Electrodeposition of metallic molybdenum films in
吉林省个体工商户雇工工伤保险办法

007. C. C. Yang, M. Nomura, M. Okamoto and I. Okada, 1988, “Isotope effect of Li-ions in countercurrent electromigration of molten LiOH”, Z. Naturforsch. 43a, 91. (SCI)
023. C. C. Yang, S. H. Wu and K. S. Shen, 2000, “The electrodeposition of tungsten in the low melting molten carbamide electrolyte”, J. of Science and Technology, 9, 31.(EI)
015. C. C. Yang and B. Lee, 1993, “Internal cation mobilities in the molten binary systems (Li, Na)Cl and (Na, K)Cl”, Z. Naturforsch. 48a. (SCI)
016. C. C.Yang, 1994, “The mechanism of ionic transport in some molten alkali chloride electrolytes”, J. of Yunlin Institute of Technology, 3, 111. (EI)
电镀行业术语之欧阳歌谷创编

常用名词欧阳歌谷(2021.02.01)1.化学腐蚀chemical corrosion金属在非电化学作用下的腐蚀(氧化)过程。
通常指在非电解质溶液及干燥气体中,纯化学作用引起的腐蚀。
2.双电层electric double layer电极与电解质溶液界面上存在的大小相等符号相反的电荷层。
3.双极性电极bipolar electrode一个不与外电源相连的,浸入阳极与阴极间电解液中的导体。
靠近阳极的那部分导体起着阴极的作用,而靠近阴极的部分起着阳极的作用。
4.分散能力throwing power在特定条件下,一定溶液使电极上(通常是阴极)镀层分布比初次电流分布所获得的结果更为均匀的能力。
此名词也可用于阳极过程,其定义与上述者类似。
5.分解电压decomposition voltage其定义与上述者类似。
能使电化学反应以明显速度持续进行的最小电压(溶液的欧姆电压降不包括在内)。
6.不溶性阳极(惰性阳极)inert anode在电流通过时,不发生阳极溶解反应的阳极。
7.电化学electrochemistry研究电子导体和离子导体的接触界面性质及其所发生变化的科学。
8.电化学极化(活化极化)activation polarization由于电化学反应在进行中遇到困难而引起的极化。
9.电化学腐蚀electrochemical corrosion在卑解质溶掖中或金属表面上的液膜中,服从于电化学反应规律的金属腐蚀(氧化)过程10.电化当量electrochemical equivalent在电极上通过单位电量(例如1安时,1库仑或1法拉第时),电极反应形成产物之理论重量。
通常以克/库仑或克/安时表示。
11 电导率(比电导)conductivity单位截面积和单位长度的导体之电导,通常以S/m表示。
12 电泳electrophoresis液体介质中带电的胶体微粒在外电场作用下相对液体的迁移现象。
13 电动势electromotive force原电池开路时两极间的电势差。
钠离子电池钼基负极材料的研究进展

2021年 5月 Journal of Science of Teachers′College and University May 2021文章编号:1007-9831(2021)05-0052-04钠离子电池钼基负极材料的研究进展张美娜,朱文霞,张欣艳,张平,王春香,陈丽梅(黑龙江八一农垦大学 理学院,黑龙江 大庆 163319)摘要:由于钠离子电池资源丰富,成本低廉,在大规模储能等方面具有很大的发展潜力.负极材料作为钠离子电池重要的组成部分,提升负极材料的性能是研究人员关注的重点内容.由于钼基过渡金属化合物在电化学反应过程中发生多电子转移,可以提供很高的可逆容量,因此钼基过渡金属化合物作为钠离子电池负极材料被广泛关注.从3个方面对钼基过渡金属化合物进行综述,首先,介绍钼基氧化物负极材料的研究进展;其次,介绍钼基硫化物负极材料的研究进展;最后,对开发与应用高性能钠离子电池钼基负极材料进行总结与展望.关键词:钠离子电池;钼基;负极材料中图分类号:O69 文献标识码:A doi:10.3969/j.issn.1007-9831.2021.05.011Research progress of molybdenum-based anode materials for sodium ion batteries ZHANG Meina,ZHU Wenxia,ZHANG Xinyan,ZHANG Ping,WANG Chunxiang,CHEN Limei(School of Science,Heilongjiang Bayi Agricultural University,Daqing 163319,China)Abstract:Sodium ion batteries have great potential in large-scale energy storage because of the abundant nature of sodium resource and low cost.As an important part of sodium ion battery,improving the performance of anode electrode material is the focus of researchers.Due to the multi-electron transfer of molybdenum-based transition metal compounds during electrochemical reaction,it can provide high reversible capacity,so molybdenum-based transition metal compounds are widely concerned as anode materials for sodium ion batteries.Molybdenum-based transition metal compounds are reviewed from three aspects.First,the research progress of molybdenum-based oxide anode materials is introduced.Secondly,the research progress of molybdenum-based sulfide anode materials is introduced.Finally,the development and application of molybdenum-based anode materials for high performance sodium ion batteries are summarized and prospected.Key words:sodium-ion batteries;molybdenum-based;anode materials锂离子电池作为便携式电子设备的主要能源供应装置,作为电动汽车的主要动力供应装置得到了广泛的研究与应用[1].然而,未来可再生能源一体化与智能电网的大规模应用,使资源储量、储能装置的安全性及生产成本等成为研究的焦点问题[2].其中,钠资源储量丰富,可利用性高,成本低,与锂有相似的氧化还原电位(-2.71 V,vs. SHE),使钠离子电池成为锂离子电池后最具有应用前景的储能装置[3].在锂离子电池研究的启发下,无序碳纳米材料是较合适的钠离子电池负极材料,但其电化学性质并不理想,因此收稿日期:2021-01-12基金项目:大庆市指导性科技计划项目(zd-2020-64);黑龙江农垦总局课题(HKKYZD-190504);黑龙江省大学生创新创业训练计划项目(201910223016);黑龙江省高等教育教学改革项目(SJGY20180362, SJGY20170444);黑龙江省教育厅高等教育教学改革研究项目(NDJY2025)作者简介:张美娜(1992-),女,黑龙江齐齐哈尔人,助理实验师,硕士,从事物理实验研究.E-mail:*****************通信作者:张平(1982-),男,河北张家口人,实验师,在读博士,从事物理实验教学研究.E-mail:********************开发稳定性好,容量高的钠离子电池负极材料迫在眉睫.由于钼基过渡金属化合物电化学反应过程可以发生多电子反应,提供更高的容量,因此钼基过渡金属化合物作为钠离子电池负极材料被广泛研究.1 钼基氧化物研究进展1.1 三氧化钼(MoO3)MoO3是一种低成本、环境友好的电极材料,其作为钠离子电池负极可提供高理论容量(1 117 mA h/g),约为石墨负极理论容量的3倍[4].为了更好地理解MoO3作为钠离子电池负极材料的储钠机理,Xia[5]等通过原位透射电子显微镜(TEM)对MoO3负极在电化学反应过程中电极材料的微观结构变化及相转变进行研究,在首次嵌钠过程中,1 mol MoO3与x mol Na+反应生成非晶态Na x MoO3,进一步嵌钠生成晶态NaMoO2和Na2O,最终得到结晶态Mo纳米颗粒分散在Na2O的基体中.在脱钠过程中,Mo纳米颗粒先被氧化成中间相NaMoO2,最后转化为非晶态Na2MoO3,表明在第1次嵌钠/脱钠过程中发生了不可逆的结构相变.在随后的嵌钠/脱钠电化学循环中,晶态Mo与非晶态Na2MoO3之间发生稳定的相变.Hariharan[6]等研究α-MoO3作为钠离子电池负极材料初始放电容量和充电容量分别为771,410 mA h/g,但首次库仑效率相对较低,仅有53%,主要是因为在充放电过程中电导率差和体积变化大.为了获得容量高、循环稳定性好、库仑效率高以及倍率性能好的电极材料,通常将粒径减小到纳米尺度来缩短钠离子扩散距离,建立导电网络以提高电导率,引入保护层以缓冲循环过程中的体积变化.通常采用多种合成方法得到不同的纳米结构,如纳米带、纳米片等,并将其应用于钠离子电池负极.Liu[7]等采用水热法制备聚吡咯包覆的MoO3纳米带,将其应用于水系钠离子电池负极材料,当与Na0.35MnO2正极组装全电池时,充放电电压范围为0~1.7 V,在80 W/kg的功率密度下可提供20 W h/kg的能量密度.此外,还与纯的MoO3电极相比,聚吡咯涂层不仅提供了良好的循环性能,而且也提供了良好的倍率性能.Kuan[8]等采用溶剂热和烧结2步法成功地将MoS2转化为MoO3阵列,在碳纤维布上得到致密且垂直的MoO3纳米片阵列(MoO3NSA/CFC),该阵列表现出优异的电化学性能,经过200次循环后容量保持率为90%.这得益于MoO3NSA/CFC的多孔结构和大的比表面积,可为钠离子储存提供丰富的电化学活性位点,并且垂直取向的MoO3纳米片与碳纤维布的紧密连接可以防止在脱钠过程中活性材料从集电极上剥落,确保多数MoO3纳米片参与电化学反应,从而提高循环过程中结构的稳定性.Yang[9]等通过简单的热处理钼基金属-有机骨架(Mo-MOFs)制备MoO3纳米片(MoO3NPs),将其用作钠离子电池负极材料,经过1 200次循环后,材料在50 mA/g的电流密度下表现出154 mA h/g优越的放电容量.即使在500 mA/g的电流密度下,经过500次循环后,也展示出217 mA h/g的高比容量.这种MoO3纳米片的设计可有效缓解体积膨胀,并在放电和充电过程中为钠离子输运和电子转移提供了多种渠道. 1.2 二氧化钼(MoO2)钼基氧化物除MoO3外,MoO2也可作为钠离子电池负极材料,在前几年,由于MoO2具有比MoO3更高的电子电导率而被广泛研究.He[10]等采用简单的水热法成功合成了嵌入在非晶态碳基体中的MoO2纳米片(MoO2/C纳米片),并将其作为钠离子电池负极,在50 mA/g的电流密度下,经过100次循环后,可保持367.8 mA h/g的可逆容量,其库伦效率保持在99.4%.MoO2/C纳米片在电流密度分别为50,100,200,500,50 mA/g时,其可逆容量分别为594,502,431,389,505 mA h/g.MoO2/C纳米片具有稳定的循环性能和高的倍率性能,主要是由于超薄的MoO2/C纳米片可以有效减小充放电过程中的应力或应变;嵌入在无定型基体中的MoO2纳米片可以很好地适应钠离子嵌入和脱出过程中较大的体积变化,有效防止MoO2纳米片的团聚;MoO2/C纳米片的结构可以促进电解质与电极之间的传输,减小钠离子的传输距离,改善电子和离子传输,提高复合电极的电化学性能.Cui[11]等通过简单的研磨与退火工艺合成了MoO2@C纳米花,在100 mA/g的电流密度下,具有172 mA h/g的可逆容量,在高的电流密度1 000 mA/g时,经过1 000次循环后仍具有166 mA h/g的容量.MoO2@C纳米花表现出优越的电化学性能,主要是由于其结构优势,MoO2@C纳米花可缩短离子扩散距离,提供更多的活性中心;纳米花形态可提高MoO2@C的分散性,促进电解质的快速渗透,并提供充足的孔隙来缓冲充放电过程中的体积变化;此外,在MoO2上直接包覆无定型碳,可以有效提高MoO2@C的电子电导率,增强结构完整性,还可以减轻循环过程中的体积变化.1.3 双金属钼基氧化物双金属钼基氧化物材料在电化学反应过程中,比单一金属氧化物具有更好的导电性,并且2种金属之间的协同效应使其性能优于单一金属氧化物.双金属氧化物材料有望克服单一金属氧化物所面临的库仑效率低、形成的固态电解质界面层不稳定和循环性差等问题.Chen[12]等用传统的固相法合成了钼酸银Ag2Mo2O7,将其作为钠离子电池负极材料.Ag2Mo2O7电极在电流密度为500 mA/g时,具有接近190 mA h/g 的高可逆容量,并且在1 000次循环后容量保持率为55%的长循环寿命.此外,通过原位X射线衍射、拉曼光谱和高分辨透射电镜对该材料的储钠机理进行分析.Ag2Mo2O7在初始放电过程中分解为Ag金属和Na2MoO4,在后期的循环过程中钠离子在立方相的Na2MoO4嵌入脱出,从而实现能量存储,为今后设计电极材料提供新思路.Huang[13]等通过共沉淀与热处理方法制备出氮掺杂碳包覆CoMoO4纳米棒(CoMoO4@NC),研究其作为钠离子电池负极材料的电化学性能.CoMoO4@NC电极在1 A/g的高电流密度下,在3 200个循环之后,仍然保持190 mA h/g的容量,比单纯的CoMoO4性能好很多.此外,将CoMoO4@NC作为负极,Na3V2(PO4)3作为正极,进行全电池测试.该全电池在1 A/g的电流密度下,经历100次循环后,具有152 mA h/g的可逆容量,且容量保持率为75%.因此,优化后的复合材料CoMoO4@NC具有良好的反应动力学和循环稳定性,这主要是将N掺杂的碳壳作为缓冲层,可以更好地适应脱钠/嵌钠过程中严重的体积变化,并且N掺杂可以提高电子电导率,激活表面位点.2 钼基硫化物研究进展钼基硫化物(MoS2)具有较高的理论可逆容量(670 mA h/g),并且MoS2具有良好的层状结构,其二维平面由S-Mo-S化学键相连的3个原子层组成,相邻的平面由范德华相互作用堆叠到一起,二维平面沿c轴的层间距为0.62 nm,这更易于Na+的嵌入/脱出,因此钼基硫化物(MoS2)在钠离子电池负极材料的研究中展现出巨大的发展潜力[14-15].然而,电化学反应过程中Na+在MoS2材料中重复嵌入/脱出,产生巨大的体积变化,将导致活性材料的粉碎和脱落,同时也会存在较低的电子电导率问题,加快了容量衰减[16].为了解决这些问题,通常通过控制材料的形貌或者采用与碳基材料复合的方式提升钼基硫化物的电化学性能.Wang[17]等制备了三维花状结构的碳复合MoS2纳米球(MoS2/C)钠离子电池负极材料.在电流密度为0.1 C的条件下,MoS2/C的可逆容量可达520 mA h/g,且将电流密度提高到1 C后,MoS2/C电极经历300次循环后仍能保持400 mA h/g的比容量.MoS2/C展现出较高的容量、较长的循环寿命和优异的倍率性能,主要是由于无定型碳包覆、小的纳米球尺寸以及在含有氟代碳酸乙烯酯(FEC)添加剂的电解质中MoS2/C纳米球上形成了稳定的固体电解质界面层.此外,研究人员通过原位XRD证明了MoS2与钠离子之间转化反应的可逆性.二维石墨烯具有优异的力学、热学、电学性能,是MoS2纳米片的理想载体.二维MoS2/石墨异质界面在提高MoS2的电子电导率,增大Na+在MoS2层表面的吸附能,保持Na+的高扩散迁移率方面起到非常重要的作用.Sun[18]等采用低成本、高产的合成方法,利用商用MoS2和石墨经过球磨剥离制备一种新型的MoS2与石墨烯纳米片杂化材料(MoS2/G),研究该材料作为钠离子电池负极材料的电化学性能,在20 A/g(≈30 C)的电流密度下,可逆容量可达284 mA h/g,在50 A/g(≈75 C)高的电流密度下,依然有201 mA h/g 的可逆容量,在0.3 A/g的电流密度,250次循环后容量保持率为95%,MoS2/G展现出优秀的倍率性能和良好的循环稳定性.研究人员进一步通过密度泛函理论计算表明,直接从商用块状MoS2和石墨中提取的MoS2/G纳米片具有较低的缺陷和残余含氧基团,增强二维异质界面,从而使材料获得了更高的电子电导率和更低的Na+扩散势垒,进而提供了超快的钠离子存储能力.生物质作为环境友好碳质前驱体可广泛应用于能源储存,生物质中各种杂原子(如N,P,S,O)可以原位引入到生物碳中,可有效提高材料的电子电导率和表面润湿性,进而提高材料的电子性能.Luo[19]等利用表面富含官能团的小球藻,通过氢键吸附水溶液中的磷钼酸,进一步进行简单煅烧,制备出嵌入在N/P共掺杂生物碳上的纳米尺寸的少层MoS2(MoS2-N/P-C).将其作为钠离子电池负极材料时,在5 A/g 的电流密度下,经过2 000次循环后,仍然有175 mA h/g的可逆容量.MoS2-N/P-C电极在高电流密度下的超长循环稳定性主要是由于含有大量N掺杂石墨的高导电生物碳,同时少层MoS2作为稳定材料,也可有效地缩短钠离子的扩散路径,在高电流密度下快速离子运输中起着重要的作用.另外,N和P共掺杂会在生物碳上产生丰富的缺陷,提高碳的电子电导率,从而产生优异的倍率性能.3 结语本文综述了钼基过渡金属氧化物、硫化物及其复合材料作为钠离子电池负极的最新研究进展.钼基过渡金属化合物电极由于转化反应机理、结构不稳定和电导率低,使其陷入了理论比容量高、库仑效率低、循环稳定性差、倍率性能差的困境.为了解决电化学过程中遇到的问题,研究人员利用许多改性方法,通过形貌调控和杂化碳复合材料制备,提高电子/离子迁移速率,抑制结构的变化.进一步通过原位TEM和原位XRD等一系列新的表征手段,对钼基过渡金属化合物的电荷储存机理进行研究,并对其进行原位EIS 测试等电化学表征.高性能钼基过渡金属化合物在钠离子电池负极的研究与应用,为今后设计电极材料、改善循环稳定性和研究充放电机理提供参考,为高性能钠离子电池的应用铺平了道路.虽然取得了一些研究进展,但仍需要清楚地认识到对反应机制深入了解的重要性.