碳钢在N-甲基二乙醇胺介质中的电化学阻抗谱研究

应用电化学阻抗谱(EIS)研究碳钢在N-甲基二乙醇胺(MDEA)介质中的腐蚀行为.实验表明,未经预阴极活化处理的碳钢表面存在氧化膜,溶解氧促使它腐蚀速率增大,经活化处理去除氧化膜后则相反.在不含热稳定性盐(HSS)的MDEA溶液中,碳钢的腐蚀性随MDEA浓度的增加呈先上升后下降趋势;而在HSS高含量的溶液中,其腐蚀性则随MDEA浓度的增加而单调下降.在含有HSS模拟溶液中,碳钢的阳极极化EIS随极化电位由低到高分别出现感抗、负阻抗以及Warburg阻抗响应等特征,对应于孔蚀、活化状态向钝化状态过渡以及进入钝化的趋势,腐蚀反应的阴极过程表现为电化学反应和扩散传质混合控制,阳极过程为电化学反应控制.     

镁合金在含F－的NaOH溶液中钝化行为的电化学研究

采用极化曲线、电容-电位曲线、Mott-Schottky分析以及电化学阻抗(EIS)等电化学方法研究了镁合金在含F^－ NaOH溶液中的阳极钝化行为. 结果表明, 在－1.2～1.8 V的电位范围内, 镁合金在含F^－的NaOH溶液中发生阳极钝化. 所形成的钝化膜表现出n型半导体的导电特性. 在0.7～1.8 V的电位范围内, 随着F^－浓度增大, 镁合金的阳极极化电流密度呈现出随着电位升高而逐渐增大的趋势, 随着F^－浓度增大这一趋势逐渐减弱. 并且F^－浓度的增大使得镁合金表面空间电荷层电容和钝化膜的载流子密度都不断减小. 通过极化曲线和电化学阻抗共同说明, 在5%的Na₂SO₄溶液中, NaOH溶液中阳极钝化后的镁合金随着钝化体系中F^－浓度的增加其耐蚀性逐渐减弱.     

铁极化曲线的测定及应用实验研究

采用线性扫描伏安法 (LSV)和TAFEL方法测定铁的极化曲线 ,求得铁在不同介质中的自腐蚀电位、自腐蚀电流、钝化电位范围、钝化电流等电化学参数 ,并探讨 pH、Cl- 、缓蚀剂对铁的腐蚀和钝化成膜的影响。     

磁场作用下铁电极的不均匀阳极溶解

采用电化学方法以及扫描电镜形貌观察研究了磁场对铁在硫酸溶液中的阳极溶解的影响 .恒电位极化测试结果表明 ,随外加阳极电位的增加 ,磁场的存在将加速阳极溶解 ,使振荡态或钝态变为活性溶解态 ,维持钝态 .于特定电位下与重力方向平行的电极表面两侧将因局部溶解加速而出现凹陷 .由于电极周边浓度梯度场的特殊性以及磁场的作用方向导致了铁的不均匀阳极溶解     

B10合金的硫酸盐还原菌腐蚀研究

利用电化学方法研究了B1 0合金在含有硫酸盐还原菌的PostgateC培养基中的腐蚀电化学为 .结果表明 ,在有菌培养基中 ,B1 0合金的腐蚀电位剧烈负移 ,腐蚀速率显著增加 ,同时 ,由于硫化物覆盖层的形成 ,其阳极极化曲线出现“钝化”现象 .电子探针测量表明合金发生了镍和铁的选择性溶解 ,腐蚀形貌呈海绵状     

化学镀非晶态Ni-P和Ni-B合金在H_2SO_4溶液中的电化学行为

应用极化曲线,交流阻抗等电化学测量方法分别研究了化学镀Ni-P和Ni-B合金电极在0.5mol/L硫酸溶液中的电化学行为,分析探讨了Ni,Ni-P和Ni-B合金三者在上述H2SO4溶液中其开路电位和阳极溶解特性差异的可能原因.     

