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Electrode solution

Migration is the movement of ions due to a potential gradient. In an electrochemical cell the external electric field at the electrode/solution interface due to the drop in electrical potential between the two phases exerts an electrostatic force on the charged species present in the interfacial region, thus inducing movement of ions to or from the electrode. The magnitude is proportional to the concentration of the ion, the electric field and the ionic mobility. [Pg.1925]

The potential of a metallic electrode is determined by the position of a redox reaction at the electrode-solution interface. Three types of metallic electrodes are commonly used in potentiometry, each of which is considered in the following discussion. [Pg.473]

Controlled-potential coulometry also can be applied to the quantitative analysis of organic compounds, although the number of applications is significantly less than that for inorganic analytes. One example is the six-electron reduction of a nitro group, -NO2, to a primary amine, -NH2, at a mercury electrode. Solutions of picric acid, for instance, can be analyzed by reducing to triaminophenol. [Pg.502]

When two conducting phases come into contact with each other, a redistribution of charge occurs as a result of any electron energy level difference between the phases. If the two phases are metals, electrons flow from one metal to the other until the electron levels equiUbrate. When an electrode, ie, electronic conductor, is immersed in an electrolyte, ie, ionic conductor, an electrical double layer forms at the electrode—solution interface resulting from the unequal tendency for distribution of electrical charges in the two phases. Because overall electrical neutrality must be maintained, this separation of charge between the electrode and solution gives rise to a potential difference between the two phases, equal to that needed to ensure equiUbrium. [Pg.510]

On the electrode side of the double layer the excess charges are concentrated in the plane of the surface of the electronic conductor. On the electrolyte side of the double layer the charge distribution is quite complex. The potential drop occurs over several atomic dimensions and depends on the specific reactivity and atomic stmcture of the electrode surface and the electrolyte composition. The electrical double layer strongly influences the rate and pathway of electrode reactions. The reader is referred to several excellent discussions of the electrical double layer at the electrode—solution interface (26-28). [Pg.510]

Eigure 3 schematically depicts the stmcture of the electrode—solution interface. The inner Helmholtz plane (IHP) refers to the distance of closest approach of specifically adsorbed ions, generally anions to the electrode surface. In aqueous systems, water molecules adsorb onto the electrode surface. [Pg.510]

Pig. 3. Representation of the electrical double layer at a metal electrode—solution interface for the case where anions occupy the inner Helmholtz plane... [Pg.510]

Fig. 7. (a) Simple battery circuit diagram where represents the capacitance of the electrical double layer at the electrode—solution interface, W depicts the Warburg impedance for diffusion processes, and R is internal resistance and (b) the corresponding Argand diagram of the behavior of impedance with frequency, for an idealized battery system, where the characteristic behavior of A, ohmic B, activation and C, diffusion or concentration (Warburg... [Pg.514]

Transport of a species in solution to and from an electrode/solution interface may occur by migration, diffusion and convection although in any specific system they will not necessarily be of equal importance. However, at the steady state all steps involved in the electrode reaction must proceed at the same rate, irrespective of whether the rate is controlled by a slow step in the charge transfer process or by the rate of transport to or from the electrode surface. It follows that the rate of transport must equal the rate of charge transfer ... [Pg.1199]

In a cathodic process, removal of ions from solutions will result in a decrease in their concentration at the electrode/solution interface compared to that in the bulk solution, and this in turn will cause a concentration gradient and consequent diffusion. Furthermore, the potential gradient... [Pg.1199]

Activation Overpotential that part of an overpotential (polarisation) that exists across the electrical double layer at an electrode/solution interface and thus directly influences the rate of the electrode process by altering its activation energy. [Pg.1363]

Concentration (diffusion or transport) Overpotential change of potential of an electrode caused by concentration changes near the electrode/solution interface produced by an electrode reaction. [Pg.1365]

Controlled-potential (potentiostatic) techniques deal with the study of charge-transfer processes at the electrode-solution interface, and are based on dynamic (no zero current) situations. Here, the electrode potential is being used to derive an electron-transfer reaction and the resultant current is measured. The role of the potential is analogous to that of the wavelength in optical measurements. Such a controllable parameter can be viewed as electron pressure, which forces the chemical species to gain or lose an electron (reduction or oxidation, respectively). [Pg.2]

Accordingly, the resulting current reflects the rate at which electrons move across the electrode-solution interface. Potentiostatic techniques can thus measure any chemical species that is electroactive, in other words, that can be made to reduce or oxidize. Knowledge of the reactivity of functional group in a given compound can be used to predict its electroactivity. Nonelectroactive compounds may also be detected in connection with indirect or derivatization procedures. [Pg.3]

This chapter attempts to give an overview of electrode processes, together with discussion of electron transfer kinetics, mass transport, and the electrode-solution interface. [Pg.3]

The charging of the double layer is responsible for the background (residual) current known as the charging current, which limits die detectability of controlled-potential techniques. Such a charging process is nonfaradaic because electrons are not transferred across the electrode-solution interface. It occurs when a potential is applied across the double layer, or when die electrode area or capacitances are changing. Note that the current is the tune derivative of die charge. Hence, when such processes occur, a residual current flows based on die differential equation... [Pg.21]

When the electrode/solution system contains substances that are oxidized or reduced faster than the surface can be renewed, the potentials observed during the surface renewal are shifted. [Pg.39]