在未来研究的过程中,除了将钼基过渡金属化合物电极应用在锂离子电池和钠离子电池外,还应更多地关注其在不同储能装置中原位电化学反应的研究,特别是复合电极,具有较强的化学吸附效果和电化学催化活性,因此迫切需要对其在钠硫电池和金属氧化物电池等新型电池系统进行合理的设计和深入的研究,也可以在反应机理的研究、提高库仑效率和循环稳定性方面付出更多的努力,以实现未来高能量、低成本和环境友好的能源供应.参考文献:[1] Armand M,Tarascon J M.Building better batteries[J].Nature,2008,451(7179):652-657.[2] Jiang Y,Hu M,Zhang D,et al.Transition metal oxides for high performance sodium ion battery anodes[J].Nano Energy,2014(5):60-66.[3] Lee M,Hong J,Lopez J,et al.High-performance sodium-organic battery by realizing four-sodium storage in disodiumrhodizonate[J].Nature Energy,2017(2):861-868.[4] Wang G,Ni J,Wang H,et al.High-Performance CNT-Wired MoO3 Nanobelts for Li-Storage Application[J].Journal of MaterialsChemistry A,2013(1):4112-4118.[5] Xia W,Xu F,Zhu C,et al.Probing microstructure and phase evolution of α-MoO3 nanobelts for sodium-ion batteries by in situtransmission electron microscopy[J].Nano Energy,2016,27:447-456.[6] Hariharan S,Saravanan K,Balaya P.α-MoO3:A high performance anode material for sodium-ion batteries[J].ElectrochemistryCommunications,2013,31:5-9.[7] Liu Y,Zhang B H,Xiao S Y,et al.A nanocomposite of MoO3coated with PPy as an anode material for aqueous sodiumrechargeable batteries with excellent electrochemical performance[J].Electrochimica Acta,2014,116:512-517.[8] Kuan W,Jing Z,Gang X,et al.MoO3 nanosheet arrays as superior anode materials for Li-and Na-ion batteries[J].Nanoscale,2018,10(34):16040-16049.[9] Yang C,Xiang Q,Li X,et al.MoO3 nanoplates:a high-capacity and long-life anode material for sodium-ion batteries[J].Journalof Materials Science,2020,55:12053-12064.[10] He H,Man Y,Yang J,et al.MoO2 nanosheets embedded in amorphous carbon matrix for sodium-ion batteries[J].Royal SocietyOpen Science,2017,4(10):170892.[11] Cui C,Wei Q,Zhou L,et al.Facile synthesis of MoO2@C nanoflowers as anode materials for sodium-ion batteries[J].MaterialsResearch Bulletin,2017,94(11):122-126.[12] Chen N,Gao Y,Zhang M,et al.Electrochemical Properties and Sodium-Storage Mechanism of Ag2Mo2O7 as the Anode Materialfor Sodium-Ion Batteries[J].Chemistry A European Journal,2016,22(21):7248-7254.[13] Huang X,Zhang W,Zhou C,et al.N-doped carbon encapsulated CoMoO4 nanorods as long-cycle life anode for sodium-ionbatteries[J].Journal of Colloid and Interface Science,2020,576:176-185.[14] Zhu C,Mu X,Van A,et al.Single-layered ultrasmall nanoplates of MoS2embedded in carbon nanofibers with excellentelectrochemical performance for lithium and sodium storage[J].Angewandte Chemie International Edition,2014,53(8):2152-2156.[15] Choi S H,Ko Y N,Lee J K,et al.Rechargeable Batteries:3D MoS2-Graphene Microspheres Consisting of Multiple Nanosphereswith Superior Sodium Ion Storage Properties[J].Advanced Functional Materials,2015,25(12):1765.[16] Xie X,Ao Z,Su D,et al.MoS2/Graphene Composite Anodes with Enhanced Performance for Sodium-Ion Batteries:The Role ofthe Two-Dimensional Heterointerface[J].Advanced Functional Materials,2015,25(9):1393-1403.[17] Wang J,Luo C,Gao T,et al.An advanced MoS2/carbon anode for high-performance sodium-ion batteries[J].Small,2015,11(4):473-481.[18] Sun D,Ye D,Liu P,et al.MoS2/Graphene Nanosheets from Commercial Bulky MoS2 and Graphite as Anode Materials for HighRate Sodium-Ion Batteries[J].Advanced Energy Materials,2018,8(10):1702383.[19] Luo F,Xia X,Zeng L,et al.A composite of ultra-fine few-layer MoS2 structures embedded on N,P-co-doped bio-carbon forhigh-performance sodium-ion batteries[J].New Journal of Chemistry,2020,44:2046-2052.。
电镀行业术语之欧阳化创编

常用名词1.化学腐蚀chemical corrosion金属在非电化学作用下的腐蚀(氧化)过程。
通常指在非电解质溶液及干燥气体中,纯化学作用引起的腐蚀。
2.双电层electric double layer电极与电解质溶液界面上存在的大小相等符号相反的电荷层。
3.双极性电极bipolar electrode一个不与外电源相连的,浸入阳极与阴极间电解液中的导体。
靠近阳极的那部分导体起着阴极的作用,而靠近阴极的部分起着阳极的作用。
4.分散能力throwing power在特定条件下,一定溶液使电极上(通常是阴极)镀层分布比初次电流分布所获得的结果更为均匀的能力。
此名词也可用于阳极过程,其定义与上述者类似。
5.分解电压decomposition voltage其定义与上述者类似。
能使电化学反应以明显速度持续进行的最小电压(溶液的欧姆电压降不包括在内)。
6.不溶性阳极(惰性阳极)inert anode在电流通过时,不发生阳极溶解反应的阳极。
7.电化学electrochemistry研究电子导体和离子导体的接触界面性质及其所发生变化的科学。
8.电化学极化(活化极化)activation polarization由于电化学反应在进行中遇到困难而引起的极化。
9.电化学腐蚀electrochemical corrosion在卑解质溶掖中或金属表面上的液膜中,服从于电化学反应规律的金属腐蚀(氧化)过程10.电化当量electrochemical equivalent在电极上通过单位电量(例如1安时,1库仑或1法拉第时),电极反应形成产物之理论重量。
通常以克/库仑或克/安时表示。
11 电导率(比电导)conductivity单位截面积和单位长度的导体之电导,通常以S/m表示。
12 电泳electrophoresis液体介质中带电的胶体微粒在外电场作用下相对液体的迁移现象。
13 电动势electromotive force原电池开路时两极间的电势差。
从氯化镍溶液中电沉积α-Ni(OH)2

Trans. Nonferrous Met. Soc. China 30(2020) 2802−2811α-Ni(OH)2 electrodeposition from NiCl2 solutionJun-jie ZHANG1,2, Ting-an ZHANG1,2, Sen FENG11. School of Metallurgy, Northeastern University, Shenyang 110819, China;2. Key Laboratory of Ecological Metallurgy of Multi-metal Intergrown Ores of Ministry of Education,Northeastern University, Shenyang 110819, ChinaReceived 10 January 2020; accepted 7 August 2020Abstract: α-Ni(OH)2was synthesized from a NiCl2solution by electrodeposition method. In order to conduct asystematic study on the effects of experimental parameters, a series of electrolyte initial pH values, current densities,electrodeposition temperatures, and electrodeposition time were used. Cyclic voltammetry results demonstrated a sidereaction of Ni2++2e→Ni. The X-ray diffraction analysis, Fourier-transform infrared spectrum, and the color of the product showed that pure α-Ni(OH)2 could be obtained in the initial pH value range of 2−5.86, current density range of10−25 mA/cm2, electrodeposition temperature range of 25−35 °C, and electrodeposition time range of 1.0−3.0 h. Whenelectrodeposition temperature increased to 45 °C, a mixture of α-Ni(OH)2and metallic Ni was obtained. A currentdensity higher than 30 mA/cm2resulted in the sample with features of β-Ni(OH)2. A small amount of metallic Niexisted in the as-prepared sample when current density decreased to 5 mA/cm2. A slight increase of electrolyte pH wasobserved with increasing initial solution pH and current density. Electrodeposition mass revealed a slight decrease withinitial pH decreasing and showed an almost linear increase with current density increasing. The slope of the curve forelectrodeposition mass versus electrodeposition time remained stable in the first 2.0 h and then decreased.Key words: α-Ni(OH)2; NiCl2; electrodeposition; electrolyte initial pH; current density; electrodeposition temperature;electrodeposition time1 IntroductionNickel hydroxide is widely used as the activematerial for nickel−metal hydride (Ni−MH)rechargeable batteries due to its excellent electro-chemical performances [1−4]. It exists in twodifferent crystallographic forms of α-Ni(OH)2andβ-Ni(OH)2 [5,6]. During the charging process, eachNi atom in α-Ni(OH)2 can exchange 1.69 electrons,resulting in a theoretical specific capacity of482 mA·h/g [7,8], whereas each Ni atom inβ-Ni(OH)2 can exchange 0.99 electron, leading to atheoretical capacity of 289 mA·h/g [9]. Therefore,by using α-Ni(OH)2as the active material forNi−MH batteries, a higher specific capacity can beachieved [10,11]. As portable energy storagedevices are already a part of our daily life, and thistrend will certainly increase, it is imperative tostudy the synthesis process of α-Ni(OH)2to bettermeet this demand.Numerous methods have been adopted tosynthesize α-Ni(OH)2. Due to its low cost and shortprocess time, electrodeposition is often used toprepare α-Ni(OH)2[12−14]. Most commonly,Ni(NO3)2is used as the raw material to prepareα-Ni(OH)2via this method [15,16]. STREINZet al [17,18] quantified the mass of nickelhydroxide as functions of electrolytic conditions byan electrochemical quartz crystal nanobalance(EQCN). JAYASHREE and KAMATH [19,20]studied the factors governing the electrodepositionprocess of α-Ni(OH)2from Ni(NO3)2solutionand put forward the relevant electrodepositionFoundation item: Project (U1710257) supported by the National Natural Science Foundation of ChinaCorresponding author:Ting-anZHANG;Tel:+86-24-83681563;E-mail:***************DOI:10.1016/S1003-6326(20)65422-XJun-jie ZHANG, et al/Trans. Nonferrous Met. Soc. China 30(2020) 2802−2811 2803mechanism. As we know, α-Ni(OH)2 is unstable ina strong alkaline solution and is progressivelytransformed into β-Ni(OH)2[4,5]. JAYASHREEand KAMATH [21] investigated the effects of Aland Zn dissolved in the lattice of theelectrodeposited α-Ni(OH)2and found that α-Ni(OH)2could be stabilized by Al and Zn. PAN et al [22] prepared Al-stabilized α-Ni(OH)2fromNi(NO3)2and Al(NO3)3solutions by electrode-position method. GUALANDI et al [23] preparedmulti-metals-stabilized