电解制备二氧化锰强酸性电解液中气体扩散电极的稳定性与失效行为

采用气体扩散电极(GDE)代替传统析氢阴极电解制备二氧化锰(EMD),重点研究了气体扩散电极在强酸性MnSO4-H2SO4电解液中的稳定性、寿命及失效行为.结果表明:气体扩散电极在MnSO4-H2SO4电解液中重现性好、具有一定的稳定性,寿命可达400 h;平行实验表明,阳极沉积一定厚度的EMD是槽电压第一次升高的主要原因;电流密度为100 A m-2时,气体扩散电极失效前阴极过程的速度由氧的离子化反应和氧的扩散混合控制,失效后阴极过程由氧去极化和氢去极化共同组成,主要发生析氢反应;催化层聚四氟乙烯(PTFE)网络结构的破坏和镍网层的溶解是电极失效的原因之一;Pt的团聚降低了电极的电催化活性,是电极失效的主要原因;阴极失效是槽电压再次升高的主要原因.     

Charge transfer between two immiscible electrolyte solutions: Part VI. Polarographic and voltammetric study of picrate ion transfer across the water/nitrobenzene interface

The transfer of the picrate ion across the interface between two immiscible electrolyte solutions, 0.05 M LiCl in water and 0.05 M tetrabutylammonium tetraphenylborate in nitrobenzene was investigated by electrolysis with the electrolyte dropping electrode and by cyclic voltammetry. Under the conditions of the experiments the charge-transfer process is controlled solely by diffusion. The maximum which appears on the polarogram of the picrate ion close to the limiting current can be suppressed by the addition of a surface-active substance (gelatine). The diffusion coefficients of the picrate ion in the aqueous and nitrobenzene phase were determined from the limiting polarographic current and from the peak current on the cyclic voltammogram. The value of the formal potential of the charge-transfer reaction, which was calculated from the half-wave potential or from the peak potential, is in good agreement with that inferred from the extraction data.     

Equilibrium lithium-ion transport between nanocrystalline lithium-inserted anatase TiO2 and the electrolyte

The power density of lithium-ion batteries requires the fast transfer of ions between the electrode and electrolyte. The achievable power density is directly related to the spontaneous equilibrium exchange of charged lithium ions across the electrolyte/electrode interface. Direct and unique characterization of this charge-transfer process is very difficult if not impossible, and consequently little is known about the solid/liquid ion transfer in lithium-ion-battery materials. Herein we report the direct observation by solid-state NMR spectroscopy of continuous lithium-ion exchange between the promising nanosized anatase TiO(2) electrode material and the electrolyte. Our results reveal that the energy barrier to charge transfer across the electrode/electrolyte interface is equal to or greater than the barrier to lithium-ion diffusion through the solid anatase matrix. The composition of the electrolyte and in turn the solid/electrolyte interface (SEI) has a significant effect on the electrolyte/electrode lithium-ion exchange; this suggests potential improvements in the power of batteries by optimizing the electrolyte composition.     

A comparative study of the anion transfer kinetics across a water/nitrobenzene interface by means of electrochemical impedance spectroscopy and square-wave voltammetry at thin organic film-modified electrodes

The kinetics of the transfer of a series of hydrophilic monovalent anions across the water/nitrobenzene (W/NB) interface has been studied by means of thin organic film-modified electrodes in combination with electrochemical impedance spectroscopy and square-wave voltammetry. The studied ions are Cl-, Br-, I-, ClO4-, NO3-, SCN-, and CH3COO-. The electrode assembly comprises a graphite electrode (GE) covered with a thin NB film containing a neutral strongly hydrophobic redox probe (decamethylferrocene or lutetium bis(tetra-tert-butylphthalocyaninato)) and an organic supporting electrolyte. The modified electrode is immersed in an aqueous solution containing a supporting electrolyte and transferring ions, and used in a conventional three-electrode configuration. Upon oxidation of the redox probe, the overall electrochemical process proceeds as an electron-ion charge-transfer reaction coupling the electron transfer at the GE/NB interface and compensates ion transfer across the W/NB interface. The rate of the ion transfer across the W/NB interface is the limiting step in the kinetics of the overall coupled electron-ion transfer reaction. Moreover, the transferring ion that is initially present in the aqueous phase only at a concentration lower than the redox probe, controls the mass transfer regime in the overall reaction. A rate equation describing the kinetics of the ion transfer that is valid for the conditions at thin organic film-modified electrodes is derived. Kinetic data measured with two electrochemical techniques are in very good agreement.     

