N80油套管钢应力状态下的CO2腐蚀行为研究

利用交流阻抗技术研究了拉伸、压缩和弯曲三种应力状态下N80油套管钢在饱和CO₂地层水中的腐蚀过程. 结果表明, 三种状态下的阳极电化学阻抗谱均出现了高频容抗弧、中低频感抗弧和低频容抗弧三个时间常数, 其中高频容抗弧与双电层电容和传递电阻有关, 感抗弧对应膜的活性溶解, 低频容抗弧与试样表面膜的生成有关. 随着三种状态下应变的增加, 感抗弧逐渐扩大, 而低频容抗弧则逐渐缩小, 表明应力状态下N80钢的CO₂腐蚀会加剧. 三种状态下的阴极阻抗谱高频均由容抗弧组成, 中低频由Warburg阻抗和容抗弧共同组成, 三种状态下随着应变程度的增加, Warburg阻抗增加, 反应电阻减小, 双电层电容减小, 说明应力会加速阴极反应过程的进行, 从而增加N80钢的CO₂腐蚀速率.     

不同阳极电位下铝青铜的电化学阻抗谱研究

应用电化学阻抗谱(EIS)方法研究了铝青铜的腐蚀溶解机制.结果表明,在活性溶解区,铝青铜以氯化络合物的形式溶解,并且CuCl2的扩散是该溶解过程的控制步骤;而在过渡区,铝青铜的EIS谱出现第2个容抗弧,这是由于CuCl络合物和氧化腐蚀产物在电极表面沉积成膜所致;在极限电流区,腐蚀产物膜产生破损点,导致电极表面快速溶解,产生严重的点蚀,这就是在该区域极化电位下EIS出现感抗弧的原因.     

纯铝在强碱溶液中阳极溶解的电化学阻抗谱解析

依据曹楚南提出的法拉第导纳表达式，拟合了纯铝在强碱溶液中的阳极溶解过程的电化学阻抗谱，并据此提出了这一反应进行的机理.结果表明,阻抗谱中的低频容抗弧是由表面裸露的Al转变为中间产物Al(OH)ads的反应引起的，而中频感抗弧则由Al(OH)ads转变为Al(OH)3,ads的反应引起.法拉第导纳的时间常数τ1和τ2的物理意义是物种Al(ss)和Al(OH)ads在单位表面活性位上的转化时间. τ1 >0和τ2 >0是符合稳定性条件的，也能够满足Kramers-Kronig转化的必要条件. g1和g2是与物种Al(ss)和Al(OH)ads在电极表面的覆盖密度随电位E变化有关的参数，由g1< 0可知随电位升高，纯铝表面的活性位面积减小.     

滑竹叶提取物在HCl介质中对铝的缓蚀性能

采用失重法、动电位极化曲线、电化学阻抗谱、红外光谱、紫外光谱和扫描电子显微镜研究了滑竹叶提取物(YPLE)在1.0 mol/L HCl介质中对铝的缓蚀作用。结果表明,YPLE对铝具有良好的缓蚀作用,缓蚀率随其浓度的增加而增大,且在铝表面的吸附符合Langmuir吸附等温式。YPLE为阴极抑制型缓蚀剂;电化学阻抗谱在高频区呈容抗弧,在低频区呈感抗弧,添加YPLE后,阻抗值显著增大。SEM表明,添加YPLE对铝的腐蚀产生了明显的抑制作用。     

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.     

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.     

环氧树脂涂覆LY12铝合金在NaCl溶液中的阻抗模型

分别研究了裸LY12铝合金及涂覆环氧树脂涂层后合金在3.5％NaCl溶液中的电化学阻抗谱（EIS）.结果表明,LY12铝合金在点蚀电位以下阻抗谱上出现两个容抗弧,高频段对应Cl－参与的成膜阻抗,低频段对应铝阳极溶解的电化学反应阻抗.合金发生点蚀后出现低频感抗弧.合金/电极在NaCl溶液中先发生涂层吸水,当水及O2抵达基体后建立起电化学反应界面,合金遭受腐蚀；受涂层阻挡的影响,腐蚀产物的扩散逐渐成为控制步骤；当扩散速度较慢的Cl－抵达涂层/金属界面后,与界面处聚集的腐蚀产物间发生化学反应,完成成膜过程,阻抗谱上出现盐膜的阻抗,而扩散阻抗消失.提出了不同浸泡失效阶段涂层电极体系的阻抗模型.     

覆铜板在NaCl溶液中的腐蚀电化学行为

应用线性极化、循环伏安(CV)及电化学阻抗谱(EIS)等电化学方法对覆铜板(CCL)和纯铜的腐蚀电化学行为进行了研究和比较. 结果表明, 覆铜板的耐蚀性弱于纯铜, 其阳极溶解过程与纯铜有所不同; 在较低电位下, CCL 以铜的氯化络合物的形式溶解, CuCl-2的扩散为该过程的控制步骤; 随着电位的升高, 腐蚀产物CuCl在电极表面形成疏松多孔的膜, Cl-在膜中的传输成为溶解过程的控制步骤. 电极表面CuCl 膜的消长过程是产生感抗弧的主要原因.     

