共查询到18条相似文献,搜索用时 121 毫秒
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低温化学镀镍中络合剂作用研究 总被引:2,自引:0,他引:2
研究了络合剂在低温化学镀镍槽液中的作用.试验表明,络合剂的正确选择是低温镇工艺实现的关键,络合剂的稳定性不但影响槽液的稳定,而且对镀速和镀层质量都有重要影响.络合剂的稳定性与其结构及配位原子性质、位阻效应等关系密切.选用复合络合剂,有利于调整镀速与镀层质量.络合剂的缓冲作用对提高镀速有利. 相似文献
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目的提高LED支架的性价比,减少SPCC钢表面镀银预镀铜工艺的镀液污染,简化现有的预镀镍-镀铜施镀工艺,提高预镀层质量。方法采用HEDP碱性无氰直接预镀铜方法来简化工艺,用单因素实验法,系统研究了电流密度、镀液pH、电镀温度、HEDP/Cu~(2+)摩尔比、电镀时间等参数,对镀层镀速、孔隙率及镀层表面质量的影响,并表征镀层的微观组织及镀层结合力。结果在阴极电流密度为1.41 A/dm~2,pH值为9.5,温度为50℃,HEDP/Cu~(2+)摩尔比为3.75:1(Cu~(2+)为10 g/L),时间为11 min的条件下,可获得镀速约为1.7 mg/(cm~2·min)的预镀铜层,且镀层与基体的结合力良好,无孔隙,呈良好的光亮/半光亮状的细晶镀层。结论与钢铁表面氰化镀铜及镀银前预镀铜工艺相比,推荐的HEDP直接预镀铜工艺的镀层质量好,可满足直接镀铜和镀银前预镀铜工艺要求,可有效减少镀液污染和简化施镀工艺,对SPCC钢的镀铜工艺改善具有较好的推广价值。 相似文献
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研究了络合剂在低温化学镀镍槽液中的作用。试验表明,络合剂的正确选择是低温镀工艺实现的关键络合剂的稳定性不但影响槽液的稳定,而且对镀速和镀层质量都有重要影响。络合剂的稳定性与其结构及配位原子性质,位阻效应等关系密切。 相似文献
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《热加工工艺》2018,(22)
在镀液基本组成为焦磷酸钾(260 g/L)、焦磷酸铜(18 g/L)、焦磷酸亚锡(2.0 g/L),电镀工艺条件为电流0.15A,温度30℃,pH=9~10,电镀5 min,和空气搅拌的条件下,利用正交实验探究羟基乙叉二膦酸(HEDP)、酸铜走位剂(AESS)和K_2CO_3对无氰仿金电镀镀层颜色的影响。对正交结果进行分析,最终得出HEDP、AESS、K_2CO_3的最优组合为:HEDP:15 g/L,K_2CO_3:40 g/L,AESS:24×10~(-3)g/L。对以上组合所得到的镀层形貌、厚度、成分、相组成进行。该配方可获得Hull槽试片上全范围光亮的仿金镀层,且镀层表面平整,镀层厚度约为1.5μm。Sn在镀层中主要以Cu_(13.7)Sn的形式存在,且为立方结构。 相似文献
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采用电化学技术(动电位极化曲线、自腐蚀电位、EIS以及Mott-Schottky曲线)和表面分析方法(SEM、XPS)研究了羟基亚乙基二膦酸(HEDP)对空冷20SiMn低合金钢在含Cl-的高碱性混凝土模拟孔隙液中的缓蚀作用及机理。结果表明,HEDP对20SiMn钢在含1 mol/L NaCl饱和Ca(OH)2溶液中的缓蚀效果随HEDP浓度的升高存在极值,最佳浓度为1.441×10-4mol/L。在此浓度下HEDP将20SiMn钢的钝性保持时间从6 h延长至9 h,缓蚀效率达到46.45%~59.78%。在发生点蚀的情况下,HEDP对点蚀的发展亦有显著的抑制作用,缓蚀效率超过93%。电化学和表面分析结果表明,HEDP优先吸附在钝化膜表面,通过竞争吸附机制屏蔽了侵蚀性Cl-向钝化膜表面的附着,从而对其产生保护作用。 相似文献
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江冶 《腐蚀科学与防护技术》1991,3(2):33-41
<正> 前言自从六年代初日本浅田教授开发了铝及其合金电解着色技术以来,锡盐着色技术在国内应用较为普遍。然而,多年来锡盐着色液的稳定性及再生处理技术一直未得到彻底解决。主盐Sn~(2+)很容易氧化成Sn~(4+),这不仅消耗了槽液的有效成分,而且Sn~(4+)又易发生水解生成氢氧化锡沉淀,使槽液浑浊,加速了槽液的老化,而且,当槽液内Sn(OH)_4积累到一定量后,着色效率和着色质量下降,而且槽液药品消耗量迅速增加,只有除去槽 相似文献
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The study of adsorption/desorption processes of 1‐hydroxy‐ethanol‐1,1‐diphosphonic acid (HEDP) molecules, and the mixture of HEDP/zinc ion on gold surface has been investigated in neutral perchlorate solution using cyclic voltammetry and electrochemical scanning tunnelling microscopy (EC‐STM). Cyclic voltammetry measurements showed that HEDP molecule has an effect on the anodic oxidation of gold. The reversible adsorption/desorption peak in presence of zinc cations is attributed to the effect of zinc ions on the adsorption of HEDP. Results of in situ EC‐STM studies on the initial stages of HEDP adsorption on gold single crystal (111) are presented and compared with the adsorption of the mixture of HEDP/zinc ion. The morphology of the gold (111) surface changed during repeated cycles. Sub‐mono‐layer islands are formed in presence of HEDP molecules. The surface morphology changed significantly in presence of both HEDP and zinc in the solution. After repeated cycles the whole gold surface was covered with a network‐type layer. This adsorbed layer varied in function of the gold (111) potential. The results were analysed and discussed. 相似文献