高选择性和稳定性SnO2纳米催化剂上 CO2电化学还原为甲酸

作为最重要的还原产品,甲酸是 CO2还原中非常有价值的液体燃料.已有研究报道, Sn类金属电极对甲酸生成有很好的催化活性,所用电解液均为 KHCO3溶液(0.5 mol/L),但多数研究没有对其电解液条件的影响给出清晰解释.一般而言,电解液 pH值会影响 H2O和 CO2还原的电极电势,酸性环境有利于氢析出,碱性环境则不利于甲酸形成.在中性偏碱性环境, CO2电解可以提供维持氧化物稳定性的可能性.同时,电解质浓度也极大地影响甲酸形成.研究表明,当在固定床反应器中使用 Sn颗粒电极,在 KHCO3溶液(0.5 mol/L)中甲酸的法拉第效率比 K2CO3溶液(0.1 mol/L)的法拉第效率更大.我们研究组通过简单的水热自组装法成功制备了一种纳米结构 SnO2催化剂.其中 SnO2-50纳米催化剂由三维多级结构组成,为纳米颗粒和微米球的聚集体,其中含有直径为500 nm?1μm的高度多孔结构.该催化剂负载气体扩散电极用于 CO2电化学还原,表现出优异的 CO2还原催化活性和甲酸选择性.与其他文献报道相比,该电极具有明显的低过电位(?0.56 V vs. SHE).经研究发现,这与甲酸形成由传质和电荷传递过程控制有关,同时 CO2还原强烈依赖于电解液条件.此外,催化剂的电化学性能和甲酸选择性强烈依赖于电解液浓度.在0.5 mol/L KHCO3电解液中,当电解液浓度为0.1?0.5 mol/L时,催化性能随电解液浓度增加而提高,同时在电解液浓度为0.5 mol/L时催化性能达到最佳,获得56%的甲酸法拉第效率,这主要是由于 HCO3?直接参与反应的结果.在电解液浓度较低时,甲酸的形成由传质控制,而在电解液浓度较高时,甲酸的形成则由电荷传递控制.
　　同时我们发现在形成甲酸过程中,电解液 pH值对 CO2电化学还原过程有很大影响.为了研究电解液pH值影响,重点考察了pH值分别为6,7,8.3和9时的电位值,其原因是酸性过高有利于氢气形成,碱度过高不利于甲酸形成.结果表明,pH =8.3的电解液为 CO2还原的最佳电解液条件.此外,在最负的电势下,电解液pH=8.3时,阴极电流密度比其他电解液都大,几乎是pH=6的电解液的2倍.此时在中性偏碱性环境下, CO2还原可以提供维持氧化物稳定性的可能性.当电解液 pH增加到9.0时,甲酸产量及法拉第效率略有下降,可能是碱性环境不利于甲酸形成.
　　同时,对 SnO2-50纳米催化剂经28 h电解后的甲酸法拉第效率的衰减机制进行了深入研究.结果表明,随着电解时间延长,甲酸法拉第效率衰减.电解时间为1?28 h时,法拉第效率和甲酸产量均保持平稳下降趋势,28 h后法拉第效率由初始的56%降至24%.有文献报道,甲酸法拉第效率随电解时间的改变主要是由于阳极上甲酸的氧化或阴极上杂质的污染.为了证明阴极电解后的状态,我们对 SnO2-50/GDL阴极电解前后的 XPS谱进行了分析.结果发现,法拉第效率的下降是由于痕量氟离子沉积到 SnO2-50/GDL电极表面,这些痕量氟离子可能来自反应槽,阻碍电极表面 CO2电化学还原为甲酸.     

Enhancement of mass transfer efficiency and photoelectrochemical activity for TiO_2 nanorod arrays by decorating Ni~(3+)-states functional NiO water oxidation cocatalyst

Photoelectrochemical(PEC) water splitting is a promising technology to use solar energy.However,current metal oxides photoanode face the problem of sluggish water oxidation kinetic.In this study,we propose that the sluggish water oxidation process will cause slow mass transfer efficiency,which are rarely considered previously,especially at large bias and strong illumination.Mass transfer refers to the migration of reactants(like H_2 O and OH~-) to the photoanode surface,reaction with holes and diffusion of products(like radical and O_2) to the bulk of the electrode.If the migration and diffusion are not fast enough,the mass transfer will inhibit the increase of PEC activity.This problem will be more apparent for nanorod arrays(NRAs),where the space among the NRAs is related narrow.Herein,we solve this problem by decorating the surface of the photoanode by NiO clusters with Ni~(3+) state as water oxidation cocatalysts.This work studies the PEC process from the viewpoint of mass transfer and firstly demonstrates that mass transfer in NRAs structure can be promoted by using Ni-based water oxidation cocatalyst.     

