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介电层的制备方法(氯化钠模板法、糖模板法、碳酸氢盐类模板法、微球模板法和硅模板法等);并介绍了微结构弹性体介电层在应力应变传感器和纳米发电机上的应用。     

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.     

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。     

电合成系列锌配合物及纳米ZnO的制备

采用锌金属为“牺牲”阳极,首次在无隔膜电解槽中,电化学一步法制备了纳 米ZnO前驱体锌配合物Zn(OEt)_2, Zn(OBu)_2, Zn(acac)_2, Zn(OEt)_2(acac)_2, Zn(OBu)_2(acac)_2(acac为乙酰丙酮基),产物通过红外光谱(FTIR)、拉曼光谱和 核磁共振进行表征。同时采用含Zn(OEt)_2(acac)_2的电解液直接水解制备纳米 ZnO粉体,纳米ZnO通过拉曼光谱、X射线粉末衍射(XRD)和透射电子显微镜（TEM） 进行表征。实验表明电解时防止阳极钝化,控制温度在50～60 ℃之间,采用有机 胺溴化物为导电盐,可以提高电合成效率;电解合成Zn(acac)_2, Zn(OEt)_2 (acac)_2, Zn(OBu)_2(acac)_2的电流效率比Zn(OEt)_2, Zn(OBu)_2高,其中Zn (OEt)_2(acac)_2适宜作为溶胶-凝胶法制备纳米ZnO的原料,制备得到的纳米ZnO经 600 ℃煅烧后呈球形单分散结构,平均粒径在5～10nm左右。     

Electrochemically catalyzed synthesis of cyclic carbonates from CO2 and propargyl alcohols

A convenient and efficient electrochemical method has been developed for the synthesis of the α-alkylidene cyclic carbonates from carbon dioxide (CO₂) and propargyl alcohols at room temperature. The electrosynthesis was successfully carried out with a copper anode and a nickel cathode in an undivided cell containing n-Bu₄NBr-MeCN electrolyte with a constant current under 3 MPa pressure of CO₂, and the α-alkylidene cyclic carbonates were obtained in good to excellent isolated yields in the secondary and tertiary terminal propargylic alcohols cases. The experimental results show that the electrogenerated Cu⁺ ions and strong bases in situ could efficiently catalyze or promote the coupling reaction under the cooperation of electrolytic medium MeCN and supporting electrolyte n-Bu₄NBr. The plausible mechanism of the coupling reaction was also discussed briefly.     

Electrochemical procedures in the treatment of spent nuclear fuel

The use of an electrochemical process for U/Pu partitioning has demonstrated a good performance and is a safe alternative for nuclear facilities. Its great advantages are the lack of introduction of foreign ions into the process and, especially, the minimization of the waste volume generated. For the introduction of electrochemical U/Pu partitioning in the 2nd Pu purification cycle, preliminary studies were carried out with a single mixer-settler unit. Based on the results, an 8-stage electrolytic mixer-settler (M-S MIRELE) was designed. Titanium was MIRELE's housing material (cathode) and platinum the anode, insulated with PTFE. The Pu recovery was higher than 99%, indicating the efficiency of this equipment.     

电流密度对锌电积用Pb-Ag平板阳极电化学行为的影响(英文)

研究了在不同电流密度下进行长时间极化后Pb-Ag(0.8%(质量分数,w))平板阳极的阳极电位、腐蚀率及阳极钝化膜.同时,也研究了该阳极在ZnSO4-MnSO4-H2SO4电解液中的阴极电流效率和阴极锌品质.阳极钝化膜的表面形貌用扫描电镜(SEM)进行观测.实验结果表明,不管电解液中是否存在Mn2+,电流密度对阳极和阴极的电化学行为都产生了显著的影响.随着电流密度的升高,阳极电位、腐蚀率、阴极电流效率和阳极泥生成量也增加,而阴极锌中的Pb含量则减少.当电流密度从500A·m-2降到200A·m-2时,阳极在ZnSO4-MnSO4-H2SO4电解液中的稳定电位和腐蚀率分别减少64mV和40%.此外,在比较低的电流密度下,阳极电位更容易稳定,阳极表面生成的钝化膜更加致密并与基体结合牢固,这些都有利于降低阳极腐蚀率.为了降低阳极电位、减小阳极腐蚀率及阳极泥生成量并提高阴极电流效率和阳极锌品质,锌电积的理想工作条件是较低的阳极电流密度和较高的阴极电流密度.     

