Dual Bath Electrodeposition of Alternate Multilayer Coatings of Zinc and Nickel Deposits

ZINC electroplating is well established as a sacrificialcoating for the protection of steel substrates.Nevertheless,such coatings deteriorate and areconsumed quickly in severely corrosive environments.Increasing the thickness of pure zinc coating orimproving the passivation methods after plating mayenhance the corrosion resistance,but there are stillproblems during forming and post-deposition weldingprocesses"'.Recently,a new class of coatingsconsisting of a large number of alternate layers h…     

Effect of borate coating on corrosion resistance of pure nickel in molten LiCl-Li2O

1　INTRODUCTIONAttheendofthetwentiethcentury ,alithiumreductiontechniquewasdevelopedtodisposeofnucle arfuel(UO2 )used[1] .Inthis process ,theoxide(UO2 )isreducedtothemetallicform(U)byreactionwithlithiumdissolvedinmoltenLiClat 75 0℃ .Thetechniquecaneffectivelyreducethevolumeandradia tionofspentnuclearfuel,whichisconvenienttostoreandmanage .Unfortunately ,thecontainmentmaterialsusedinthetechniqueundertakeseverecor rosionowingtothestrongbasicoxideLi2 OformedanddissolvedinmoltenLiCl.Sev…     

TiB2 coating formed on nickel substrates by electroplating in molten salt of fluoride

The TiB2 coatings deposited over nickel substrate by electroplating was investigated, which is in molten salt of a fluoride mixture involving KF, NaF, K2 TiF6 and KBF4. Effects of temperature, cathodic current density (Jc) and duration on the coating's formation were examined. The composition, morphology and structure of the coatings were characterized by scanning electron microscopy (SEM), energy dispersive X-ray detector (EDS) and X-ray diffraction (XRD). The results show that the coatings, with black, smooth and uniform appearance, are composed of predominating TiB2 and small amounts of nickel titanium oxide (Ni0.75 Ti0.125 O). The coatings show a nodular morphology and the grain size is dependent on the Jc and ranges about 1 - 10 μm. There is a linear relationship between the coating's thickness and the time of electrolysis within certain duration range. The reduction of the potassium can take place simultaneously with the electrochemical synthesis of TiB2 as the Jc is in excess of certain level. The hardness of the TiB2 coatings is likely to be deteriorated due to the presence of potassium and Ni0.75Ti0.125 O in the coatings.     

钛基体化学镀镍及其耐蚀性能

采用化学镀在钛基体上制备Ni-P合金镀层.研究了活化时间、镀液pH值、热处理温度及时间对镀层的影响.用动电位极化曲线法比较镀层的耐均匀腐蚀性能,并用X-射线衍射仪和扫描电子显微镜分别研究镀层结构和表面形貌.结果表明,以HF为主剂的活化液,时间60 s,pH值4.8～5.2的活化工艺以及250 ℃、保温2 h的热处理为最佳工艺.镀层具有较高的耐蚀性能,属于非晶和微晶组成的混晶结构.借助于正交试验,确定了最佳工艺.     

金属镍电沉积中枝晶分形生长的研究

将分形几何与电化学原理相结合,通过改进的有限扩散凝聚模型(diffusion-limited aggregation,DLA),采用基于Microsoft Visual C 6.0的Open GL编程,对点电极为阴极进行二维电沉积时沉积产物的形貌进行了模拟.以环形金属镍为阳极,石墨为阴极,用自行设计的试验设备制备了二维的金属镍枝晶以验证模拟结果.结果表明,在保持电压恒定的条件下,镍沉积层的形貌特征为具有分形结构的枝晶,这与采用DLA模型模拟所得的二维枝晶形貌具有相似性,表明该模型对枝晶电沉积的实验研究具有很好的指导意义.     

化学镀Ni-P-Cr2O3和Ni-P-SiO2复合镀层的研究

本文对化学镀镍及化学镀镍磷基质中SiO2与Cr2O3的共沉积进行了研究.微粒在不断生长的膜层中共沉积引起了新的化学复合镀层的出现,这些复合镀层许多都具有优异的耐磨及耐蚀性能.通过选取镀层合金/复合微粒/金属基体的组分可改进镀层,获得所需的性能,以满足特别的需求.在对这些复合镀层的应用需求正在迫近与增长的同时,其市场正在迅速扩张.本文开发出了一种合适的复合化学镀镍液,并通过维氏硬度法对化学复合镀镍层进行了表征.采用动电位极化及交流阻抗法测定了镀层的Taber耐磨性能及耐蚀性能.采用SEM及XRD对复合镀层的表面形貌进行了分析.     

无铅无镉光亮化学镀镍

分别研究了单组分无机金属盐、有机物以及组合光亮剂对化学镀镍层光亮性的影响。结果发现,单组分光亮剂的光亮效果不理想,而含硫有机物与其它组分配合形成的多组分光亮剂可使化学镀镍层获得光亮的效果,从而确定了无铅、无镉化学镀镍光亮剂。利用原子力显微镜观察了镀层的微观形貌。探讨了镀层的光亮机理。镀层的全谱直读电感耦合等离子发射光谱仪测试结果表明,只要控制主盐中的铅含量,镀层中的铅、镉含量均可达到欧盟的RoHS标准。     

电镀银镍合金工艺及其在电接触材料生产中的应用

介绍了用于生产电接触材料的银镍合金电镀工艺。镀液配方为:30~80g/LKAg(CN)2,10~30g/LKCN,10~20g/LK2CO3,0.2~0.3g/LCdSO4,0.1~0.2g/L糖精,100~150g/L络合剂Ⅱ,5~10g/L镍盐,1~2g/LK2SeO3。介绍了镀液中各组分的作用、镀液的维护及杂质影响与去除方法。讨论了镀液中各组分的含量及工艺条件(温度、电流密度、搅拌方式)对镀液和镀层性能的影响。该工艺操作简单,工艺范围宽,电流效率高,沉积速度快。     

温度对电沉积氢氧化镍电化学性能的影响

在0.1mol/L的Ni(NO3)2溶液中,采用电化学沉积法制备出适用于锌镍微电池的氢氧化镍电极,研究了电沉积温度对Ni(OH)2电极的电化学循环伏安性能以及充放电性能的影响。测试结果表明,电沉积方法制备的Ni(OH)2电极适合于微电池的制作。30°C下电沉积制备的Ni(OH)2电极具有优异的电化学性能,其质子扩散系数为7.71×10-12cm2/s,放电比容量为1285μAh/cm2,利用率达91.4%。     

新型纳滤膜分离电镀镍漂洗水的试验研究

本文介绍了TFC?-S型纳滤膜分离电镀镍漂洗水的试验研究,讨论了温度、操作压力、浓差极化、共存离子对膜分离性能的影响。结果表明,这种纳滤膜对电镀镍漂洗水中Ni2 的去除率高于99.5%,透过液中Ni2 质量浓度小于1mg/L;对CODCr的去除率大于96%,透过液中CODCr低于14mg/L,达到国家工业废水排放标准(GB8978-1996),可以直接排放或回用于镀件漂洗。