α-Ni(OH)2from its nitratesalts via electrodeposition.SHANGGUAN et al [24] prepared α-Ni(OH)2from various nickel salt solutions by a two-stepdrying method and reported that α-Ni(OH)2prepared from NiCl2solution exhibited betterperformance than that prepared from Ni(NO3)2solution. Considerable attention has been paid tothe preparation of α-Ni(OH)2from Ni(NO3)2solution; however, very few studies haveinvestigated the synthesis route of α-Ni(OH)2 fromNiCl2solution by electrodeposition method. NiCl2may be a more suitable raw material forsynthesizing α-Ni(OH)2 by electrodeposition. YAOet al [25] synthesized α-Ni(OH)2∙0.75H2O from a pure water dilute solution of NiCl2 (7−10 mmol/L)by electrodeposition method in a conventionalthree-electrode system and investigated the effectsof electrolyte concentration and electrodepositiontime. However, for industrial production, thereliability of this experiment needs to be considered.Besides the electrolyte concentration and reactiontime, other conditions, electrolyte initial pH, currentdensity, electrodeposition temperature, and electro-deposition time, should be considered.In the present study, a systematic investigationof the experimental parameters effects on α-Ni(OH)2 electrodeposition was carried out.2 Experimental2.1 Preparation of materialsThe electrolyte consisted of NiCl2·6H2O (analytical grade, ≥98%) as the solute and a mixture of ethanol and deionized water at the volume ratio of 1:1 (ethanol ≥99.7%) as the solvent [17,18,26]. The electrolytic cell was composed of a cathode chamber and two anode chambers. The anode chambers were located beside the cathode chamber. The chambers were separated with a cationic selectively permeable membrane. A stainless- steel sheet (35 mm × 90 mm × 1 mm) acted as the cathode and two iridium and ruthenium coated titanium sheets (17.5 mm × 90 mm × 1 mm) acted as the anode. In the present experiment, a series of the electrolyte initial pH values (2−5.86), current densities (5−30 mA/cm2), electrodeposition temperatures (25−45 °C), and electrodeposition time (1.0−3.0 h) were used. The concentration of the electrolyte was 0.2 mol/L (initial pH=5.86). In order to investigate the influences of the electrolyte initial pH, hydrochloric acid was used to acidize the electrolyte to pH values of 2, 3, 4, and 5. After electrodeposition, the synthesized powders in the cathode chamber were collected by filtration, washed with deionized water copiously, dried at 60 °C for 10 h, and weighed.2.2 Measurements of electrodeposition systemA PHSJ−3F acidometer was used to record the pH of the cathodic electrolyte during the experimental process. An electrochemical workstation (Zennium-pro) was used for cyclic voltammetry (CV) measurements. CV measure- ments were carried out in a typical three-electrode system. Both the working electrode and counter electrode were made of the same material as that used in the electrodeposition process, and their diameters were 1 mm. An Ag/AgCl electrode was used as the reference electrode. The electrolyte used for CV measurements was composed of NiCl2 (1 g/L) and NaCl (1 g/L) dissolved in a solvent composed of ethanol and water at the volume ratioof 1:9. NaCl was used as the supporting electrolyte. All CV tests were run from negative to positive potentials at a scanning rate of 30 mV/s.2.3 Characterization of materialsThe phase of the prepared samples was confirmed via X-ray diffractometry (XRD) using a Bruker D8 X-ray diffractometer. Fourier-transform infrared spectroscopy (FT-IR) was performed using a Nicolet iS50 infrared spectrometer. The morphology of the products was observed using a scanning electron microscope (SEM; SU8010).3 Results and discussion3.1 CV curvesThe CV curves of the electrodeposition system presented in Fig. 1 reveal the occurrence of twoJun-jie ZHANG, et al/Trans. Nonferrous Met. Soc. China 30(2020) 2802−2811 2804cathodic reactions. The first corresponded to the reduction reaction of Ni2+ions to metallic Ni at about −1.0 V (vs Ag/AgCl) (Eq. (1)) and the second corresponded to the hydrogen evolution reaction (Eq. (2)). In order to verify the hydrogen evolutionFig. 1CV curves of electrodeposition system with variations of initial pH in l g/L NiCl2+ 1 g/L NaCl solution (a), electrodeposition temperature in l g/L NiCl2 + 1 g/L NaCl solution (b), and solvents in 1 g/L NaCl solution (c) reaction, other two CV curves of the working electrode were measured in the NiCl2-free electrolyte, as shown in Fig. 1(c). It is noticeable from Fig. 1(c) that the second reduction reaction was neither specific to the NiCl2 solution nor to the ethanol solution. It was even present in pure water solution of NaCl, which meant that it was a hydrogen evolution reaction. The hydogen evolution reaction occurred due to the cathodic reaction in the NiCl2bath, and the first reduction reaction could be attributed to a side reaction of the electrodeposition process. Notably, in the acidic solution, the hydrogen evolution reaction should include Eqs. (2) and (3). As Eq. (2) dominated the hydrogen evolution reaction in the present work, it was used in the CV diagram to represent this reaction. OH− ions produced in Eq. (2) reacted with Ni2+to form Ni(OH)2(Eq. (4)), and the anodic reaction was the formation of chlorine gas (Eq. (5)). Ni2++2e→Ni (1) 2H2O+2e→2OH−+H2 (2) 2H++2e→H2 (3) Ni2++2OH−→Ni(OH)2 (4) 2Cl−−2e→Cl2 (5) The peak area of the side reaction in Fig. 1(a) increased with the decrease of the initial pH of the electrolyte; thus the number of Ni2+ ions taking part in the side reaction increased with the decreasing initial pH. The hydrogen evolution reaction showed similar trend with the side reaction. When the pH decreased, more H+ions were generated in the electrolyte. OH−ions existed in a non-free state, thus more Ni2+ions became free in these electrolytes. As the polarization became more negative, Ni2+ ions were reduced preferentially; hence, the reduction degree of Ni2+ions increased with the decrease of the pH value. For the hydrogen evolution reaction, with the decreasing pH, the electrolyte produced more hydrogen as there were more H+ions in the solution. Then, OH−ions became free by consuming H+ ions and reacted with Ni2+ to from Ni(OH)2 [27]. Figure 1(b) illustrates a favorable trend toward the side reaction with the increasing electrodeposition temperature, which is in accordance with the color of the prepared powders in Figs. 2(a1, a2). The color of the prepared samples changed from light green to dark green when the electrodeposition temperature increasedJun-jie ZHANG , et al/Trans. Nonferrous Met. Soc. China 30(2020) 2802−2811 2805Fig. 2 Photographs of samples obtained under different conditions: (a 1, a 2) 1.0 h of electrolysis in unacidified electrolyte (pH=5.86) at current density of 15 mA/cm 2 at 35 and 45 °C, respectively; (b 1, b 2) 1.0 h electrolysis in unacidified electrolyte at room temperature and current desities of 10 and 5 mA/cm 2, respectively; (c 1, c 2) 1.0 h electrolysis in pH=5.86 (unacidified) and pH=2 electrolytes at current density of 15 mA/cm 2 and room temperature, respectivelyfrom 35 to 45 °C. The dark green color was the result of a mixture of dark grey (the color of metallic Ni produced as a side product in this experiment) and light green (the color of Ni(OH)2). In addition to the initial pH of the electrolyte and the electrodeposition temperature, the current density also manifested a significant effect on the side reaction. The color of the product shifted from light green to celadon when the current density was reduced from 10 to 5 mA/cm 2 (Fig. 2(b 1, b 2)). Figure 2(c 1, c 2) displays the color of the samples synthesized at initial pH values of 5.86 and 2. Based solely on the color changes of the samples, the effect of the initial pH on the side reaction cannot be distinguished.3.2 Phase constitution and structural disorderIt is well known that both the phase and average long-range structure of the sample can be exhibited by its XRD pattern [28]. Figure 3 displays the XRD patterns of the powder samples obtained under different electrodeposition conditions. The diffraction peaks at 2θ values of 22.7°, 33.4°, 38.7°, and 59.9° appeared from the (006), (101), (015), and (110) planes of pure hydrous nickel hydroxide (Ni(OH)2·0.75H 2O, α-Ni(OH)2) (JCPDS No. 38− 0715). All of these powders obtained were indexed as pure α-Ni(OH)2 except for that obtained at 45 °C, which showed