Fractal Characterization of Silica Sol Prepared by the Sol-Gel Method: From the Sol Formation to the Flocculation Process

The fractal characterization of silica particles prepared by the sol-gel method was obtained; from the beginning of the sol-gel synthesis to the aggregation process of these particles by adding metal ions in solution, the fractal dimension was determined. At the beginning of the sol-gel process, unstable structures were formed due, essentially, to the auto-catalytic nature of the sol-gel condensation reactions; these particles are fractal structures with a fractal exponent corresponding to a reaction limited aggregation regime. As the time proceeds, the reactants are consumed approaching the system to equilibrium, stabilizing the size of the silica particles. The silica sol can be flocculated by adding metal ions in solution. The fractal exponent for the aggregation process was determined, obtaining a value corresponding to a diffusion limited aggregation regime.     

Anomalous temperature-isotope dependence in proton-coupled electron transfer

Motivated by the experiments of Hodgkiss et al. [J. Phys. Chem. (submitted)] on electron transfer (ET) through a H-bonding interface, we present a new theoretical model for proton-coupled electron transfer (PCET) in the condensed phase, that does not involve real proton transfer. These experiments, which directly probe the joint T-isotope effects in coupled charge transfer reactions, show anomalous T dependence in k(H)k(D), where k(H) and k(D) are the ET rates through the H-bonding interface with H-bonded protons and deuterons, respectively. We address the anomalous T dependence of the k(H)k(D) in our model by attributing the modulation of the electron tunneling dynamics to bath-induced fluctuations in the proton coordinate, so that the mechanism for coupled charge transfer might be better termed vibrationally assisted ET rather than PCET. We argue that such a mechanism may be relevant to understanding traditional PCET processes, i.e., those in which protons undergo a transfer from donor to acceptor during the course of ET, provided there is an appropriate time scale separating both coupled charge transfers. Likewise, it may also be useful in understanding long-range ET in proteins, where tunneling pathways between redox cofactors often pass through H-bonded amino acid residues, or other systems with sufficiently decoupled proton and electron donating functionalities.     

渗透物在致密聚合物膜中扩散的分形介质模型

利用自由体积理论讨论了渗透物分子在致密聚合物膜内的扩散机理, 提出了“扩散通道”的概念, 建立了渗透物在致密聚合物膜中扩散的分形介质模型, 考虑了自由体积分布对扩散过程的影响. 根据建立的模型, 渗透物在膜内的扩散是由在“扩散通道”上的一系列跳跃构成的. 根据致密膜内扩散通道的关联长度ξ(p)与膜厚L的关系, 可以把扩散分为正常扩散、 过渡扩散和分形扩散三部分, 给出了扩散相图, 提出并解释了分形渡越现象.     

An analysis of the reaction–diffusion mechanism governing the chlorination process of poly(vinyl chloride)

Chlorinated poly(vinyl chloride) (CPVC) obtained through a dry chlorination of PVC films or grains can show a heterogeneous repartition of its chlorine atoms because the reaction process is limited by the mass transfer of the chlorine gas in the material. In order to describe the evolution of such a system, a set of coupled equations is derived where only two dimensionless constants have to be determined: K_S, which depends on the solubility of the chlorine gas in the PVC, and K_T, the ratio between the diffusion and the reaction characteristic times. The kinetics of chlorination obtained for the different regimes matches the available experimental data, and the corresponding concentration profiles for the chlorinated PVC chains are displayed to demonstrate how a heterogeneous chlorination can arise from this dual process. In particular, a sharp interface appears in the diffusion‐limited regime that separates the chlorinated region from an unchlorinated core and is shown to progress deeper into the film with the square root of time. To a larger extent, this analysis shows how heterogeneity of reaction and nonlinear effects can arise from a coupling between a diffusive phenomenon and a reactive phenomenon. © 2000 John Wiley & Sons, Inc. J Polym Sci B: Polym Phys 38: 3201–3209, 2000     

