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Hydrogen evolution Equation

Equation (24-68a) means that the protection potential, U, must be reached at the end of the pipeline (x = L), and that at the drainage point x = 0), the potential must not fall below because due to hydrogen evolution, according to Eq. (2-19), Eq. (24-67)... [Pg.552]

It follows from equation 1.45 that the corrosion rate of a metal can be evaluated from the rate of the cathodic process, since the two are faradai-cally equivalent thus either the rate of hydrogen evolution or of oxygen reduction may be used to determine the corrosion rate, providing no other cathodic process occurs. If the anodic and cathodic sites are physically separable the rate of transfer of charge (the current) from one to the other can also be used, as, for example, in evaluating the effects produced by coupling two dissimilar metals. There are a number of examples quoted in the literature where this has been achieved, and reference should be made to the early work of Evans who determined the current and the rate of anodic dissolution in a number of systems in which the anodes and cathodes were physically separable. [Pg.83]

The hydrogen evolution reaction (h.e.r.) and the oxygen reduction reaction (equations 1.11 and 1.12) are the two most important cathodic processes in the corrosion of metals, and this is due to the fact that hydrogen ions and water molecules are invariably present in aqueous solution, and since most aqueous solutions are in contact with the atmosphere, dissolved oxygen molecules will normally be present. [Pg.96]

Figure 3.16 Volcano plot for the hydrogen evolution reaction (HER) for various pure metals and metal overlayers. Values are calculated at 1 barof H2 (298K) and at a surface hydrogen coverage of either 0.25 or 0.33 ML. The two curved lines correspond to the model (3.24), (3.25) transfer coefficients (not included in the indicated equations) of 0.5 and 1.0, respectively, have also been added to the model predictions in the figure. The current values for specific metals are taken from experimental data on polycrystalline pure metals, single-crystal pure metals, and single-crystal Pd overlayers on various substrates. Adapted from [Greeley et al., 2006a] see this reference for more details. Figure 3.16 Volcano plot for the hydrogen evolution reaction (HER) for various pure metals and metal overlayers. Values are calculated at 1 barof H2 (298K) and at a surface hydrogen coverage of either 0.25 or 0.33 ML. The two curved lines correspond to the model (3.24), (3.25) transfer coefficients (not included in the indicated equations) of 0.5 and 1.0, respectively, have also been added to the model predictions in the figure. The current values for specific metals are taken from experimental data on polycrystalline pure metals, single-crystal pure metals, and single-crystal Pd overlayers on various substrates. Adapted from [Greeley et al., 2006a] see this reference for more details.
Table 5.5 Constants a and b of the Tafel equation and the probable mechanism of the hydrogen evolution reaction at various electrodes with H30+ as electroactive species (aH3o+ ) (According to L. I. Krishtalik)... [Pg.365]

Schuldiner (1959) studied the effect of H2 pressure on the hydrogen evolution reaction at bright (polished) Pt in sulphuric acid. The mechanism of the reaction was assumed to be as in equations (3.3) and (3.4). The step represented by equation (3.3) was assumed to be at equilibrium at all potentials and equation (3.4) represented the rate-determining step. The potentials were measured as overpotentials with respect to the hydrogen potential, i.e. the potential of the H +/H2 couple in the solution (0 V vs. RHE). [Pg.249]

If the coverage of the adsorbed hydrogen intermediate is I at the hydrogen potential, i.e. 0O = 1, then equation (3.27) would most certainly be inapplicable to the observed data. On the other hand, Schuldiner reasoned that if 0O was very low and the coverage only increased slowly as the potential was moved into the hydrogen evolution region, then equation (3.27) reduces to ... [Pg.250]

Hydrogen evolution, the other reaction studied, is a classical reaction for electrochemical kinetic studies. It was this reaction that led Tafel (24) to formulate his semi-logarithmic relation between potential and current which is named for him and that later resulted in the derivation of the equation that today is called "Butler-Volmer-equation" (25,26). The influence of the electrode potential is considered to modify the activation barrier for the charge transfer step of the reaction at the interface. This results in an exponential dependence of the reaction rate on the electrode potential, the extent of which is given by the transfer coefficient, a. [Pg.287]

A hydrogen evolution rate of about 35 pmol/hr over the first few hours of reaction using NiO powder was reported. This decreased with time reaching a value of 20 pmol/h after 55 hours. The energy efficiency was calculated using the equation [206]... [Pg.85]

Equation 16.9 tells us that the protective oxide film on iron will be preserved in alkaline media, weakened in neutral water, and lost in acidic environments. Indeed, in very acidic solutions, the distinction between extended anodic and cathodic sites will be lost along with the oxide film, although local anodic and cathodic spots will persist, and so dissolution of iron with accompanying hydrogen evolution becomes general across the surface of the specimen. [Pg.334]

Equation 7 shows the interaction of ferricyanide and cobaltocyanide to form a binuclear complex as described by Haim and Wilmarth (4). It is probable that the hydrogen evolution noted occurs via displacement of the equilibrium shown in Equation 6. Equation 8 defines the role of alkali, the presence of which is required to effect the catalytic reduction of ferricyanide. The hydroxo complex so obtained may then undergo the reverse aging process shown in Equation 5 to reform cyanocobaltate(II), which then absorbs hydrogen. The over-all result is reduction of ferri- to ferrocyanide by hydrogen. [Pg.215]

Pour 5 ml of a 1 W hydrochloric acid solution into a test tube and throw a small piece of zinc into it. When the evolution of hydrogen becomes quite vigorous, add 1-2 g of sodium acetate. Explain the change in the rate of hydrogen evolution. Write the molecular and net ionic equations of the chemical reaction of hydrochloric acid with sodium acetate. Does the activity of acetic acid decrease when dry sodium acetate is added to its solution ... [Pg.86]

The actual current passed / = 2F/4Jt,[H + ]exp[ — J pAE] since two electrons are transferred for every occurrence of reaction I. Equation (1.64) constitutes the fundamental kinetic equation for the hydrogen evolution reaction (her) under the conditions that the first reaction is rate limiting and that the reverse reaction can be neglected. From this equation, we can calculate the two main observables that can be measured in any electrochemical reaction. The first is the Tafel slope, defined for historical reasons as ... [Pg.38]

Highly reactive halogen-substituted silanes were understandably avoided in earlier mechanism studies, and attention was devoted instead to the hydrolytic and solvolytic cleavage of the more stable Si-H bond. The reaction, most simply represented by the expression, SiH -)- H20 - SiOH -f- H2, is strongly base catalyzed. However, as Price (55) pointed out, the stoichiometry is represented better by the equation SiH + ROH -j- OH - - SiOH + OR- -)- H2. Price found that the rate of hydrogen evolution is given by the expression kx t = In [VF[VF— V]... [Pg.457]


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See also in sourсe #XX -- [ Pg.3 , Pg.270 , Pg.271 ]




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