evident diffraction peaks of metallic nickel. Notably, the resultant powder obtained at a current density of 5 mA/cm 2 was indexed as pureJun-jie ZHANG , et al/Trans. Nonferrous Met. Soc. China 30(2020) 2802−28112806Fig. 3 XRD patterns of samples synthesized in 0.2 mol/L NiCl 2 solution under different conditions: (a) 1.0 h electrolysis at current density of 15 mA/cm 2 in initial pH range of 2−5.86 at room temperature; (b) 1.0 h electrolysis in unacidified electrolyte at room temperature in current density range of 5−30 mA/cm 2; (c) 1.0 h electrolysis in unacidified electrolyte at current density 15 mA/cm 2 in electrodeposition temperature range of 25−45 °C; (d) 1.0−3.0 h electrolysis in unacidified electrolyte at current density 15 mA/cm 2 and room temperatureα-Ni(OH)2, which did not fit well with Fig. 2(b 2). This discrepancy may result from the weak proportion of metallic nickel in the end product. From the aspect of the average long-range structure, it is evident that the initial pH of the electrolyte had no obvious effect on the diffraction peaks of the samples (Fig. 3(a)). This implied that both the average long-range structure and the degree of structural disorder remained stable with respect to the initial pH of the electrolyte. The diffraction peak intensities of the samples increased with increasing current density, electrodeposition temperature, and time (Figs. 3(b −d)). In particular, the diffraction peaks of the (006), (101), and (110) planes became narrow as the electrodeposition current density increased from 5 to 30 mA/cm 2 (Fig. 3(b)) due to the supply of more OH − ions. In the presence of adequate OH − ions, the vacancies for OH − ions around a Ni atom tended to be fully occupied, facilitating the generation of a completecrystalline structure with no lattice defects.3.3 FT-IR analysisThe diffraction peaks of α-Ni(OH)2 were not obvious due to its hydrotalcite-like structure (Fig. 3) [8,29]. FT-IR analysis provided the short- range coordination of the samples [28], and it complemented the XRD analysis. Both α-Ni(OH)2 and β-Ni(OH)2 possessed a layered structure stacked by Ni(OH)2 layers [30]; however, α-Ni(OH)2 existed in the OH − ion-deficient form [30,31]. In order to balance the excess positivecharges, some anions (Cl − and CO 32−) and water molecules were intercalated in the interspaces of Ni(OH)2 layers [24,32]. Figure 4(a) displays the FT-IR spectra of α-Ni(OH)2 and β-Ni(OH)2. In contrast to β-Ni(OH)2, α-Ni(OH)2 did not show the narrow absorption peak of non-H-bonded OH − groups at approximately 3640 cm −1; however, it showed a wide absorption peak of H-bonded OH −Jun-jie ZHANG , et al/Trans. Nonferrous Met. Soc. China 30(2020) 2802−2811 2807Fig. 4 FT-IR spectra of α-Ni(OH)2 and β-Ni(OH)2 (a), and samples obtained under different electrolyte initial pH values (b), current densities (c), and electrodeposition time (d)representing interlayer water molecules at approximately 3400 cm −1 [9,33]. In addition, compared to α-Ni(OH)2, the vibration peak of the in-plane Ni —O —H bond of β-Ni(OH)2 shifted from approximately 650 to 570 cm −1 [9,34]. For α-Ni(OH)2, the peaks at 1621 and 1361 cm −1 corresponded to the bending of water molecules and CO 32−ions intercalated in the interlayer space (Figs. 4(b −d)) [4,35]. The very tiny absorption peak at 1062 cm −1 appeared from the vibration of the interlayered Cl − from the raw material. Figures 4(b) and (d) demonstrate that β-Ni(OH)2-free α-Ni(OH)2 was synthesized under varying initial pH (2−5.86) and electrodeposition time (1.0−3.0 h). Figure 4(c) shows the effect of current density on the FT-IR spectra of the products. A dimly-visible narrow peak at 3640 cm −1 representing β-Ni(OH)2 appeared at the current density of 30 mA/cm 2, indicating that further increasing current density could lead to β-Ni(OH)2.3.4 Morphology of synthesized samplesThe morphologies of the samples obtainedunder different electrodeposition conditions manifested no prominent difference (Fig. 5). They all consisted of large and small irregularly-shaped particles, similar to those obtained from a Ni(NO 3)2 solution by the electrodeposition method [20,22].3.5 Variation of electrolyte pHThe curves of pH versus time for the cathodic electrolyte at various initial pH values and current densities are illustrated in Fig. 6. The solid and dashed lines in Fig. 6 represent the measured (the metrical position is 2.5 cm from the cathode) and calculated results based on the solubility product constant (K sp ) of Ni(OH)2 (5.5×10−16), respectively. It is evident from Fig. 6 that the measured values of the pH were lower than the calculated value, which indicated that theoretically, no Ni(OH)2 was synthesized in the bulk solution of the cathodic chamber. In fact, Ni(OH)2 was deposited on the surface of the electrode and then was detached to the vicinity of the electrode (Fig. 6(a)). The metrical position of the pH value could be considered to be in the bulk solution because there was a distanceJun-jie ZHANG , et al/Trans. Nonferrous Met. Soc. China 30(2020) 2802−28112808Fig. 5 SEM images of samples obtained under different electrodeposition conditions: (a) 15 mA/cm 2, 1 h, pH=5.86; (b) 20 mA/cm 2, 1 h, pH=5.86; (c) 15 mA/cm 2, 1 h, 35 °C; (d) 15 mA/cm 2, 2 h, pH=5.86Fig. 6 Variation of pH of electrodeposition systems vs time at different initial pH (a) and current densities (b)of 2.5 cm between them. Figure 6(a) reveals that the pH of the electrolyte remained stable after 5 min of electrodeposition even when the initial pH value was 2. In comparison to the unacidified electrolyte (pH=5.86), more H + ions were present in the electrolyte acidified by hydrochloric acid; thus this acidified electrolyte easily produced more H + ions (Fig. 6(a)), thereby these H + ions were quickly consumed, consequently, OH − ions became free in the electrolyte. The pH of the electrolyte began to increase until the generation and consumption rates of OH − became almost the same; therefore, the initial pH almost had no effect on the pH of the electrolyte after 5 min electrodeposition. Notably,the electrolytic energy consumed by H + ions did not result in OH − ions, leading to a waste of energy. Figure 6(b) presents the relationship between the pH of the cathodic electrolyte and the current density. A slight increase in the pH was observed with the increasing current density, because OH − ions produced on the electrode surface were not consumed in time and were transported to the bulk solution.3.6 Deposition mass versus electrodepositionconditionsFigure 7 shows the relationship between the deposition mass and different electrodepositionJun-jie ZHANG, et al/Trans. Nonferrous Met. Soc. China 30(2020) 2802−2811 2809Fig. 7 Relationship between electrodeposition mass and electrodeposition conditions with varying electrolyte initial pH (a), current density (b), and electrodeposition time (c)conditions. The solid and dashed lines in Fig. 7 represent measured and calculated results based on Faraday’s law, respectively. It is noticeable that the collected mass of each separated sample decreased slightly with the decrease of initial pH (Fig. 7(a)) because the consumption of electrolytic energy by H+ions used to acidify the solution. Figure 7(b) shows an almost linear relationship (R2=0.9993) between the electrodeposition mass and the current density (10−30 mA/cm2). The slope of curve for electrodeposition mass vs electrodeposition time (electrodeposition rate) remained nearly constant when the electrodeposition time was less than 2.0 h and decreased after that, as shown in Fig. 7(c), because the concentration of Ni2+was decreased due to consumption. Particularly, some metrical points were found to be higher than the calculated ones (Fig. 7) because the actual molecular mass is higher than the applied one (106.19 for Ni(OH)2·0.75H2O) due to the presence of intercalated anions (CO32−, Cl−) (Fig. 4) [17,18,20].4 Conclusions(1) CV results demonstrated a side reaction of Ni2++ 2e→Ni.(2) XRD results showed that pure α-Ni(OH)2 was obtained in the initial pH value range of 2−5.86, the current density range of 5−30 mA/cm2, the electrodeposition temperature range of 25−35 °C, and the electrodeposition time range of 1.0−3.0 h. When the electrodeposition temperature increased to 45 °C, a mixture of α-Ni(OH)2and metallic Ni was obtained. FT-IR results showed that current density of 30 mA/cm2resulted in samples with features of β-Ni(OH)2. The color of the product displayed that a small amount of metallic Ni existed in the sample when the current density decreased to 5 mA/cm2.