Simultaneous ion transfer across the microhole ITIES: an example of ternary electrodiffusion

Ternary electrodiffusion at the immiscible liquid liquid interface (ITIES) is considered in the case where a univalent cation is transferring from the water to the organic phase through a microhole, and simultaneously a univalent anion is transferring in the opposite direction. The process is assumed to take place at steady-state. If the separation between the formal transfer potentials of these ions is large enough, a limiting current corresponding to the electrodiffusion of the ion with the lower formal transfer potential is observed. Thereafter, the current begins to rise again as a linear function of the cell potential because the Galvani potential across the interface has reached its limiting value and the potential is expended in the form of ohmic loss in the diffusion boundary layers. The Galvani potential across the interface cannot overcome the average value of the formal transfer potentials due to the electroneutrality condition. The present case is analogous to a redox reaction at the ultramicroelectrode with sign reversal (K.B. Oldham, J. Electroanal. Chem. 337 (1992) 91) but no suitable experimental system has yet been found with which to test this prediction. Experiments without supporting electrolytes seem to have only little value in quantitative analysis of ion transfer.     

Monitoring Diffusion of Reptating Polymer Chains by a Direct Energy Transfer Method: A Monte Carlo Simulation

A kinetic Monte Carlo method was used to simulate the diffusion of reptating polymer chains across an interface. A time‐resolved fluorescence technique in conjunction with a direct energy transfer method was used to measure the extent of diffusion of dye‐labeled reptating polymer chains. The diffusion of donor‐ and acceptor‐labeled polymer chains between adjacent compartments was randomly generated. The fluorescence decay profiles of donor molecules were simulated at several diffusion steps to produce mixing of the polymer chains. Mixing ratios of donor‐ and acceptor‐labeled polymer chains in compartments were measured at various stages (snapshots) of diffusion. It was observed that for a given molecular weight, the average interpenetration contour length was found to be proportional to the mixing ratio. Monte Carlo analysis showed that the curvilinear diffusion coefficient is inversely proportional to the weight of polymer chains during diffusion.     

Lateral diffusion of molecules in two-component lipid bilayer: a Monte Carlo simulation study

Lateral diffusion of membrane components makes possible any in-plane membrane reaction and has a key role in signaling in cell membranes. In this report the equilibrium lateral diffusion of intrinsic molecules in an equimolar DMPC/DSPC mixture is simulated using a thoroughly tested two-state model of two-component phospholipid bilayers. The model has been successful in calculating the excess heat capacity function, the most frequent center-to-center distances between DSPC clusters, and the fractal dimensions of gel clusters (Sugar, I. P., Thompson, T. E., Biltonen, R. L. Biophys. J. 1999, 76, 2099-2110). In the gel/fluid mixed phase region, a diffusing intrinsic molecule may change its state from fluid to gel (or from gel to fluid) at any time. A common characterization of the diffusion of intrinsic molecules is given by the simulated average first-passage time curves. We find that these curves can be described as power functions containing two parameters, alpha and beta, except near the percolation threshold of gel/fluid or compositional clusters. We find also that the intrinsic molecules are involved in approximately normal diffusion, i.e., beta approximately 2 in the extreme gel and fluid phase regions, while in the gel/fluid and gel/gel mixed phase regions the diffusion is anomalous, i.e., beta not equal 2. In the mixed phase regions, when the initial local state of the diffusing molecule is not specified, each component is involved in sub-diffusion (beta > 2). In the gel/fluid mixed phase region molecules situated initially inside a fluid cluster are involved in sub-diffusion, but DMPC molecules situated initially inside a gel cluster are involved in super-diffusion (beta < 2). The possibility of anomalous diffusion in membranes apparently arises because the diffusing molecule visits a variety of different environments characterized by its relative proximity to various membrane components. The diffusion is actually anomalous when the components of the bilayer are nonrandomly distributed. The deviation from random distribution is strongly correlated with beta. Similar to the results of the NMR experiments, the calculated relative diffusion coefficient continuously decreases in the gel/fluid mixed phase region with decreasing temperature. In apparent contradiction, diffusion measured by fluorescence recovery after photobleaching (FRAP) demonstrates the existence of a threshold temperature, below which long-range diffusion of FRAP probe molecules is essentially blocked. This threshold temperature is highly correlated with the percolation temperature of gel clusters.     

