共查询到16条相似文献,搜索用时 171 毫秒
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陶瓷电容器化学镀铜的研究 总被引:1,自引:0,他引:1
陶瓷电容器化学镀铜的研究袁永明万家义王惠萍(四川大学化学系成都610064)关键词陶瓷电容器以铜代银化学镀中图分类号O69陶瓷电容器是最基本的电子元件,目前国内外大都采用涂银(印银)-烧银法制作银电极。这种方法需要消耗大量的贵金属银,设备投资贵、成本... 相似文献
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电位活化现象与金属电沉积初始过程的研究 总被引:12,自引:0,他引:12
进行了恒电流电位-时间曲线和循环伏安曲线的测定,显示了铁电极进行氰化物镀铜时,镀层沉积前铁表面的电位活化过程. 对铁电极上焦磷酸盐镀铜的初始过程研究表明,由于铜的析出电位较正,铜是在未活化的电极表面上沉积的,因此镀层的结合强度很差.采用氩离子溅射和X射线光电子能谱相结合的方法,检测焦磷酸盐镀铜层和铁基体界面区含氧量的变化,证明了氧化层的存在. 通过添加辅助络合剂和控制起始电流密度的方法,可以增强无氰电镀时阴极的极化. 当铜的析出电位负于铁基体的活化电位时,可显示出铁表面的电位活化过程,定量测量镀层的结合强度也与氰化物电镀相近. 相似文献
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通过研究塑料化学镀铜的时间与铜沉积速率的关系,使学生理解甲醛作为还原剂进行塑料化学镀铜的原理;同时,掌握研究问题的方法和思路,为以后进行课程设计或进行研究性工作奠定基础。 相似文献
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在化学镀铜溶液中,p-Si片在波长为514.5nm的激光束的照射下,得到了选择性的铜镀层。采用AES、SEM、RBS和电学技术对比了在3种含不同还原剂的镀液中得到的镀层的形貌、组成、界面扩散及电学性质,探讨了液相激光诱导化学沉积铜的机理。 相似文献
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以分布有微孔的印刷线路板(PCB)作为模板,按照PCB孔金属化工艺路线,研究乙醛酸化学镀铜和柠檬酸盐体系铜电沉积工艺在PCB微孔金属化中的应用.结果表明,乙醛酸化学镀铜和柠檬酸盐体系电沉积铜可以成功地应用于PCB微孔金属化加工工艺中.微孔化学镀铜金属化导电处理后,铜附着于微孔内壁,颗粒细小,但排列疏松且局部区域发生漏镀现象.微孔一经电镀铜加厚,镀层电阻显著下降;孔壁内外的铜沉积速率达到0.8:1.0;铜颗粒具有一定的侧向生长能力,能够完全覆盖化学镀铜时产生的微小漏镀区域;微孔内壁铜镀层连续、结构致密并紧密附着于内壁,大大增强了PCB上下层互连的导电性能. 相似文献
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随着半导体集成度的不断提高,铜互连线的电阻率迅速提高。当互连线宽度接近7 nm时,铜互连线的电阻率与钴接近。IBM和美国半导体公司(ASE)已经使用金属钴取代铜作为下一代互连线材料。然而,钴种子层的形成和超级电镀钴填充7 nm微孔的技术工艺仍是一个很大的挑战。化学镀是在绝缘体表面形成金属种子层的一种非常简单的方法, 通过超级化学镀填充方式, 直径为几纳米的盲孔可以无空洞和无缝隙的方式完全填充。本文综述了化学镀钴的研究进展,并分析了还原剂种类对化学镀钴沉积速率和镀膜质量的影响。同时, 在长期从事超级化学填充研究的基础上, 作者提出了通过超级化学镀钴技术填充7 nm以及一下微盲孔的钴互连线工艺。 相似文献
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在以酒石酸钾钠和乙二胺四乙酸二钠为双配位剂、 甲醛为还原剂的化学镀铜液中, 研究了5,5-二甲基乙内酰脲(DMH)在化学镀铜中的作用. 化学镀铜实验结果表明, DMH提高了镀液的稳定性; 扫描电子显微镜(SEM)结果表明, DMH使镀层颗粒尺寸减小, 镀层光亮致密; 紫外-可见光谱结果表明, DMH在镀液中与Cu(II)不发生强配位作用; 线性伏安扫描结果表明, DMH在化学镀铜过程中能抑制Cu+的产生或促进Cu+快速还原, 降低甲醛的氧化速率; X射线衍射(XRD)结果表明, 在含和不含DMH化学镀铜液中, 得到的铜镀层均呈现面心立方混晶结构的特征, 且未出现Cu2O夹杂衍射峰. 相似文献
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Comparison of Bottom-up Filling in Electroless Plating with an Addition of PEG,PPG and EPE 总被引:1,自引:0,他引:1
The bottom‐up filling capabilities of electroless copper plating bath with an addition of additives, such as polyethylene glycol (PEG), polypropylene glycol (PPG) and triblock copolymers of PEG and PPG with ethylene oxide terminal blocks termed EPE, were investigated by the cross‐sectional scanning electron microscopy (SEM) observation of sub‐micrometer trenches. Though three additives had inhibition for electroless copper deposition, the suppression degrees of three additives were different. EPE‐2000 had the strongest suppression for electroless copper deposition, and the suppression of PEG‐2000 was the weakest. The bottom‐up filling capability of electroless copper was investigated in a plating bath containing different additives with the concentration of 2.0 mg/L. The cross‐sectional SEM observation indicated the trenches with the