(3) The pH of the cathodic electrolyte displayed a slight increase with increasing electrolyte initial pH and current density.(4) Electrodeposition mass showed no obvious influence by the initial pH of the electrolyte and increased almost linearly with the current density increasing. The slope of curve of electrodeposition mass versus electrodeposition time remained stable in the first 2.0 h and decreased after that. References[1]ASH B, KHETIC K, SUBBAIAH T, ANAND S,PARAMGURU R K. Physcio-chemical and electro-chemicalproperties of nickel hydroxide precipitated in the presence ofmetal additives [J]. Hydrometallurgy, 2006, 84: 250−255. [2]LIU B, YUAN H T, ZHANG Y S, ZHOU Z X, SONG D Y.Cyclic voltammetric studies of stabilized α-nickel hydroxideelectrode [J]. Journal of Power Sources, 1999, 79: 277−280.Jun-jie ZHANG, et al/Trans. Nonferrous Met. Soc. China 30(2020) 2802−2811 2810[3]HU W K, GAO X P, NOREUS D, BURCHARDT T,NAKSTAD N K. Evaluation of nano-crystal sized α-nickelhydroxide as an electrode material for alkaline rechargeablecells [J]. Journal of Power Sources, 2006, 160(1): 704−710. [4]LI J L, ASLAM M K, CHEN C G. One-pot hydrothermalsynthesis of porous α-Ni(OH)2/C composites and itsapplication in Ni/Zn alkaline rechargeable battery [J].Journal of the Electrochemical Society, 2018, 165(5):A910−A917.[5]YAO J H, LI Y W, LI Y X, ZHU Y X, WANG H B.Enhanced cycling performance of Al-substituted α-nickelhydroxide by coating with β-nickel hydroxide [J]. Journal ofPower Sources, 2013, 224: 236−240.[6]BAO Jie, ZHU Yan-juan, ZHUANG Yi-huan, XUQing-sheng, ZHAO Ru-dong, LIU Yong-lin, ZHONGHao-liang. Structure and electrochemical performance of Cusingly doped and Cu/Al co-doped nano-nickel hydroxide [J].Transactions of Nonferrous Metals Society of China, 2013,23: 445−450.[7]CHENG F Y, CHEN J, SHEN P W. Y(OH)3-coated Ni(OH)2tube as the positive-electrode materials of alkalinerechargeable batteries [J]. Journal of Power Sources, 2005,150: 255−260.[8]HUANG H L, GUO Y J, CHENG Y H. Ultrastable α phasenickel hydroxide as energy storage materials for alkalinesecondary batteries [J]. Applied Surface Science, 2018, 435:635−640.[9]LI Y W, YAO J H, ZHU Y X, ZOU Z G, W ANG H B.Synthesis and electrochemical performance of mixed phaseα/βnickel hydroxide [J]. Journal of Power Sources, 2012,203: 177−183.[10]LI Y W, YAO J H, LIU C J, ZHAO W M, DENG W X,ZHANG S K. Effect of interlayer anions on theelectrochemical performance of Al-substituted α-type nickelhydroxide electrodes [J]. International Journal of HydrogenEnergy, 2010, 35: 2539−2545.[11]JAYASHREE R S, KAMATH P V. Nickel hydroxideelectrodeposition from nickel nitrate solutions: Mechanisticstudies [J]. Journal of Power Sources, 2001, 93: 273−278. [12]DONG Q, YUAN H L, YAN Y B. Research progress inpreparation methods of nickel hydroxide [J]. Hebei Chemical,2004, 6: 28−31. (in Chinese)[13]DIXIT M, KAMATH P V, KUMAR V G,MUNICHANDRAIAH N, SHUKLA A K. An electrochemically impregnated sintered-nickel electrode [J].Journal of Power Sources, 1996, 63: 167−171.[14]SASAKI Y, YAMSHITA T. Effect of electrolytic conditionson the deposition of nickel hydroxide [J]. Thin Solid Films,1998, 334: 117−119.[15]ASH B, MISHRA K G, SUBBAIAH T, PARAMGURU R K,MISHRA B K. Electrochemical studies on electrolyticpreparation of battery grade nickel hydroxide—Effect ofOH− to Ni2+ ratio [J]. Journal of Power Sources, 2015, 275:55−63.[16]WATANABE K, KIKUOKA T, KUMAGAI N. Physical andelectrochemical characteristics of nickel hydroxide as apositive material for rechargeable alkaline batteries [J].Journal of Applied Electrochemistry, 1995, 25: 219−226. [17]STREINZ C C, MOTUPALLY S, WEIDNER J W. The effectof temperature and ethanol on the deposition of nickelhydroxide films [J]. Journal of the Electrochemical Society,1995, 142: 4051−4056.[18]STREINZ C C, HARTMAN A P, MOTUPALLY S,WEIDNER J W. The effect of current and nickel nitrateconcentration on the deposition of nickel hydroxide [J].Journal of the Electrochemical Society, 1995, 142: 1084−1089.[19]JAYASHREE R S, KAMATH P V. Factors governing theelectrochemical synthesis of α-nickel(II) hydroxide [J].Journal of Applied Electrochemistry, 1999, 29: 449−454. [20]JAYASHREE R S, KAMATH P V. Nickel hydroxideelectrodeposition from nickel nitrate solutions: Mechanisticstudies [J]. Journal of Power Sources, 2001, 93: 273−278. [21]JAYASHREE R S, KAMATH P V. Suppression of theα→β-nickel hydroxide transformation in concentrated alkali:Role of dissolved cations [J]. Journal of Applied Electrochemistry, 2011, 31: 1315−1320.[22]PAN T, WANG J M, ZHAO Y L, CHEN H, XIAO H M,ZHANG J Q. Al-stabilized α-nickel hydroxide prepared byelectrochemical impregnation [J]. Materials Chemistry andPhysics, 2003, 78: 711−718.[23]GUALANDI I, MONTI M, SCA VETTA E, TONELLI D,PREVOT V, MOUSTY C. Electrodeposition of layereddouble hydroxides on platinum: Insights into the reactionssequence [J]. Electrochimica Acta, 2015, 152: 75−83.[24]SHANGGUAN E B, LI J, GUO D, GUO L T, NIE M Z,CHANG Z R, YUAN X Z, WANG H J. A comparative studyof structural and electrochemical properties of high-densityaluminum substituted α-nickel hydroxide containing different interlayer anions [J]. Journal of Power Sources,2015, 282: 158−168.[25]YAO K L, ZHAI M H, NI Y H. α-Ni(OH)2∙0.75H2Onanofilms on Ni foam from simple NiCl2solution: Fastelelctrodeposition, formation mechanism and application asan efficient bifunctional electrocatalyst for overall watersplitting in alkaline solution [J]. Electrochimica Acta, 2019,301: 87−96.[26]PAN T. Preparation of stabilized α-Ni(OH)2by cathodicelectrodeposition [D]. Hangzhou: Zhejiang University, 2003.(in Chinese)[27]YA VUZ A, ERDOGAN P Y, OZDEMIR N, ZENGIN H,ZENGIN G, BEDIR M. Electrochemical synthesis of CoOOH−Co(OH)2composite electrode on graphite currentcollector for supercapacitor applications [J]. Journal ofMaterials Science: Materials in Electronics, 2019, 30:18413−18423.[28]RAMESH T N, VISHNU KAMATH P. Synthesis of nickelhydroxide: Effect of precipitation conditions on phaseselectivity and structural disorder [J]. Journal of PowerSources, 2006, 156: 655−661.[29]MIYAATA S. Anion-exchange properties of hydrotalcite-likecompounds [J]. Clays and Clay Minerals, 1983, 31: 305−311.[30]LI H L, LIU S Q, HUANG C H, ZHOU Z, LI Y H, FANG D.Characterization and supercapacitor application of coin-likeβ-nickel hydroxide nanoplates [J]. Electrochimica Acta, 2011,58: 89−94.[31]ANDRATE T M, DANCZUK M, ANAISSI F J. Effect of。
三氧化钼应用为锂离子电池负极材料研究综述

三氧化钼应用为锂离子电池负极材料研究综述谢三木1余飞2廖心2(1.广州铁路职业技术学院 广东广州 511300;2.中国铁路广州局集团有限公司广州动车段 广东广州 511400)摘要:锂离子电池由于其具备的高能量密度、较长的循环寿命和无记忆效应等优点被广泛应用在储能领域。
传统商用锂离子电池石墨负极理论容量为372 MAh/g,这极大地限制了电池性能的进一步发展。
三氧化钼负极由于其具备较高的理论容量和特殊的电化学性质而备受关注,但仍存在着如导电性差、循环和倍率性能差等缺点。
基于此,通过梳理近年来关于三氧化钼应用为锂离子电池负极的研究,综述了多种提升三氧化钼电极材料性能的方法,以期为后续的研究作为参考。
关键词:锂离子电池 负极三氧化钼 纳米材料 电极材料中图分类号:O64文献标识码:A 文章编号:1672-3791(2023)24-0073-03A Research Review of the Application of Molybdenum Trioxide asthe Negative Electrode Material of Lithium-Ion BatteriesXIE Sanmu1YU Fei2QUAN Ming2(1.Guangzhou Railway Polytechnic, Guangzhou, Guangdong Province, 511300 China; 2.Guangzhou EMU Depot,China Railway Guangzhou Group Co., Ltd., Guangzhou, Guangdong Province, 511400 China) Abstract:Lithium-ion batteries are widely used in the field of energy storage due to their advantages such as high energy density, long cycle life and memoryless effects. The theoretical capacity of the graphite anode of traditional commercial lithium-ion batteries is 372 MAh/g, which greatly limits the further development of battery perfor‐mance. The molybdenum oxide negative electrode has attracted much attention due to its high theoretical capacity and special electrochemical properties, but there are still shortcomings such as poor conductivity and poor cycling and rate performance. Based on this, this article sorts out recent research on the application of molybdenum oxide as the negative electrode of lithium-ion batteries, and reviews various methods to improve the performance of mo‐lybdenum trioxide electrode materials, with the aim of serving as a reference for subsequent research.Key Words: Lithium-ion batteries; Negative electrode; Molybdenum trioxide; Nano materials; Electrode material1 研究背景锂离子电池负极作为电池的重要组成部分,对电池的电化学性能起着决定性作用。
电镀工艺术语中英文对照