Facilitated Ion Transfer Across the Micro-liquid/Liquid Interface Supported at the Tip of a Silanized Micropipette

IntroductionIon transfer across a liquid/liquid( L/L) inter-face or an interface between two immiscible elec-trolyte solutions( ITIES) plays a significant role inmany biochemical fields and technological systemsfrom biological membrane and drug delivery to ex-traction process and chemical sensors[1] . Theminiaturization of ITIESwas firstachieved by Tay-lor and Girault via supporting the interface at thetip of a micropipette in1 986[2 ] .Later on a nano-ITIES supported at a nanopipette …     

染料敏化太阳电池中多相接触界面电子转移机制和动力学过程

采用电化学阻抗谱(EIS)研究了染料敏化太阳电池(DSC)中由导电玻璃、 纳米多孔TiO₂薄膜和电解质构成的多相复杂接触界面的电子转移机制和动力学过程. 通过沉积聚合物薄膜简化多相接触界面结构, 根据接触界面结构和电子转移途径的变化, 分析了不同偏压下多相接触界面电子转移机制, 构建与之对应的等效电路, 获得了DSC内部各个主要接触界面的电子转移动力学常数. 结果表明, 通过外加偏压的控制和多相接触界面结构的简化, 可以区别分析多相复杂接触界面电子转移机制与动力学过程.     

高效的CdS/Ti-Fe2O3异质结光阳极:研究Z型电荷迁移机制增强光电化学水氧化活性

近年来以Z型机制为转移的光催化体系成微光电化学分解水领域的研究热点.相比较传统的异质结,Z型异质结能够保留具有高氧化能力与高还原能力的位点,从而提高光电化学效率.其中,证明电荷的Z型迁移机制成为研究人员努力的方向,比较有效的证明方法包括自由基捕获、XPS分析和检测还原位点等.对于Z型异质结,界面电场处电荷的迁移行为是至关重要的,但目前常用的证明手段对界面电场处电荷的迁移行为研究还比较少.因此,本文精心设计了CdS/Ti-Fe₂O₃异质结光阳极来探索光电化学分解水中的电荷转移行为.采用开尔文探针测试、表面光电压谱测试和瞬态光电压谱测试等光物理测试手段监测CdS/Ti-Fe₂O₃Z型异质结光阳极界面电场中光生电荷的迁移行为.其中,开尔文探针和表面光电压测量表明,CdS/Ti-Fe₂O₃界面驱动力有利于激发电子快速迁移至CdS;由于Z型异质结是一个双光子的过程,因此在瞬态光电压的过程中采取了双光束策略,即用不同波长的光分别从两个半导体侧进行照光,以充分发挥内层CdS的电子传输层的作用.结果表明,在双光束照射下界面电场增强,使得更多Ti-Fe₂O₃电子与CdS空穴结合,使得更多Ti-Fe₂O₃电子与CdS空穴结合,更多的空穴迁移到Ti-Fe₂O₃的表面去参与反应,充分证明了CdS/Ti-Fe₂O₃光阳极的Z型迁移机制.基于界面电场有效的电荷迁移与分离的分析,对Z型异质结光阳极进行了光电化学的测试,与单纯Ti-Fe₂O₃光阳极相比,CdS/Ti-Fe₂O₃光阳极表现出优异的光电化学性能.其中,25CdS/Ti-Fe₂O₃光阳极的光电流密度在1.23V(相对于标准氢电极)达到1.94 mA/cm²,比单纯Ti-Fe₂O₃光电流高出两倍.阻抗测试结果表明,CdS/Ti-Fe₂O₃光阳极能够减小电荷传输阻力,从而加快电荷分离效率,这也间接证明了Z型光阳极的成功构筑,因此,本文提供了一个有效且新颖的手段来证明光电化学分解水中光催化系统的Z型电荷转移机制.     