氯离子对模拟混凝土孔隙液中钢筋腐蚀行为的影响

应用动电位扫描法研究钢筋在模拟混凝土孔隙液中的腐蚀电化学行为以及氯离子的影响作用,并根据阳极极化曲线的变化揭示钢筋表面钝化膜的击穿电位及其变化规律,得出当溶液pH值分别为12.50和12.00时,由氯离子侵蚀引起的钢筋局部腐蚀,其钝化膜击穿电位突降的浓度临界值.     

扫描电化学显微镜原位表征pH值对核电蒸汽发生器合金腐蚀行为的影响(英文)

用扫描电化学显微镜(SECM)和电化学阻抗谱(EIS)原位表征了溶液pH值对核电蒸汽发生器800合金溶液中的腐蚀行为的影响.实验结果表明:在酸性氯化钠溶液中,SECM探针渐进曲线为正反馈,表明800合金为活化阳极溶解,腐蚀电位下的EIS图呈现完整的单容抗弧特征;而在中性或者碱性溶液中,SECM探针渐进曲线为负反馈,表明800合金为自钝化,不同阳极电位下的EIS图均呈现不完整的容抗弧特征,但随着阳极极化电位的增加,EIS谱容抗弧半径减小,表明钝化膜的耐蚀性下降;SECM二维扫描图像结果显示探针电流增加,表明电极表面活性增加,即钝化膜的溶解速度增加.而在中性或者碱性溶液中的SECM二维图像中均可观察到若干活性点,这可能与晶界或者金属夹杂物等有关.     

扫描电化学显微镜原位表征pH值对核电蒸汽发生器合金腐蚀行为的影响

用扫描电化学显微镜(SECM)和电化学阻抗谱(EIS)原位表征了溶液pH值对核电蒸汽发生器800 合金溶液中的腐蚀行为的影响. 实验结果表明：在酸性氯化钠溶液中,SECM探针渐进曲线为正反馈,表明800合金为活化阳极溶解,腐蚀电位下的EIS 图呈现完整的单容抗弧特征;而在中性或者碱性溶液中,SECM探针渐进曲线为负反馈,表明800 合金为自钝化,不同阳极电位下的EIS 图均呈现不完整的容抗弧特征,但随着阳极极化电位的增加,EIS 谱容抗弧半径减小,表明钝化膜的耐蚀性下降;SECM二维扫描图像结果显示探针电流增加,表明电极表面活性增加,即钝化膜的溶解速度增加. 而在中性或者碱性溶液中的SECM二维图像中均可观察到若干活性点,这可能与晶界或者金属夹杂物等有关.     

稀酸溶液中氯离子对工业纯铁的腐蚀机理研究

关于铁在酸性溶液中的腐蚀电化学行为，对不合特性吸附离子的体系而言，溶液PH值的改变对铁的阳极溶解起着重要作用，表明0＊一参与了钱的阳极溶解过程k’］．当向体系中引入具有特性吸附能力的执离子时，可以引起腐蚀中铁的腐蚀电位、Tdel斜率以及腐蚀电流密度和反应级教等诸多数的变化问，表明CI一也参与了铁腐蚀的电化学过程问．由于介质体系、电板材料及实验条件的差异，不同的研究者所获得的实验结果也不同卜和．然而，这些机理所讨论的均为把高于对阳极过程的影响，对氛离子存在时是否影响阴极析氢过程较少有实验证明．并且，对阳极…     