Electrochemical reduction of aliphatic conjugated dienes in the presence of carbon dioxide

A voltammetric and electrolytic study involved in the electroreductive carboxylation of multi-substituted aliphatic coujugated dienes has been successfully conducted. With methyl sorbate as the modal compound, acceptable yields of carboxylation and dimerization were achieved, which were influenced by various reaction conditions such as the supporting electrolyte, cathode nature, current density, charge passed and temperature. A correlation was first established between distinct electronic effects of the dienes and the electrochemical characteristics of their reduction and the distribution law of target products.     

阳极支撑层憎水性对被动式直接甲醇燃料电池传质性能的影响

通过测定甲醇渗透率,详细研究了阳极支撑层的聚四氟乙烯（PTFE）含量对全被动式直接甲醇燃料电池（DMFC）甲醇传质和电池性能的影响。 膜电极集合体均使用相同的阳极催化层,膜和阴极。 实验结果表明,随着阳极支撑层PTFE含量的提高,甲醇渗透速率明显减小。 其含量较高时,甲醇传质阻力较大,会导致电池在很低的电流密度下就出现传质控制区。 采用PTFE质量分数为40%的支撑层时,DMFC以9 mol/L甲醇为燃料最大功率密度可达32×10-3 W/cm2,也进一步证明了适当提高阳极支撑层的憎水性,既有助于减少甲醇的渗透,又缓解了阴极的“水淹”问题。     

熔盐电化学低碳冶金新技术研究

本文重点介绍“氯化物熔盐体系电解还原固态氧化物冶金过程的高效化”和“氯化物熔盐体系电裂解硫化物及熔融碳酸盐与熔融氧化物体系电分解氧化物无温室气体排放冶金”的研究进展,结合武汉大学的部分代表性工作阐述了相关技术的原理,以期揭示熔盐电解技术在节能减排和资源高效利用上的优势及其发展前景,为发展短流程、低碳高效的电化学冶金工业提供理论和技术支持。     

Effects of current densities on the formation of LiCoO<Subscript>2</Subscript>/graphite lithium ion battery

The activation characteristics and the effects of current densities on the formation of a separate LiCoO₂ and graphite electrode were investigated and the behavior also was compared with that of the full LiCoO₂/graphite batteries using various electrochemical techniques. The results showed that the formation current densities obviously influenced the electrochemical impedance spectrum of Li/graphite, LiCoO₂/Li, and LiCoO₂/graphite cells. The electrolyte was reduced on the surface of graphite anode between 2.5 and 3.6 V to form a preliminary solid electrolyte interphase (SEI) film of anode during the formation of the LiCoO₂/graphite batteries. The electrolyte was oxidized from 3.95 V vs Li⁺/Li on the surface of LiCoO₂ to form a SEI film of cathode. A highly conducting SEI film could be formed gradually on the surface of graphite anode, whereas the SEI film of LiCoO₂ cathode had high resistance. The LiCoO₂ cathode could be activated completely at the first cycle, while the activation of the graphite anode needed several cycles. The columbic efficiency of the first cycle increased, but that of the second decreased with the increase in the formation current of LiCoO₂/graphite batteries. The formation current influenced the cycling performance of batteries, especially the high-temperature cycling performance. Therefore, the batteries should be activated with proper current densities to ensure an excellent formation of SEI film on the anode surface.