of ammonia in KOH solution were individually investigated via cyclic voltammetry on three electrodes, i.e. bare Ni foam electrode, Pt-loaded Ni foam electrode and Pt-Ir loaded Ni foam electrode. The morphology and composition of the prepared Ni foam electrode were analyzed by scanning electron microscopy (SEM) and X-ray diffraction (XRD). Effects of the concentration of electrolyte solution and temperature of electrolytic cell on the electrolysis reaction were examined in order to enhance the efficiency of ammonia electrolysis. The competition of ammonia electrolysis and water electrolysis in the same alkaline solution was firstly proposed to explain the changes of cell voltage with the electrolysis proceeding. At varying current densities, different cell voltages could be obtained from galvanostatic curves. The low cell voltage of 0.58 V, which is less than the practical electrolysis voltage of water (1.6 V), can be obtained at a current density of 2.5 mA/cm². Based on some experimental parameters, such as the applied current, the resulting cell voltage and output of hydrogen gas, the power consumption per gram of H₂ produced can be estimated.     

混合超级电容器AC/LiMn2O4体系的电化学性能

对AC/LiMnO4体系混合电容器进行研究,以活性炭(AC)为负极材料,尖晶石结构的LiMn2O4为正极材料,Li2SO4为电解液。该体系的原理与锂离子电池很相似,从本质上说属于一种特殊的锂离子电池。改变正负极的质量配比,根据其电化学性能确定了该体系最佳的正负极质量配比。对不同电解液浓度的电容器进行不同电流密度充放电测试,发现电解液浓度增加,会使容量和大电流性能得到明显改善,极化电阻的增大会大大降低放电电压平台。实验表明该体系具有较高的能量密度和功率密度,同时保持了良好的循环性能。     

Electrocarboxylation of Carbon Dioxide with Polycyclic Aromatic Hydrocarbons Using Ni as the Cathode

Using Ni cathode and Al sacrificial anode, the electrocarboxylation of polycyclic aromatic hydrocarbons (naphthalene, 5‐methylnaphthalene, anthracene, phenanthrene and 1H‐indene) with carbon dioxide (4 MPa) could be successfully performed in an undivided cell containing n‐Bu₄NBr‐DMF supporting electrolyte with a constant current at room temperature, affording the corresponding trans‐dicarboxylic acids in good to excellent yields (62% –90%). Among the examined cathode materials (Ni, Pt, Ag, Cu and Zn), Ni and Pt cathodes exhibited a good catalytic activity for the electrocarboxylations. In addition, the experimental results indicated that electrolytic conditions (conducting salts, electricity, CO₂ pressure and temperature) could also affect the result of the electrocarboxylation. According to the results of the electrocarboxylations and CV (cyclic voltammetry), a possible electrochemical reaction mechanism was also proposed.     

Determination of mercury(II) ion by electrochemical cold vapor generation atomic absorption spectrometry.

A technique for determination of mercury is described; it is based on electrolytic reduction of Hg(II) ion on a graphite cathode, the trapping of mercury vapor and its volatilization into a quartz tube aligned in the optical path of an atomic absorption spectrometer. The electrochemical cell consisted of a graphite cathode and an anode operating with constant direct current for the production of mercury atoms. A pre-activated graphite rod was used as the cathode material. The optimum conditions for electrochemical generation of mercury cold vapor (the electrolysis time and current, the flow rate, the type of electrode and electrolyte) were investigated. The characteristic electrochemical data with chemical cold vapor using NaBH4-acid were compared. The presence of cadmium(II), arsenic(III), antimony(III), selenium(IV), bismuth(III), silver(I), lead(II), lithium(I), sodium(I) and potassium(I) showed interference effects which were eliminated by suitable separation techniques. The calibration curve is linear over the range of 5-90 ng ml(-1) mercury(II). The detection limit is 2 ng ml(-1) of Hg(II) and the RSD is 2.5% (n = 10) for 40 ng ml(-1). The accuracy and recovery of the method were investigated by analyzing spiked tap water and river water.     

Modelling of micro-electrochemical machining parameters used for machining of holes on copper plate

The electrochemical machining is a non-conventional machining process based on the electrolysis principle. It is used to machine various features on conducting engineering materials with the required accuracy and precision. So an attempt has been made to machine micro-holes on a 300 μm thick copper plate as an anode and a hollow stainless steel tool electrode of 250 μm diameter as the cathode. The machining operation is performed on the in-house developed micro-ECM experimental setup with controlled machining parameters voltage, concentration, and duty factor varied in three levels. A full factorial experimental plan is used to study the output responses material removal rate (MRR), radial overcut (ROC), circularity, and taper angle (TA). Later an adaptive neuro-fuzzy inference system (ANFIS) model has been developed and shown the effectiveness of the developed model in the paper. The Sugeno fuzzy model has been used in ANFIS to generate the fuzzy rules required for the model. Out of 27 experiments, 22 machining data are used for training the model, and the remaining 5 machining data are used for testing the developed model. The average error observed between the ANFIS predicted values and experimental values of MRR is 12.56%, circularity is 43.09%, ROC is 13%, and TA is 27.53%, respectively.     

发泡镍电极电化学还原嘌呤中间体

由三维发泡镍电极H2SO4电解质和阳离子交换膜,组成隔膜式三维发泡镍电解循环装置.利用该装置将3-甲基-4-亚氨基-5-异亚硝基脲嗪(NAU)电还原为3-甲基-4,5-二氨基脲嗪(DAU).比较发泡镍阴极的电流密度,测定不同pH条件下的反应电位.结果表明,发泡镍电极的电流密度比平板镍高77.3%～86.7%,电流效率平均90.3%,NAU还原转化率平均98.4%,电还原能耗平均2.92kWh/kg.恒电流电还原过程出现峰电位,继续延长电还原时间则有副反应产生.分别以传统铁粉还原和电还原的DAU完成下游嘌呤产品的合成,证明电还原产品收率不低于铁粉还原.