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电解抛光和离子薄化法联合制备纳米晶双相稀土永磁合金TEM样品(1)
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实验结果及讨论 图 l 是我们经过上述实验方法所获得的透射电
镜照片, 从图 l 中可清晰地看出纳米晶双相稀土永 磁合金的纳米晶粒的大小; 图 2 是纳米晶双相稀土 永磁合金晶粒中的亚结构。 我们在实验中也曾试验直接用电解双喷法来制 备纳米晶双相稀土永磁合金, 但在制作完成后进行 供分析用的有效组织范围 的 TEM 透射电镜分析时, 十分有限, 且材料明显有氧化现象。同时, 在电解制 电解双喷的喷 作过程中, 由于温度在 0 ~ 5C 范围, 枪的聚中很可能因为热胀冷缩而变形, 导致材料在 双喷中电解液无法聚中分析样品的中心部分, 从而 使电解双喷制备 TEM 分析样品失败。 利用离子薄化技术单一进行离子轰击, 虽能获 得比较满意的透射电镜观察效果, 但离子薄化所制 工作效率极低。 备的一个 TEM 用的样品需 7 ~ l31, 总之, 采用电解抛光和离子薄化法联合制备纳 米晶双相稀土永磁合金 TEM 样品的实验方法是可 行的, 该方法不仅对制备纳米晶双相稀土永磁合金 有效, 对解决所分析的材料在其宽度小于 3 mm 时, 也应是十分有效的制备 TEM 样品的参考方法之一。 由于双喷电解液对分析样品表面的冲击, 可能 会造成因纳米晶双相稀土永磁合金样品脆性而发生 碎裂, 致使制作纳米晶双相稀土永磁合金 TEM 产品 失败。因此, 在进行电解双喷时, 使双喷电解液流速 应尽可能偏少, 才有利于保持纳米晶双相稀土永磁 合金样品表面不被电解液冲击而碎裂。
电子显微学报
J. Chin. EIectr. MicroSc. Soc. 2002 年
(5) 21 1 840 ~ 841
8ห้องสมุดไป่ตู้1
参考文献:
[ 1 ]李巧玲, 叶云 . 电子显微学报, ,5) : 1999( 567-568 .
电极界面浓差极化对锂金属沉积的影响
物 理 化 学 学 报Acta Phys. -Chim. Sin. 2021, 37 (2), 2009001 (1 of 7)Received: September 1, 2020; Revised: September 27, 2020; Accepted: September 30, 2020; Published online: October 21, 2020. *Correspondingauthors.Emails:*******************.cn(Y.Z.);***************(F.D.).The project was supported by the Foundation of National Key Laboratory of China (6142808180202), the Pre-Research Foundation of China (61407210406, 61407210208, and 41421080401), and the Open Fund of Jiangsu Key Laboratory of Electrochemical Energy Storage Technologies (EEST2019-1).国防科技重点实验室基金(6142808180202), 装备预研领域基金(61407210406, 61407210208, 41421080401)和江苏省高效电化学储能技术重点实验室开放基金(EEST2019-1)资助项目© Editorial office of Acta Physico-Chimica Sinica[Article] doi: 10.3866/PKU.WHXB202009001 Influence of Interfacial Concentration Polarization on Lithium Metal ElectrodepositionYitao He 1, Fei Ding 2,*, Li Lin 3, Zhihong Wang 1, Zhe Lü 1, Yaohui Zhang 1,*1 School of Physics, Harbin Institute of Technology, Harbin 150001, China.2 Science and Technology on Power Sources Laboratory, Tianjin Institute of Power Sources, Tianjin 300384, China.3 Wuhan Institute of Marine Electric Propulsion, Wuhan 430064, China.Abstract: As an ideal negative electrode material for next-generation high-energy-density batteries, lithium (Li) metal has received extensive attention from the global research community. However, the safety hazards and short cycle life caused by the growth of Li dendrites have seriously hampered the application of Li metal batteries. Based on electrochemical phenomena and theory, this paper discusses the mechanism of dendritic growth, dead Li formation, and full battery failure from the perspective of concentration polarization. During the electrodepositionprocess, the consumption of Li ions on the surface induces concentration polarization. After the initial deposition, a relatively loose dendrite layer appears on the Li metal surface; the electrolyte can penetrate this dendrite layer to reach the dense Li metal surface. When the grown dendrites penetrate the concentration polarization layer, the interface concentration battery is short-circuited. In this case, the concentration difference battery tends to release all stored power and reach a potential balance between the high- and low-concentration regions, which causes the deposition of Li ions over the dendrites to reduce the ion concentration in the surrounding electrolyte. Meanwhile, the dissolution of Li ions that occurs at the roots of the dendrites increases the local ion concentration. This process accelerates the formation of a dead Li layer. A similar electrochemical process often occurs in columnar Li, as reported in other studies. When columnar Li is cycled several times, each Li column degenerates into a matchstick shape with a large head and thin neck. Therefore, eliminating concentration polarization is necessary for the application of columnar Li. Furthermore, in this work, concentration polarization and dendrite suppression in state-of-the-art porous host electrodes are analyzed. The larger specific surface area of the porous electrode greatly reduces the local current density on the electrode surface, which can reduce the interface concentration polarization and thus prevent dendrite growth. In charge-discharge cycling, a constant-voltage charging or shelving step is often inserted in each cycle in order to eliminate the influence of concentration polarization. However, if a dendritic layer has been formed on the Li metal surface after charging, in addition to the self-diffusion of ions, the self-discharge process of the interface concentration battery causes the detachment of the dendrite layer, thus resulting in the above-mentioned dead Li. Therefore, a larger amount of deposited Li yields a thicker Li dendritic layer, thus accelerating the capacity decay and failure of the battery, especially to those with high-capacity, high-voltage positive electrodes. The conclusions obtained in this paper can provide a theoretical basis for researchers to further explore Li metal protection strategies.Key Words: Lithium metal; Concentration polarization; Dendrite suppression; Interface concentration differencebattery; Porous host electrode电极界面浓差极化对锂金属沉积的影响何一涛1,丁飞2,*,林立3,王志红1,吕喆1,张耀辉1,*1哈尔滨工业大学物理学院,哈尔滨 1500012天津电源研究所化学与物理电源重点实验室,天津 3003843武汉船用电力推进装置研究所,武汉 430064摘要:锂金属作为下一代高能量密度电池的理想负极材料受到研究人员广泛关注。
电化学脱合金的英文
电化学脱合金的英文Electrochemical Dealloying: Principles, Applications, and Challenges.Introduction.Electrochemical dealloying is a process that involves the selective removal of one or more constituent metalsfrom a multicomponent metallic alloy by electrochemical means. This process, often referred to as "dealuminization" in the context of aluminum-based alloys, has found widespread applications in materials science, nanotechnology, and energy conversion and storage systems. The primary advantage of electrochemical dealloying lies in its ability to create nanostructured materials with unique physical and chemical properties, such as high surface area, porosity, and conductivity.Principles of Electrochemical Dealloying.The electrochemical dealloying process occurs when an alloy is immersed in an electrolyte solution and apotential is applied between the alloy and a counter-electrode. The applied potential drives the electrochemical reactions at the alloy surface, resulting in thedissolution of one or more constituent metals. The dissolution rate of each metal depends on its electrochemical properties, such as the redox potential and electrochemical activity in the given electrolyte.During the dealloying process, the alloy is typically the anode, and the counter-electrode is the cathode. The anode is connected to the positive terminal of the power source, while the cathode is connected to the negative terminal. When the potential is applied, the alloy begins to dissolve, and the dissolved metal ions migrate towards the cathode. At the cathode, the metal ions are reduced and deposited on the surface, forming a new metal layer.The rate of metal dissolution during electrochemical dealloying is controlled by several factors, including the electrolyte composition, applied potential, temperature,and alloy composition. By optimizing these parameters, researchers can precisely control the morphology, porosity, and composition of the resulting nanostructured materials.Applications of Electrochemical Dealloying.Electrochemical dealloying has found numerous applications in materials science and engineering. Some of the key applications are discussed below:1. Nanoporous Metals: Electrochemical dealloying is widely used to create nanoporous metals with high surface area and porosity. These materials exhibit unique physical and chemical properties that are beneficial in various applications, such as catalysis, sensors, and energy storage.2. Battery Materials: Nanoporous metals produced by electrochemical dealloying have been explored as anode materials for lithium-ion batteries. The high porosity and surface area of these materials enhance the lithium storage capacity and improve the battery's performance.3. Fuel Cells: Electrochemical dealloying has also been used to create nanostructured catalysts for fuel cells. These catalysts exhibit enhanced activity and durability, which are crucial for efficient fuel cell operation.4. Biomedical Applications: Nanoporous metals produced by electrochemical dealloying have potential applicationsin biomedicine, such as drug delivery, tissue engineering, and implant materials. The