电吸附除氯过程的电化学阻抗谱及动力学研究

借助三电极体系, 基于电化学交流阻抗谱图, 提出了一种对已吸附Cl^-的活性炭再次吸附一个Cl^-弛豫时间的测定方法, 根据弛豫时间确定速率控制步骤 . 研究了阳极电势、 预处理时间和预处理浓度对电化学过程的影响, 基于得到的电化学交流阻抗谱图上的参数, 求出不同条件下电吸附Cl^-的弛豫时间及覆盖度. 结果表明, 不同条件下得到的复数平面图均由一个容抗弧和一个感抗弧构成, 分别代表Cl^-在阳极上发生电荷转移的过程和 Cl^-在活性炭电极上的吸附过程 . 增加阳极极化可有效缩短弛豫时间, 阳极极化时, 弛豫时间为2.0×10^-5 s; 增加预处理时间, 弛豫时间逐渐增加, 预处理时间为180 min时, 弛豫时间增加到4.9×10^-5 s; 预处理浓度对弛豫时间的影响可忽略. 弛豫时间分析结果表明, Cl^-吸附速率比扩散速率小, 吸附是电吸附过程的速率控制步骤. 电极表面的覆盖度较低, 仅有10^-4...     

碳钢在碳酸铵溶液中的腐蚀研究实验改进

采用线性扫描伏安法和交流阻抗法研究了碳钢在不同实验条件下的腐蚀规律,碳钢在碳酸铵溶液中的阳极过程为溶解、钝化、过钝化溶解,溶解初期在电极界面的传质为线性扩散控制;随着溶液温度的升高,阻抗谱表示为单一时间常数的容抗弧,容抗弧直径逐渐减小,电阻变小,碳钢的腐蚀速度增大;Cl~-浓度越大,钝化区域变小,碳钢更容易腐蚀;加入硫脲缓蚀剂,碳钢容抗弧直径增大,电阻变大,有利于保护碳钢。     

La0.8Sr0.2MnO3／YSZ高温电极交流阻抗研究

用交流阻抗方法研究了Ｌａ０．８Ｓｒ０．２ＭｎＯ３电极上进行的氧化电化学还原反应。实验表明反应速度控制步骤随反应温度，氧分压及过电位发生显著变化，近平衡下反应的ｒｄｓ为氧的解离吸附过程。强阳极极化下，电解质表面产生大量电子空穴；强阴极极化下，ＬＳＭ电极表面形成大量氧空位，二者的结果均使界面电导增加，电化学反应区扩展。     

Deviations of capacitive and inductive loops in the electrochemical impedance of a dissolving iron electrode.

The electrochemical impedance of an iron electrode often shows the capacitive and inductive loops on the complex plane. The capacitive loop originates from the time constant of the charge transfer resistance and the electric double layer capacitance. The inductive loop is explained by Faradaic processes involving the reaction intermediate. In some cases, these loops deviate from a true semicircle. In this paper, the origins and curve-fitting methods for the deviated loops of electrochemical impedance are discussed. The constant phase element (CPE) was used to present the deviation of the capacitive loop instead of electric double layer capacitance. The reaction rate constants, which are a function of the frequency, are proposed for the Faradaic impedance to present the deviated inductive loop.     

Electrocatalytic reduction of CO2 in neat and water-containing imidazolium-based ionic liquids

Energetically efficient electrochemical reduction of CO₂ would offer the possibility of storing electricity from renewables in the form of fuels and other valuable chemicals. It may also help mitigate the increase of atmospheric CO₂ associated with global warming. However, the process suffers from a low energy efficiency because of the large overpotentials required. In aqueous electrolytes, the competing hydrogen evolution reaction also decreases the faradaic efficiency (which contributes to the low energy efficiency of the process). Recent claims of high faradaic efficiency and low overpotentials for the reduction of CO₂ in room-temperature ionic liquids (RTILs) and RTIL–water mixtures have spurred considerable research. Here, we offer a critical review of those claims and of recent work aimed at understanding the details of this important reaction in these nonconventional electrolytes.     

The anodic dissolution of silver into silver rubidium iodide — Impedance measurements

A.c. impedance measurements have been made on the Ag/Ag₄RbI₅ interphase at anodic potentials less than 50 mV vs. Ag/Ag⁺, using an automatic frequency response analyser.At overpotentials between 10 and 35 mV a high frequency semicircle and a low frequency inductive shape were seen. Spectra at these low overpotentials can be interpreted in terms of rate determining two-dimensional nucleation and growth of holes in the metal surface. The number of atoms in the critical nucleus at various overpotentials have been calculated from both steady state and impedance measurements.     

