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Potential Relationship

Anodic behavior of sihcon can best be characterized by i-V curves. Neglecting the details associated with a silicon substrate such as doping, the current-potential relationship of silicon in aqueous solutions can be considered to be principally determined by the pH and HE concentration as illustrated in Pig. 5.1. In nonalkaline and nonfluoride aqueous solutions, silicon as an electrode is essentially inert, showing a very small current at anodic potential due to the presence of a thin oxide film. In alkaline solutions, silicon is also passivated by an oxide film at anodic potentials but is active below the passivation potential, Vp. In fluoride solutions, the silicon electrode is active in the whole anodic region as shown by the large anodic current. [Pg.167]

FIGURE 5.1. Typical i V curve in HF and nonfluoride, nonalkaline solutions. [Pg.168]


Fig. 4. Capacitance—potential relationship at a mercury electrode for a nonspecific absorbiag electrolyte where regions A and B represent inner layer anions... Fig. 4. Capacitance—potential relationship at a mercury electrode for a nonspecific absorbiag electrolyte where regions A and B represent inner layer anions...
Fig. 2-6 Current-potential relationships for a heterogeneous mixed eleetrode or for eell formation (explanation in the text). Fig. 2-6 Current-potential relationships for a heterogeneous mixed eleetrode or for eell formation (explanation in the text).
Figure 1.62b shows the result of raising the potential of a corroding metal. As the potential is raised above B, the current/potential relationship is defined by the line BD, the continuation of the local cell anodic polarisation curve, AB. The corrosion rate of an anodically polarised metal can very seldom be related quantitatively by Faraday s law to the external current flowing, Instead, the measured corrosion rate will usually exceed... [Pg.214]

The extent of galvanic effects will be influenced by, in addition to the usual factors that affect corrosion of a single metal, the potential relationships of the metals involved, their polarisation characteristics, the relative areas of anode and cathode, and the internal and external resistances in the galvanic circuit (see Section 1.7). [Pg.1018]

The current-potential relationship ABCDE, as obtained potentiosta-tically, has allowed a study of the passive phenomena in greater detail and the operational definition of the passive state with greater preciseness. Bonhoeffer, Vetter and many others have made extensive potentiostatic studies of iron which indicate that the metal has a thin film, composed of one or more oxides of iron, on its surface when in the passive state . Similar studies have been made with stainless steel, nickel, chromium and other metals... [Pg.1110]

Fig. 20.7 Differential capacitance/mercury electrode potential relationships for potassium chloride at different concentrations showing (a) how minima are obtained only at low concentrations and (6) the constant capacitance at negative potentials (after Bockris and Drazic )... Fig. 20.7 Differential capacitance/mercury electrode potential relationships for potassium chloride at different concentrations showing (a) how minima are obtained only at low concentrations and (6) the constant capacitance at negative potentials (after Bockris and Drazic )...
In this section we consider experiments in which the current is controlled by the rate of electron transfer (i.e., reactions with sufficiently fast mass transport). The current-potential relationship for such reactions is different from those discussed (above) for mass transport-controlled reactions. [Pg.11]

When the area A of the eleetrode/solution interface with a redox system in the solution varies (e.g. when using a streaming mercury electrode), the double layer capacity which is proportional to A, varies too. The corresponding double layer eharging current has to be supplied at open eireuit eonditions by the Faradaic current of the redox reaction. The associated overpotential can be measured with respect to a reference electrode. By measuring the overpotential at different capaeitive eurrent densities (i.e. Faradaic current densities) the current density vs. eleetrode potential relationship can be determined, subsequently kinetic data can be obtained [65Del3]. (Data obtained with this method are labelled OC.)... [Pg.271]

Beside laminar flow created by e.g. a rotating disc electrode mrbulent flow provides a means of artificially enhanced transport. A consistent mathematical description and analytical treatment of this mode of transportation is not possible. Various approximations have been proposed and tested for correctness [84Barl], an experimental setup has been described [78Ber, 83Her, 831wa]. From comparisons of measured and calculated current density vs. electrode potential relationships exchange current densities are available. (Data obtained with this method are labelled TPF.)... [Pg.273]