稀土铈对铝合金LY12CZ微生物腐蚀行为的影响

采用紫外分光光度法（UVS）、最大可能数法（MPN）、循环阳极极化法、电化学阻抗谱（EIS）和表面荧光显微法（EFM）研究了不同含量稀土Ce³⁺离子对硫酸盐还原菌（SRB）生长及LY12CZ铝合金微生物腐蚀行为的影响.结果表明:低浓度的Ce³⁺离子能够促进SRB生长,而高浓度时则抑制其生长;循环阳极极化曲线表明,稀土Ce³⁺离子的加入使铝合金LY12CZ的点蚀敏感性降低;电化学阻抗谱表明,在纯培养基中,随稀土Ce³⁺离子浓度的增大,铝合金耐蚀性增大.而在接种1%SRB的培养基中,当Ce³⁺浓度为0.376 mg·L^-1时,生长旺盛的生物膜与Ce³⁺间产生协同作用,增加了基体铝合金耐腐蚀性能.随着Ce³⁺浓度的增加,SRB生长受到抑制,不能形成致密的生物膜.此时SRB的存在促进铝合金腐蚀,显著减弱Ce³⁺对基体铝合金的保护作用.     

Corrosion inhibition of iron in hydrochloric acid using pyrazole

The corrosion and corrosion inhibition of iron in HCl solutions in the absence and presence of pyrazole (PA) were investigated by potentiodynamic polarization and electrochemical impedance spectroscopy (EIS). Changes in impedance parameters (R_ct and C_dl) were indicative of the adsorption of PA on the iron surface. The adsorption of PA is found to obey Langmuir adsorption isotherm. The study suggests that this compound is an anodic inhibitor.     

An EQCM study on the influence of saccharin on the corrosion properties of nanostructured cobalt and cobalt-iron alloy coatings

Nanostructured cobalt (Co) and cobalt-iron (CoFe) alloy coatings were electrodeposited from sulfate solutions in the presence and absence of saccharin. The effects of saccharin on the corrosion behavior of Co and CoFe alloy coatings were investigated using the electrochemical quartz crystal microbalance (EQCM) technique coupled with cyclic voltammetry (CV) measurements. Saccharin was added to the electrolyte as a grain refiner and brightener. Interestingly, opposite corrosion behaviors were found for all nanostructured coatings in 0.1 M H₂SO₄ and 0.1 M NaOH. The use of saccharin as an additive in the plating solution accelerated the anodic reaction for all deposits in acidic medium. The mass decreases while dissolution rate increased with higher saccharin concentration. Meanwhile, formation of a thick passive film on the Co electrode surface were enhanced while a hindering effect was observed for CoFe alloy coatings deposited in the presence of saccharin in alkaline solution. The anodic and cathodic curves obtained from potentiodynamic polarization experiments were also in agreement with the EQCM results.     

On the corrosion inhibition of iron in hydrochloric acid solutions,Part I: Electrochemical DC and AC studies

The inhibitive action of 4-methyl pyrazole (4MP) against the corrosion of iron (99.9999%) in solutions of hydrochloric acid has been studied using potentiodynamic polarization and electrochemical impedance spectroscopy (EIS). At inhibitor concentration range (10^?3–10^?2 M) in 1.0 M acid, the results showed that 4MP suppressed mainly the anodic processes of iron corrosion in 1.0 M HCl by adsorption on the iron surface according to Temkin adsorption isotherm. Both potentiodynamic and EIS measurements reveal that 4MP inhibits the iron corrosion in 1.0 M HCl and that the efficiency increases with increasing inhibitor concentration. Data obtained from EIS were analyzed to model the corrosion inhibition process through an equivalent circuit.     

Magnesium alloys spontaneous dissolution features under external anodic polarization in presence of inhibitors

The effect of benzotriazole (BTA) and sodium ethylenediamine tetraacetate (EDTA) to the magnesium dissolution intensity under external anodic polarization was studied. The inhibiting properties of BTA and EDTA in electrochemical corrosion of magnesium were found in the concentration range from 0.005 to 0.0125 M in sodium sulfate solution and from 0.0025 to 0.03 M in sodium chloride solution. In the presence of inhibitors, magnesium dissolution becomes uniform with decreasing surface hydrogenation and crumbling intensity of small particles into solution.     