porous structure of these materials allows for controlled drug release and improved cell adhesion and growth.Challenges and Future Directions.Despite the significant progress made inelectrochemical dealloying, several challenges remain to be addressed. One of the primary challenges is the control of the dealloying process at the nanoscale, as it is crucialfor achieving the desired material properties. Additionally, the development of new electrolytes and optimization of dealloying parameters are ongoing research efforts.Future research in electrochemical dealloying could focus on exploring new alloy systems, optimizing the dealloying process for specific applications, and understanding the fundamental mechanisms underlying metal dissolution and nanostructure formation. Furthermore, the integration of electrochemical dealloying with other nanotechnology approaches, such as lithography and templating, could lead to the development of even more advanced materials with tailored properties.Conclusion.Electrochemical dealloying is a powerful technique for creating nanostructured materials with unique physical and chemical properties. Its applications span multiple fields, including materials science, energy conversion and storage, and biomedicine. While significant progress has been madein this field, there are still numerous challenges and opportunities for further research and development. With the advancement of nanotechnology and materials science, electrochemical dealloying holds promise for enabling thecreation of next-generation materials with improved performance and functionality.。
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Electrochimica Acta51(2006)3776–3780Electrodeposition of metallic molybdenumfilms inZnCl2–NaCl–KCl–MoCl3systems at250◦CHironori Nakajima,Toshiyuki Nohira∗,Rika HagiwaraDepartment of Fundamental Energy Science,Graduate School of Energy Science,Kyoto University,Sakyo-ku,Kyoto606-8501,JapanReceived1July2005;received in revised form25October2005;accepted25October2005Available online2December2005AbstractMolybdenum metalfilm has been electrodeposited in ZnCl2–NaCl–KCl(0.60:0.20:0.20,in mole fraction)melt containing MoCl3at250◦C.In this melt,a densefilm was obtained by potentiostatic electrolysis at0.15V versus Zn(II)/Zn for3h.However,thefilm had a thickness of smaller than0.5m and was not adhesive.On the other hand,addition of4mol%of KF to the melt led to larger cathodic current in cyclic voltammogram, and gave a dense,adhesive and thicker metalfilm of ca.3m thickness in the same electrolysis condition as above.The present process is promising as a new method for molybdenum coating at low temperatures.©2005Elsevier Ltd.All rights reserved.Keywords:Electrodeposition;Molten salt;ZnCl2–NaCl–KCl;Molybdenum metalfilm;Molybdenum chloride;Fluoride ion1.IntroductionElectrodeposition of refractory metals such as tungsten, molybdenum,tantalum at low temperatures has many advan-tages from an engineering point of view.One of the promis-ing applications is the LIGA(Lithographie Galvanoformung Abformung,German abbreviation)process,a micro-fabrication technique consisting of lithography,electroforming and molding [1–6].Although many products have already been commercially produced with this method,applicable materials are limited to metals that are able to be electrodeposited in aqueous elec-trolytes such as copper,gold,nickel and Ni–Fe alloys[1–6]. Refractory metals are highly expected to be used for the elec-troforming step of LIGA process owing to their high hardness and high mechanical-strength.It is also very promising to coat the conventional LIGA parts with refractory metals by elec-trodeposition.However,electrodeposition of them has not been achieved except for chromium in aqueous solutions mostly due to the narrow electrochemical window of water.If the applica-tion of refractory metals to the LIGA process is realized,it would much contribute to improve the performance and reliability of the Micro-Electro-Mechanical Systems(MEMS)devices.∗Corresponding author.Tel.:+81757534817;fax:+81757535906.E-mail address:nohira@energy.kyoto-u.ac.jp(T.Nohira).Senderoff and Mellors have obtained refractory metals including molybdenum in alkali metalfluoride melts at 700–850◦C[7,8].Since then,refractory metals have been obtained in chloride,fluoride and oxide melts above500◦C [9,10].Katagiri et al.succeeded in obtaining metallic tungsten at 350–450◦C using ZnBr2–NaBr[11,12]and ZnCl2–NaCl melts [12,13].However,electrodeposition of smooth and dense refrac-tory metals becomes more and more difficult as the operation temperature decreases.To date,such electrodeposition of refrac-tory metals at temperatures below350◦C have not been reported except for the case of chromium.However,electrodeposition of metals must be made at and lower than250◦C for the LIGA process due to the limit of heat resistance of the resist sheet made of polymethylmethacrylate.For coating the LIGA parts, electrodeposition should be carried out at temperatures as low as possible to avoid the softening of the substrate materials. Thus,we have been studying the electrodeposition of refrac-tory metals in molten salts at around250◦C[14].It should be noted that metallic molybdenum deposit has not been obtained below550◦C[10].We selected a molten ZnCl2–NaCl–KCl eutectic(ZnCl2:NaCl:KCl=0.60:0.20:0.20,in mole fraction; mp:203◦C[15])as an electrolyte.The melts containing KF were also examined sincefine molybdenum deposits have been obtained influoride melts at high temperature in the previous works[9,10],which is possibly related to the formation offlu-oro complex ions.0013-4686/$–see front matter©2005Elsevier Ltd.All rights reserved. doi:10.1016/j.electacta.2005.10.041H.Nakajima et al./Electrochimica Acta 51(2006)3776–378037772.ExperimentalA schematic drawing of the experimental apparatus is shown in Fig.1.The experiments were conducted in an argon-filled glove box with a gas circulating purifier (MIW A MFG Co.,Ltd.).All the chemicals were anhydrous reagent grade.The eutectic mixture of ZnCl 2(99.9%,Wako Pure Chemical Industries,Ltd.),NaCl and KCl (99.5%each,Wako Pure Chemical Industries,Ltd.)was prepared (ZnCl 2:NaCl:KCl =0.60:0.20:0.20,in mole fraction),and then dried in a furnace under vacuum at 130◦C for 3days or more.After that it was melted at 250◦C in a glass beaker (Shibata Hario Glass Co.)installed in a four-necked sep-arable flask on a heating plate.A band shape heater was wound around the beaker to have uniform temperature distribution by heating.MoCl 3(99.5%,Alfa Acer)was added in the melt as a molybdenum ion source.KF (99%,Wako Pure Chemical Indus-tries,Ltd.)was added as a fluoride ion source.The working electrode was a nickel plate (99.7%,5mm ×10mm ×0.2mm,Furuuchi Chemical Corp.)that was fully immersed in the melt.The nickel plate was electrochemi-cally polished in a sulfuric acid then immersed in an acid cleaner containing NaHF2(Kizai Corp.,Kokeisan B)to remove surface oxides.The counter electrode was a glassy carbon rod (3mm,Tokai Carbon Co.,Ltd.,GC-20).A zinc wire (99.99%,0.5mm,Fig.1.Schematic drawing of experimental apparatus.(A)Thermocouple;(B)working electrode;(C)reference electrode;(D)counter electrode;(E)separable flask;(F)Pyrex beaker;(G)band heater;(H)ZnCl 2–NaCl–KCl melt;(I)heating plate.Nilaco Corp.)immersed in the melt was used for the refer-ence electrode.A chromel–alumel thermocouple was used for the temperature measurement.Cyclic voltammetry with positive feedback IR compensation and potentiostatic electrolysis were performed using electrochemical measurement systems (Hokuto Denko Co.,Ltd.,HZ-5000).After the electrolysis,the electrodes were immersed in acetone,then,rinsed with distilled water to remove adherent salts.The deposits were characterized by scanning electron microscopy (SEM,Hitachi,S-2600H),energy dispersive X-ray analysis (EDX,Horiba Co.,Ltd.,EMAX ENERGY EX-200),X-ray diffraction (XRD,Rigaku Industrial Co.,Ltd.,Multi Flex)with CuKa radiation and X-ray photoelectron spectroscopy (XPS,Shimadzu Co.,Ltd.,ESCA-3200).3.Results and discussion3.1.Electrodeposition of metallic molybdenum in ZnCl 2–NaCl–KCl–MoCl 3melt3.1.1.Cyclic voltammetryFig.2shows a cyclic voltammogram at the nickel plate elec-trode in ZnCl 2–NaCl–KCl–MoCl 3(0.05mol kg −1added)melt at 250◦C.A blank voltammogram obtained for the sameelec-Fig.2.(a)Cyclic voltammograms for nickel electrodes in ZnCl 2–NaCl–KCl and ZnCl 2–NaCl–KCl–MoCl 3(0.05mol kg −1added)melts at 250◦C.Scan rate:0.05V s −1.