The current-potential relationship indicates that the rate determining step for the Kolbe reaction in aqueous solution is most probably an irreversible 1 e-transfer to the carboxylate with simultaneous bond breaking leading to the alkyl radical and carbon dioxide [8]. However, also other rate determining steps have been proposed [10]. When the acyloxy radical is assumed as intermediate it would be very shortlived and decompose with a half life of t 10" to carbon dioxide and an alkyl radical [89]. From the thermochemical data it has been concluded that the rate of carbon dioxide elimination effects the product distribution. Olefin formation is assumed to be due to reaction of the carboxylate radical with the alkyl radical and the higher olefin ratio for propionate and butyrate is argued to be the result of the slower decarboxylation of these carboxylates [90]. [Pg.97]

The aim of this exercise is for individuals to handle potential relationship problems in the most effective way. The duration of the exercise is highly variable, depending on how many scenarios you wish to discuss. [Pg.289]

LeNoir J, Aston L, Datta S, et al. 1998. Pesticides and polychlorinated biphenyls in Sierra Nevada ecosystems Potential relationship to decline of amphibians. Division of Environmental Chemistry Preprints of Extended Abstracts 38(2) 264-266. [Pg.218]

Sweitzer SM, Hickey WF et al (2002) Focal peripheral nerve injury induces leukocyte trafficking into the central nervous system potential relationship to neuropathic pain. Pain 100(1-2) 163-170... [Pg.84]

Figure 4.4 Schematic diagram of the free energy calculated from (4.4), Fftee. versus potential cf> for the generic electrocatalytic reaction A —> B. Points indicated hy squares and circles are for specific external charges (various q) for the systems A and B, respectively. Solid and dashed lines indicate the best-fit curves for the free energy versus potential relationship for systems A and B, respectively. Figure 4.4 Schematic diagram of the free energy calculated from (4.4), Fftee. versus potential cf> for the generic electrocatalytic reaction A —> B. Points indicated hy squares and circles are for specific external charges (various q) for the systems A and B, respectively. Solid and dashed lines indicate the best-fit curves for the free energy versus potential relationship for systems A and B, respectively.
The current-potential relationship predieted by Eqs. (49) and (50) differs strongly from the Butler-Volmer law. For y 1 the eurrent density is proportional to the eleetro-static driving force. Further, the shape of the eurrent-potential curves depends on the ratio C1/C2 the curve is symmetrical only when the two bulk concentrations are equal (see Fig. 19), otherwise it can be quite unsymmetrieal, so that the interface can have rectifying properties. Obviously, these current-potential eurves are quite different from those obtained from the lattice-gas model. [Pg.187]

Heterogeneous ET reactions at polarizable liquid-liquid interfaces have been mainly approached from current potential relationships. In this respect, a rather important issue is to minimize the contribution of ion-transfer reactions to the current responses associated with the ET step. This requirement has been recognized by several authors [43,62,67-72]. Firstly, reactants and products should remain in their respective phases within the potential range where the ET process takes place. In addition to redox stability, the supporting electrolytes should also provide an appropriate potential window for the redox reaction. According to Eqs. (2) and (3), the redox potentials of the species involved in the ET should match in a way that the formal electron-transfer potential occurs within the potential window established by the transfer of the ionic species present at the liquid-liquid junction. The results shown in Figs. 1 and 2 provide an example of voltammetric ET responses when the above conditions are fulfilled. A difference of approximately 150 mV is observed between Ao et A" (.+. ... [Pg.199]

A study was conducted on 21 children, aged 18 to 36 months, to examine the potential relationship between the amounts of lead ingested in food and anthropometric measurements (height, weight, head circumference, and mid-upper arm circumference) (Stanek et al. 1998). The children resided in homes... [Pg.77]

Additional studies in rats in vivo and in rat tissues or cells in vitro have focused on potential relationships between the effects of lead on neurotransmitter systems and neurobehavioral function. Lead exposure decreased dopamine binding sites, suggesting excess dopamine availability. The decreased dopamine binding was localized in the nucleus accumbens (mesolimbic dopamine system) but not the dorsal... [Pg.268]

The two-step charge transfer [cf. Eqs. (7) and (8)] with formation of a significant amount of monovalent aluminum ion is indicated by experimental evidence. As early as 1857, Wholer and Buff discovered that aluminum dissolves with a current efficiency larger than 100% if calculated on the basis of three electrons per atom.22 The anomalous overall valency (between 1 and 3) is likely to result from some monovalent ions going away from the M/O interface, before they are further oxidized electrochemically, and reacting chemically with water further away in the oxide or at the O/S interface.23,24 If such a mechanism was operative with activation-controlled kinetics,25 the current-potential relationship should be given by the Butler-Volmer equation... [Pg.411]