width of 280 nm and the depth of 475 nm were all completely filled by the plating bath with an addition of EPE‐2000, but the trenches were not completely filled by the plating bath with an addition of PEG‐2000 or PPG‐2000, and some voids appeared. Linear sweep voltammetry measurement indicated that three additives all inhibited the cathodic reduction reaction and the anodic oxidation reaction, and the inhibition of EPE‐2000 was the strongest among three additives, which agreed with that of the deposition rate of electroless copper. Significant differences in surface roughness of deposited copper film were observed by UV‐visible near‐infrared for different suppressors, and the bright and smooth of deposited copper film were in accordance with the inhibition of three additives. 相似文献
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化学镀镍诱发过程的研究 I:金属催化活性的鉴别和反应机理 总被引:5,自引:0,他引:5
Electroless plating is known to be an autocatalytic process. For the reaction to start, the substrate metall should be either catalytic or activated by a suitable catalyst. For example, steel and nickel can be plated directly, but in the case of copper or brass, catalytic metal inducing is need. In this paper, the catalytic activity of different metals and their inducing effects were in vestigated by measuring stationary potentials nd stationary potential-time curves. Experimental results showed: (1) The stationary potential of metal provides a simple parameter to estimate the catalytic activity of metals in electroless nickeling. When 1-hydroxyethylidenediphosphonic acid (HEDP) aelectroless nickeling bath containing NaH2PO2 as reducing agent is used, electrolessnickeling may proceed spontaneously, if the stationary potential of metal is more nagative than -0.60V, no matter whether nickel (autocatalytic active) or other metals(non-autocatalytic active) is used as substrate. (2)When an autocatalytic meta is in contact with the substrate metal in the bath, a sudden decrease of stationary potential is observed. The whole inducing process could be finished within 0.5-2 sec. (3) The stationary potential of electroless nickeling coating in HEDP bath at 80`C is-0.72V, consequently nickel coating itself is a catalytic active metal. Once an electroless nickeling coating is deposited on a substrate metal, electroless nickeling reaction can then proceed continuously. (4) The sufficient conditions of electroless nickeling in HEDP bath containing NaH2PO2 are that the stationary potential of substrate metal must be more nagative than -0.60V and that the temperature of electroless nickeling bath should be higher than 50`C. (5) Inducing mechanism of electroless nickeling can be explained with chemical cell consisting of substrate metal and catalytic metal. Electrons from catalytic metal would suddenly decrease the stationary potential of substrate metal, H+ and Ni2+ complex ion would be reduced on the substrate me 相似文献
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