Comparative study of the thermodynamics and kinetics of the ion transfer across the liquid/liquid interface by means of three-phase electrodes

A comparative study of the behavior of different sorts of three-phase electrodes applied for assessing the thermodynamics and kinetics of the ion transfer across the liquid/liquid (L/L) interface is presented. Two types of three-phase electrodes are compared, that is, a paraffin-impregnated graphite electrode at the surface of which a macroscopic droplet of an organic solvent is attached and an edge pyrolytic graphite electrode partly covered with a very thin film of the organic solvent. The organic solvent contains either decamethylferrocene or lutetium bis(tetra-tert-butylphthalocyaninato) as a redox probe. The role of the redox probe, the type of the electrode material, the mass transfer regime, and the effect of the uncompensated resistance are discussed. The overall electrochemical process at both three-phase electrodes proceeds as a coupled electron-ion transfer reaction. The ion transfer across the L/L interface, driven by the electrode reaction of the redox compound at the electrode/organic solvent interface, is independent of the type of redox probe. The ion transfer proceeds without involving any chemical coupling between the transferring ion and the redox probe. Both types of three-phase electrodes provide consistent results when applied for measuring the energy of the ion transfer. Under conditions of square-wave voltammetry, the coupled electron-ion transfer at the three-phase electrode is a quasireversible process, exhibiting the property known as "quasireversible maximum". The overall electron-ion transfer process at the three-phase electrode is controlled by the rate of the ion transfer. It is demonstrated for the first time that the three-phase electrode in combination with the quasireversible maximum is a new tool for assessing the kinetics of the ion transfer across the L/L interface.     

Surface diffusion in reversed-phase liquid chromatography

More than 40 years ago, Giddings pointed out in “Dynamics of Chromatography” that surface diffusion should become an important research topic in the kinetics of chromatographic phenomena. However, few studies on surface diffusion in adsorbents used in chromatography were published since then. Most scientists use ordinary rate equations to study mass transfer kinetics in chromatography. They take no account of surface diffusion and overlook the significant contributions of this mass transfer process to chromatographic behavior and to column efficiency at high mobile phase flow rate. Only recently did the significance of surface diffusion in separation processes begin to be recognized in connection with the development of new techniques of fast flow, high efficiency chromatography. In this review, we revisit the reports on experimental data on surface diffusion and introduce a surface-restricted molecular diffusion model, derived as a first approximation for the mechanism of surface diffusion, on the basis of the absolute rate theory. We also explain how this model accounts for many intrinsic characteristics of surface diffusion that cannot properly be explained by the conventional models of surface diffusion.     

Probing the Local Reaction Environment During High Turnover Carbon Dioxide Reduction with Ag-Based Gas Diffusion Electrodes

Discerning the influence of electrochemical reactions on the electrode microenvironment is an unavoidable topic for electrochemical reactions that involve the production of OH⁻ and the consumption of water. That is particularly true for the carbon dioxide reduction reaction (CO₂RR), which together with the competing hydrogen evolution reaction (HER) exert changes in the local OH⁻ and H₂O activity that in turn can possibly affect activity, stability, and selectivity of the CO₂RR. We determine the local OH⁻ and H₂O activity in close proximity to a CO₂-converting Ag-based gas diffusion electrode (GDE) with product analysis using gas chromatography. A Pt nanosensor is positioned in the vicinity of the working GDE using shear-force-based scanning electrochemical microscopy (SECM) approach curves, which allows monitoring changes invoked by reactions proceeding within an otherwise inaccessible porous GDE by potentiodynamic measurements at the Pt-tip nanosensor. We show that high turnover HER/CO₂RR at a GDE lead to modulations of the alkalinity of the local electrolyte, that resemble a 16 m KOH solution, variations that are in turn linked to the reaction selectivity.     

法拉第吸脱附偶联过程循环伏安行为的有限元分析

法拉第吸脱附偶联过程的电化学行为较为复杂,难以定量获得其表界面反应动力学信息. 本文通过COMSOL有限元软件对法拉第吸脱附偶联过程的循环伏安行为进行数值分析,研究了反应物或产物不同吸附条件下的循环伏安行为. 结果表明：当反应物或产物弱吸附时,可通过阴、阳极峰电流之差实现饱和吸附量的定量表征. 随着吸附平衡常数的增大,反应由弱吸附向强吸附过渡,峰电流由扩散峰与吸脱附峰相互重叠过渡到相互分离的吸脱附“前波”或“后波”特征. 该吸脱附特征峰的形状和位置与电势依赖的吸附平衡常数有关. 吸附平衡常数及其电势依赖程度越大,吸脱附峰偏离扩散峰越远,吸脱附峰越尖锐. 该模型为法拉第吸脱附偶联过程的循环伏安研究提供了一种定量研究方法,能够帮助研究者从复杂的吸脱附伏安行为中定量获得饱和吸附量和吸附平衡常数等信息,并对涉及吸脱附的电催化研究具有一定指导意义.