The electrochemical detection of pH can be carried out by voltammetry (amper-ometry) or potentiometry. Voltammetry is the measurement of the current potential relationship in an electrochemical cell. In voltammetry, the potential is applied to the electrochemical cell to force electrochemical reactions at the electrode-electrolyte interface. In potentiometry, the potential is measured between a pH electrode and a reference electrode of an electrochemical cell in response to the activity of an electrolyte in a solution under the condition of zero current. Since no current passes through the cell while the potential is measured, potentiometry is an equilibrium method. [Pg.287]

Several binary alloys of technological importance are known to form by way of an underpotential co-deposition mechanism. The abnormal composition-potential relationship observed in Cu-Zn alloys deposited from cyanide-based electrolytes, one of the most widely used commercial alloy plating processes, is attributed to the underpotential co-deposition of Zn [64]. The UPD of Zn is also known to occur on Co and Fe and has been included in treatments focusing on the anomalous co-deposition of Co-Zn [65] and Ni-Zn alloys [66-68]. Alloys of Cu-Cd have been shown to incorporate Cd at underpotentials when deposited from ethylene diamine solution [69-71]. [Pg.286]

Modeling the Mn-Al system is particularly difficult because the kinetics of the Mn and A1 deposition reactions can not be measured directly. Although it is possible to estimate the current-potential relationships for both Mn and A1 from electrodeposit composition, no examination along these lines appears in the literature. A close ex-... [Pg.316]

Denote the forward and backward rate constants of this reaction by ka and kb- When the reaction proceeds under stationary conditions, the rates of the chemical and of the electron-transfer reaction are equal. Derive the current-potential relationship for this case. Assume that the concentrations of A and of the oxidized species are constant. [Pg.64]

The pH shift model of Park and Regalbuto combined (1) a proton balance between the surface and bulk liquid with (2) the protonation-deprotonation chemistry of the oxide surface (single amphoteric site), and (3) a surface charge-surface potential relationship assumed for an... [Pg.170]

Stationary and mobile fuel cells could have a potential relationship that goes beyond cost and volume. A fuel cell in a vehicle is a multi-kilo-watt power generator on wheels, which is driven about 5% of the time and parked the other 95% of the time. [Pg.187]

Because of the different potential distributions for different sets of conditions the apparent value of Tafel slope, about 60 mV, may have contributions from the various processes. The exact value may vary due to several factors which have different effects on the current-potential relationship 1) relative potential drops in the space charge layer and the Helmholtz layer 2) increase in surface area during the course of anodization due to formation of PS 3) change of the dissolution valence with potential 4) electron injection into the conduction band and 5) potential drops in the bulk semiconductor and electrolyte. [Pg.180]

We may thus translate the current and potential relationships of Section 1.3.1 [equations (1.11)] into the following dimensionless equations ... [Pg.357]


See other pages where Potential Relationship is mentioned: [Pg.667]    [Pg.686]    [Pg.13]    [Pg.272]    [Pg.272]    [Pg.289]    [Pg.209]    [Pg.253]    [Pg.300]    [Pg.80]    [Pg.439]    [Pg.220]    [Pg.333]    [Pg.143]    [Pg.126]    [Pg.382]    [Pg.75]    [Pg.53]    [Pg.78]    [Pg.286]    [Pg.69]    [Pg.99]   


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Butler—Volmer equation current—potential relationship

Charge-potential relationships

Charge-potential relationships electric double layer

Chemical Potentials and Equilibrium Relationships

Chemical potential Gibbs energy relationship

Copper electrode potential relationships

Corrosion current-potential relationship

Current potential relationship

Current-concentration relationships, potential

Current-concentration relationships, potential voltammetry

Current-potential relationship for steady-state electron transfer

Flux-potential relationship

From Chemical Potential to Electronegativity Relationships

Ionization potential electron affinity, relationship between

Linear current-potential relationship

Photocurrent-potential relationship

Polarization resistance current-potential relationships

Potential energy Hamiltonian function relationship

Potential-concentration relationships

Potential-time relationships

Quantitative structure-activity relationships potentially applicable

Redox potential-structure relationships

Relationship Between Current and Electrode Potential

Relationship Between Rate and Potential Under Stationary Diffusion

Relationship Between Tumor Cell Trafficking and Metastatic Potential

Relationships between potential functions and the vibration-rotation levels

Rotating disk electrode current-potential relationship

Surface Charge-Potential Relationship

The Current-Potential Relationship

The General Relationship between Current and Potential at an Interface

The relationships between standard reduction potentials and some other quantities

Thermochemical Relationships and Potential Energy Surfaces

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