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The effect of some phosphonic acids (HMEP, NTMP, HEDP) on the chemical passivation of iron by dissolved oxygen in neutral aqueous solutions has been investigated. It has been shown that in the presence of phosphonic acids chemical passivation cannot be attained. This effect is due to the formation of soluble complexes as could be shown by the stability constants determined. 相似文献
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过氧乙酸中硅酸钠对 Q235 钢的缓蚀影响 总被引:2,自引:2,他引:0
目的研究HEDP、十二烷基苯磺酸钠(SDBS)和硅酸钠的复配物在过氧乙酸溶液中对Q235钢缓蚀效率的影响。方法采用静态失重法和动电位极化曲线法,研究常温下在过氧乙酸质量浓度为2000 mg/L的体系中,硅酸钠与HEDP、SDBS复配时对碳钢的缓蚀协同效应,确定最佳配比,分析缓蚀机理。结果 HEDP、SDBS和硅酸钠的复配物,在过氧乙酸溶液中对Q235钢均有一定的缓蚀效果,缓蚀效率依次为:硅酸钠与HEDP硅酸钠与SDBS硅酸钠。当硅酸钠质量浓度为200 mg/L,HEDP质量浓度为100 mg/L复配时,缓蚀效率最高达到90.42%。当硅酸钠质量浓度为200 mg/L,SDBS质量浓度为200mg/L复配时,缓蚀效率最高达到57.76%。单一硅酸钠缓蚀剂的缓蚀效率最高达40.53%。结论硅酸钠能同时抑制阳极和阴极的反应,与HEDP有很好的缓蚀协同效应,硅酸钠与HEDP复配优于与SDBS复配的缓蚀效果。较优复配缓蚀剂为:硅酸钠200 mg/L,HEDP 100 mg/L。 相似文献
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《腐蚀工程科学与技术》2013,48(2):147-154
AbstractThe action of 1-hydrox yethylidene-1, 1-diphosphonic acid (HEDP) in combination with zinc ions as a corrosion inhibitor for mild steel in oxygen containing aqueous solutions has been investigated in relation to the presence of different zinc levels, the presence of aggressive anions, and different pH values. The highest inhibition effect was obtained at a 2·7:1 zinc/HEDP molar ratio, corresponding to 60 ppm zinc, and was associated with a significant anodic effect. In the absence of chloride and with no free forms of the inhibitor components, the zinc-HEDP mixture exhibited good protection over a wide range of pH (6·5-9·5). However, in a weakly acidic medium, protection could not be achieved. Calculations based on the dissociation constants of the HEDP and the stability constants of the possible zinc-HEDP complexes showed that this inhibition can be attributed to the presence of the 2:1 zinc-HEDP complex (Zn2H-1L-) at a sufficient level. It is found that this anionic complex can behave as an anodic, passivating, inhibitor at a concentration as low as 0·00015M (20 ppm zinc-32 ppm HEDP mix ture). This passivity is prevented by the presence of sufficient chloride. The critical chloride concentration in these studies is approximately ten times higher than the complex concentration, in molar terms. It is also found that free phosphonate is aggressive and can prevent passivity due to the preferential formation of soluble iron-HEDP complex. The tolerance of the 2:1 complex to free phosphonate is substantially less than to chloride, approx imately equimolar. 相似文献