导电聚苯胺／MnO2空气阴极氧还原动力学

采用动电位扫描、交流阻抗技术研究了导电聚苯胺/MnO2复合阴极上氧还原反应动力学.动电位扫描表明氧在该复合阴极上还原的极化曲线服从Butler-Volmer公式,表观标准活化能为184.9 kJ/mol,反应为电化学步骤控制;交流阻抗谱观察到氧阴极还原由3个明显的线圈组成,表明氧阴极还原分3步进行,第1个圆弧随过电位的增大而显著减小,表明第1步电荷转移过程的确为氧还原反应的速率控制步骤;导电聚苯胺的高比表面积与MnO2的多微毛细管结构使氧在该复合电极上还原变得容易.     

An immitance study of the mechanism of hydrogen reactions on a tungsten carbide electrode: Part I. Experiment and analysis in terms of a linear model

The ac admittance spectra of a smooth tungsten carbide (WC) electrode in a stirred H₂-saturated 0.5 M H₂SO₄ solution were measured at hydrogen overpotentials from −0.15 to +0.25 V in the frequency range from 0.1 to 900 Hz, at a temperature of 80°C.An extended analysis of immitance spectra in diagrams of various coordinates led to an interpretation of the system under study at any potential in terms of a linear model which took into account the constant phase element behaviour of the electrode double layer and the presence of two parallel, activation-controlled faradaic processes: the hydrogen ionization/evolution process and an additional electrochemical adsorption reaction passivating the electrode surface for the hydrogen process.Computerized fitting of a rational equivalent circuit to the immitance spectra for all the potentials gave the dependences of the equivalent circuit elements on the potential. The fits proved that the mechanism of the faradaic processes taking place on the electrode is probably the same in the entire range of potentials.     

提高电容性电化学储能装置能量容量的一些尝试

本文从作者所在的课题组在超级电容器和超级电容电池方向的研究内容为基础,在电极材料和装置层面综述了电容性电化学储能装置的发展. 导电聚合物和过渡金属氧化物分别与碳纳米管复合后的复合物能显著提高前两者作为电容性法拉第储能电极的电容性能. 活性炭和碳黑等一类碳材料则可作为非法拉第储能的电极材料. 通过对超级电容器正负极电容做相应的匹配调整可以提高超级电容器的最大充电电压,从而提高超级电容器的能量容量. 此外,为了与实际设备相匹配,超级电容可以以双极板的方式串联堆积,满足高电压的需求. 超级电容电池作为新一代的电容性电化学储能装置,分别由具有电容性和法拉第电荷储存原理的电极组成,具有高比功率和高比能量的特点,也是近年来的研究热点.     

Noble metal-free hydrazine fuel cell catalysts: EPOC effect in competing chemical and electrochemical reaction pathways

We report the discovery of a highly active Ni-Co alloy electrocatalyst for the oxidation of hydrazine (N(2)H(4)) and provide evidence for competing electrochemical (faradaic) and chemical (nonfaradaic) reaction pathways. The electrochemical conversion of hydrazine on catalytic surfaces in fuel cells is of great scientific and technological interest, because it offers multiple redox states, complex reaction pathways, and significantly more favorable energy and power densities compared to hydrogen fuel. Structure-reactivity relations of a Ni(60)Co(40) alloy electrocatalyst are presented with a 6-fold increase in catalytic N(2)H(4) oxidation activity over today's benchmark catalysts. We further study the mechanistic pathways of the catalytic N(2)H(4) conversion as function of the applied electrode potential using differentially pumped electrochemical mass spectrometry (DEMS). At positive overpotentials, N(2)H(4) is electrooxidized into nitrogen consuming hydroxide ions, which is the fuel cell-relevant faradaic reaction pathway. In parallel, N(2)H(4) decomposes chemically into molecular nitrogen and hydrogen over a broad range of electrode potentials. The electroless chemical decomposition rate was controlled by the electrode potential, suggesting a rare example of a liquid-phase electrochemical promotion effect of a chemical catalytic reaction ("EPOC"). The coexisting electrocatalytic (faradaic) and heterogeneous catalytic (electroless, nonfaradaic) reaction pathways have important implications for the efficiency of hydrazine fuel cells.     

Selective solar-driven reduction of CO2 to methanol using a catalyzed p-GaP based photoelectrochemical cell

With rising atmospheric CO2 levels, there has been increasing interest in artificial photosynthetic schemes for converting this greenhouse gas into valuable fuels and small organics. Photoelectrochemical schemes for activating the inert CO2 molecule, however, operate at excessive overpotentials and thus do not convert actual light energy to chemical energy. Here we describe the selective conversion of CO2 to methanol at a p-GaP semiconductor electrode with a homogeneous pyridinium ion catalyst, driving the reaction with light energy to yield faradaic efficiencies near 100% at potentials well below the standard potential.