Effects of 3-amino-1,2,4-triazole on the inhibition of copper corrosion in acidic chloride solutions

Effects of 3-amino-1,2,4-triazole (ATA) on the inhibition of copper corrosion in 0.5 M HCl solutions have been studied using gravimetric, electrochemical, and Raman spectroscopy investigations. Weight-loss measurements after varied immersion periods revealed that the dissolution rate of copper decreased to a minimum, while the inhibition efficiency (zeta%) and consequently the degree of surface coverage (theta) increased with the presence of ATA and the increase of its concentration. Potentiodynamic polarization, chronoamperometric, and electrochemical impedance spectroscopy (EIS) measurements after 0, 24, and 48 h immersion of the copper electrode in the test solutions showed that the presence of ATA molecules significantly decreased cathodic, anodic, and corrosion (jcorr) currents and corrosion rates (Rcorr) and greatly increased polarization resistance (Rp), zeta%, and theta; this effect was increased on increasing the ATA content in the solution. Raman spectroscopy confirmed that ATA molecules strongly adsorbed onto the copper surface, blocking its active sites and preventing it from being corroded easily.     

Corrosion and corrosion inhibition characteristics of bulk nanocrystalline ingot iron in sulphuric acid

The corrosion and corrosion inhibition of bulk nanocrystalline ingot iron (BNII) fabricated from conventional polycrystalline ingot iron (CPII) by severe rolling was studied in 0.5 M H₂SO₄ solution using electrochemical impedance spectroscopy and potentiodynamic polarization techniques. The results indicate that BNII was more susceptible to corrosion in the acidic environment essentially because of an increase in the kinetics of the anodic reaction. An amino acid cysteine (cys) was employed as a corrosion inhibitor at concentrations of 0.001 and 0.005 M. Tests in inhibited solutions revealed that cys reduced the corrosion rates of both metal specimens by different mechanisms. For CPII cys inhibited the cathodic reaction but had a stimulating effect on the anodic process at low concentration and a trivial effect at higher concentration. For BNII, cys inhibited both the cathodic and the anodic reactions, although the former effect was more pronounced. Iodide ions improved the inhibitive effect of cys without altering the inhibition mechanism.     

Preparation and electrochemical corrosion behavior of bulk nanocrystalline ingot iron in HCl acid solution

Bulk nanocrystalline ingot iron (BNII) was produced by the severe rolling technique. The corrosion behaviors of BNII and as-received conventional polycrystalline ingot iron (CPII) in 1 M HCl solution were investigated by potentiodynamic polarization tests, electrochemical impedance spectroscopy measurement, and immersion tests at room temperature. For BNII, the anodic dissolution process is inhibited, but the cathodic process is enhanced. The corrosion current and average corrosion rate of BNII are 0.479 and 0.391 those of CPII, respectively. The resistance of the charge transfer of BNII is about 1.59 times higher than that of CPII. These results indicate that the corrosion resistance of BNII is improved in comparison with CPII.     

Corrosion mechanism of pure aluminium in aqueous alkaline solution

The corrosion of pure aluminium in alkaline solution has been explored using an open circuit potential transient, potentiodynamic polarization experiment and a.c. impedance spectroscopy. The steady-state value of the open circuit potential (E _ocp ^ss ) of pure aluminium in alkaline solution was observed to decrease with increasing rotation rate of the specimen, which is ascribed to the enhanced anodic reaction. The extent of anodic polarization for the aluminium dissolution reaction on pure aluminium at E _ocp ^ss was found to be greater than that of cathodic polarization for the water reduction reaction. This indicates that the rate of corrosion of pure aluminium is mainly determined by the anodic reaction in alkaline solution. Based upon the experimental results, a corrosion mechanism for pure aluminium has been proposed in the presence of the native surface oxide film in alkaline solution, involving consecutive oxide film formation and dissolution, and simultaneous water reduction.