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Laboratory studies on corrosion of unalloyed steel in cooling waters Corrosion tests were carried out in recycle apparatures to prepare cooling-water treatment. The corrosion behaviour of unalloyed steel St 38b-2 in dependence on m-value of water was tested. The corrosion-inhibiting effect of sodium polyphosphate, zinc sulfate, 1-hydroxy-1,1-diphosphonic acid (HEDP) and the trisodium salt of HEDP and polyacrylate and their combinations in water with m-value 1.0–1.5 mmole per litre was tested in comparison with unalloyed steel. The corrosion rate increases strongly below a m-value of 2.2 mmol per litre. Sodium polyphosphate, sodium polyphosphate/zinc sulfate and zinc sulfate-polyacrylate show good protection features in water with m-value 1.0–1.5 mmole per litre. The trisodium salt of HEDP has an insufficient effect. 相似文献
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This work aims to analyze, through weight loss and X‐ray photoelectron spectroscopy (XPS) methods, the inhibitive films of 1‐hydroxyethane‐1,1‐diphosphonic acid (1‐hydroxyethylidene‐1,1‐diphosphonic acid, HEDP) and zinc(II) ions formed on AISI 1020 carbon steel when immersed in solutions containing 30 ppm of chloride ions, 50 ppm of HEDP, and three different concentrations of zinc(II) ions (14, 20, and 30 ppm). Moreover, the results of the experimental surface analyses were compared to molecular modeling studies of the proposed HEDP–Fe(III)/Zn(OH)2/HEDP–Zn(II) protective film. The film presented dissimilar structures responsible for the different levels of metallic protection for each particular zinc(II) concentration. In general, the increase in Zn(II) concentration leads to more compact and adherent film formation, with decreased corrosion rates of carbon steel. 相似文献
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Electrochemical measurements (steady‐state current‐voltage curves and AC impedance) were coupled with mass‐loss measurements, SEM examinations, and EDSX analyses to investigate the inhibition of corrosion of a carbon steel by a mixture of phosphonic acid HEDP (acid 1, hydroxyethylene, 1‐1 diphosphonic) and sodium metasilicate pentahydrate Na2SiO3. 5H2O in an industrial hard water containing 3.10?3 M Ca2+ ions. At pH 7, HEDP and Ca2+ act in a synergistic manner, by formation of a HEDP and calcium containing layer. Addition of silicate at this pH value, allows to reach an efficiency of 94% due to an additive inhibition effect. At pH 11, metasilicate, HEDP, and Ca2+ ions reinforce the passive layer in a synergistic way. The mixture (1.7 · 10?5 M HEDP + 2.6 · 10‐3 M SiO2?3) in the Ca2+ containing electrolyte is shown to be able to inhibit efficaciously the corrosion of iron at room temperature, considering uniform corrosion at pH 7 or pitting corrosion at pH 11. 相似文献
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A comparison has been made of the long term stability and corrosion resistance of trivalent chromium deposited from a chloride based solution and hexavalent chromium deposited from a sulphate based solution. The work showed a difference in corrosion resistance between the two systems and has revealed the corrosion mechanism that caused the failure of the plated films. All the work was carried out on a brass substrate overplated with bright nickel to provide a substrate for the chromium deposit. 相似文献