(b)The same voltammogram with a current density axis of smaller scale.3778H.Nakajima et al./Electrochimica Acta51(2006)3776–3780 trode in the melt without MoCl3is shown for comparison.TheseCVs were recorded after several cycles.In both the plots,acathodic current shoulder is observed at around0.03V as wellas an anodic current peak at around0.12V.They are attributedto the formation and dissolution of Ni–Zn alloy,respectively[14].Cathodic and anodic currents around0V in both theplots are attributed to the deposition and dissolution of metalliczinc,respectively.In the ZnCl2–NaCl–KCl–MoCl3melt,a newcathodic wave,C1,is also observed in the potential range of0.04–0.42V,suggesting the electrodeposition of molybdenum.The formations of Zn–Mo and/or Ni–Mo alloys are also takenaccount from the phase diagrams[16].3.1.2.Potentiostatic electrolysis and characterization of thedepositSince electrodeposition of molybdenum was suggested tooccur in the potential region of lower than0.42V,potentiostaticelectrolysis was performed at0.15V for3h,where deposition ofmolybdenum was expected whereas that of metallic zinc or theformation of Ni–Zn alloy was not.After the potentiostatic elec-trolysis,a blackfilm was deposited.However,only a small areaof the substrate was covered due to bad adhesion.Fig.3shows aspectrum of XPS of Mo3d for thefilm.Mo3d3/2and Mo3d5/2peaks corresponding to metallic molybdenum are observed at231and228eV,respectively[17].Thefilm is,thus,identifiedas metallic molybdenum.It is also confirmed that the Zn–Moand/or Ni–Mo alloys are not formed.EDX results showed thatchloride content in thefilm was lower than2at.%,indicating thatthe melt inclusion is not significant.On the other hand,an XRDpattern did not show any distinctive peaks corresponding to ametallic molybdenum crystal[18].This is likely to be caused bythe too small thickness and/or low crystallinity of thefilm.Fig.4shows a surface SEM image of thefilm,where sphericalparticles and microcracks are observed.The spherical particlesare observed as light gray because the oxidation by rinsing withthe water may have proceeded larger extent compared withtheFig. 3.An Mo3d XPS spectrum of a deposit obtained after potentio-static electrolysis at0.15V vs.Zn(II)/Zn for3h in ZnCl2–NaCl–KCl–MoCl3 (0.05mol kg−1added)melt at250◦C.Argon ion etching time:5000s.Fig.4.A surface SEM image of a deposit obtained after potentiostatic electrol-ysis at0.15V vs.Zn(II)/Zn for3h in ZnCl2–NaCl–KCl–MoCl3(0.05mol kg−1 added)melt at250◦C.flat part.The microcracks indicate that tensile stress is gener-ated on the depositedfilm.There are two possibilities for the tensile stress.One is the coefficient of thermal expansion(CTE) mismatching and the other is the deposition-induced internal stress.The CTE mismatching is excluded since CTE of nickel is larger than that of molybdenum,which gives rise to compressive stress.Thus,the microcracks would be produced by the deposi-tion induced tensile stress.The observation of theflakes of the film showed that it was dense but had a thickness lower than 0.5m.The metallic molybdenum is also obtained at0.40V, which was confirmed by XPS analysis.Hence,it is confirmed that cathodic currents at potentials lower than0.42V result from the electrodeposition of molybdenum.3.2.Electrodeposition of metallic molybdenum inZnCl2–NaCl–KCl–MoCl3–KF melt3.2.1.Cyclic voltammetryThe melts containing KF were examined sincefine molyb-denum deposits have been obtained influoride melts at high temperatures[9,10].Fig.5shows a cyclic voltammo-gram at a nickel electrode in ZnCl2–NaCl–KCl–KF(4mol% added)–MoCl3(0.05mol kg−1added)melt at250◦C.A curve for the melt added only KF to the blank melt is also shown for comparison.They were recorded after several cycles.Addi-tion of KF to the blank melt causes no distinctive change in the potential region examined in the present study.In the ZnCl2–NaCl–KCl–KF–MoCl3melt,a cathodic wave,C2,is observed in the potential region of0.04–0.45V.This current is possibly due to the electrodeposition of metallic molybde-num,which is approximately three times larger than those in the melt without KF.The shape change in the cyclic voltamme-try in the potential region of0–0.03V shows the suppression of both the deposition of metallic zinc and the formation of the Ni–Zn alloy,which coincides with the relatively large amount of molybdenum deposition at the electrode.In these potentialH.Nakajima et al./Electrochimica Acta 51(2006)3776–37803779Fig.5.Cyclic voltammograms for nickel electrodes in ZnCl 2–NaCl–KCl and ZnCl 2–NaCl–KCl–KF–MoCl 3(0.05mol kg −1added)melts at 250◦C.Scan rate:0.05V s −1.Starting potential for the ZnCl 2–NaCl–KCl–KF–MoCl 3melt:0.59V vs.Zn(II)/Zn.regions,the possibilities of the formations of the Zn–Mo and/or Ni–Mo alloys cannot be dismissed.3.2.2.Potentiostatic electrolysis and characterization of the depositSince electrodeposition of molybdenum was suggested in the potential region lower than 0.4V ,potentiostatic electrolysis was performed at 0.15V for 3h.A black film was deposited and its adhesion was better than that of the film obtained in the previous section.Fig.6shows an XRD pattern for the film.In this case,a diffract pattern is ascribed to metallic molybdenum [18].It is also confirmed by XPS analysis that no Zn–Mo and Ni–Mo alloys are formed.EDX results revealed that the chloride con-tent in the film is lower than 1at.%,indicating that the melt inclusion is also minimized in this case.Fig.7(a)shows a sur-face SEM image of the film.Although the surface was covered with spherical particles,the deposited molybdenum layer seems dense.The formation of the microcracks is also explained by the deposition-induced internal stress as the case for the melt without KF.However,the number and gaps of the microcracks markedly decreased with addition of KF.Fig.7(b)shows across-Fig.6.An XRD pattern of a deposit obtained after potentiostatic electrolysis at 0.15V vs.Zn(II)/Zn for 3h in ZnCl 2–NaCl–KCl–MoCl 3(0.05mol kg −1added)melt at 250◦C.Fig.7.(a)A surface SEM image and (b)a cross-sectional SEM image of a deposit obtained after potentiostatic electrolysis at 0.15V vs.Zn(II)/Zn for 3h in ZnCl 2–NaCl–KCl–KF (4mol%added)–MoCl 3(0.05mol kg −1added)melt at 250◦C.sectional SEM image of the film.Although the molybdenum film contains a few fine microcracks,it is almost dense and has the average thickness of approximately 3m.The improve-ment in adhesiveness,thickness and microcracks by addition of KF should be related to the change of complex structure of molybdenum species in the melt,such as the formation of fluoro or chloro–fluoro complex.This effect is now under investiga-tion by Raman spectroscopy.The microcracks will be reduced further by the other additives and/or the other electrolysis con-ditions such as the pulse technique.The electrodeposition rate observed,3m per 3h,is not large enough to apply this process directly to the electroforming step of the LIGA process.How-ever,further improvements on this process is expected because there are much room for increasing the electrodeposition rate,for example,by increasing the molybdenum composition in the melt,introducing the pulse electrodeposition technique,etc.The present method can be applied with minor improvements for3780H.Nakajima et al./Electrochimica Acta51(2006)3776–3780coating of a variety of substrates with molybdenum including the conventional LIGA parts.4.ConclusionMetallic molybdenumfilm was deposited by potentio-static electrolysis in ZnCl2–NaCl–KCl eutectic melt containing MoCl3at250◦C.In this melt,thefilm was dense,but was not adhesive.On the other hand,addition of4mol%of KF to the melt gave a dense,adhesive and thicker metal deposit in the same condition as above.The present process is promising as a new method for molybdenum coating at low temperatures such as the coating on the conventional LIGA parts.AcknowledgmentsThis study was supported by Industrial Technology Research Grant Program in2003from the New Energy and Industrial Technology Development Organization(NEDO)of Japan.We thank Sumitomo Electric Industries,Ltd.for theirfinancial and technical supports.References[1]E.W.Becker,W.Ehrfeld,P.Hagmann,A.M.D.Maner,Microelectron.Eng.4(1986)35.[2]A.Rogner,J.Eicher, D.M¨u nchmeyer,R.-P.Peters,J.Mohr,J.Micromech.Microeng.2(1992)133.[3]J.Hormes,J.G¨o 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