The entropy of formation of the interface was calculated from the temperature coefficient of the interfacial tension.304 The entropy of formation has been found to increase with the nature of the electrolyte in the same sequence as the single cation entropy in DMSO.108, 09,329 The entropy of formation showed a maximum at negative charges. The difference in AS between the maximum and the value at ff=ocan be taken as a measure of the specific ordering of the solvent at the electrode/solution interface. Data 108,109304314 have shown that A(AS) decreases in the sequence NMF > DMSO > DMF > H90 > PC > MeOH. [Pg.61]

Habib, M. A. Solvent Dipoles at the Electrode-Solution Interface 12... [Pg.604]

Fio. 8. Schematic representation of the electrode-solution interface and the potential distribution in this zone. [Pg.185]

Measurement of the differential capacitance C = d /dE of the electrode/solution interface as a function of the electrode potential E results in a curve representing the influence of E on the value of C. The curves show an absolute minimum at E indicating a maximum in the effective thickness of the double layer as assumed in the simple model of a condenser [39Fru]. C is related to the electrocapillary curve and the surface tension according to C = d y/dE. Certain conditions have to be met in order to allow the measured capacity of the electrochemical double to be identified with the differential capacity (see [69Per]). In dilute electrolyte solutions this is generally the case. [Pg.183]


See other pages where Electrode solution is mentioned: [Pg.203]    [Pg.203]    [Pg.203]    [Pg.204]    [Pg.511]    [Pg.511]    [Pg.513]    [Pg.72]    [Pg.203]    [Pg.203]    [Pg.599]    [Pg.1]    [Pg.23]    [Pg.45]    [Pg.66]    [Pg.31]    [Pg.33]    [Pg.64]    [Pg.84]    [Pg.127]    [Pg.179]    [Pg.185]    [Pg.191]    [Pg.192]    [Pg.196]    [Pg.197]   


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APPROXIMATE ANALYTICAL SOLUTIONS FOR MODELS OF THREE-DIMENSIONAL ELECTRODES BY ADOMIANS ECOMPOSITION METHOD Keith Scott and Yan-Ping Sun ntroduction

Adlayer structures, electrode/solution interface

Analytical solution channel electrode

Analytical solution rotating disc electrode

Anion structures, electrode/solution interface

Carbon electrodes aqueous solution

Diffraction studies, electrode/solution interface

Dye Molecules Adsorbed on the Electrode and in Solution

Electric Double-Layer at Interface of Electrode and Electrolyte Solution

Electrode conditioning solution

Electrode solution pressure

Electrode solution/metal interface

Electrode surfaces electrolyte solution flow rate

Electrode-solution interface

Electrode-solution interface electrochemical processes

Electrode-solution interface model

Electrode-solution interface specular reflection

Electrode-solution interface supramolecular

Electrode-solution interface, diffusion

Electrode-solution interface, structural

Electrode-solution interface, structural control

Electrode-solution interfacial phenomena

Electrode/solution interface Subject

Electrodes evolution from acid solutions

Electrodes oxygen solution

Electrodes solution pool

Face-centered cubic , electrode/solution

Forced convection electrode, solution boundary

Homogenous Solution Catalysts at Semiconductor Electrodes

In-Situ STM Study of Electrode-Aqueous Solution Interfaces

Interphase electrode-solution

Interphase electrode-solution electrical field

Interphase electrode-solution forces

Interphase electrode-solution structure

Mercury electrodes aqueous solution

Metal crystals, electrode/solution interface

Metal electrode dipping into an aqueous solution of its ions

Metal-solution interfaces that approach electrodes

Oxidation-reduction reactions, in solution and at electrodes

Oxides, electrode/solution interface

Oxides, electrode/solution interface 424 Subject

Platinizing electrodes solution

Platinum electrodes aqueous solution

Platinum electrodes in aqueous solution

Positive electrodes solution, addition

Potential perturbation, electrode—solution interface

Reconstruction, electrode/solution interface

Reduction in Aqueous Solutions at Metal Electrodes

Reduction in Nonaqueous Solutions at Metal Electrodes

Reference Electrodes for Non-Aqueous Solutions

Reference Electrodes for Use in Aqueous Solutions

Reference electrode solution

Reference electrodes, aqueous solutions

Reference electrodes, aqueous solutions bridge

Reference electrodes, aqueous solutions ionic liquids

Reference electrodes, aqueous solutions mercury

Reference electrodes, aqueous solutions miniaturized

Reference electrodes, aqueous solutions polymer membranes

Reference electrodes, aqueous solutions solid contact

Reference electrodes, for aqueous solutions

Relaxation electrode/solution interface

Reporting Electrode Potentials in Non-Aqueous Solutions (IUPAC Recommendation)

Rotating disk electrode convective-diffusion equation, solution

Rotating disk electrode electrolyte solutions

Saturated solution reference electrode

Single electrode/solution interface

Solution reactivity properties electrode transferal

Solution resistance reference electrode

Spectroscopy electrode/solution interface

Specular reflection, electrode-solution

Standard Electrode (Reduction) Potentials in Aqueous Solution at

Standard Electrode Potentials Aqueous Solutions

Standard Electrode Potentials for Aqueous Solutions

Surfaces electrode/solution interface

The Zinc Electrode in Alkaline Solutions

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