Hydrogen evolution curves

The increase of temperature with time in a hydrogen evolution experiment introduces an additional time dependence to the diffusion coefficient. The sample temperature is described by T = 7) + bt where 7) is the initial starting temperature. Previous analysis of the hydrogen evolution curves to extract a >H value have assumed that the only time dependence of >H arises from the heating rate term in T(t) (Beyer and Wagner, 1982). It turns out that the power-law time dependence of Z)H can be safely neglected in the evolution analysis. The effective diffusion time in a hydrogen evolution experiment with b = 20 K/min is less than one hour, so the decrease in... 

Figure 12. Theoretical hydrogen evolution curves using diffision equation for semi-infinite plane sheet (based on erf(x) five different initial diffusible hydrogen concentrations Dtrt = 7.5 x 105 cm2/sec).

Figure 2. Hydrogen evolution curves for normal and reduced pressure cycles with pyrrhotite (FeS) ( ), normal pressure cycle at 600°C (O), reduced pressure cycle at 550°C.

Figure 4. Hydrogen evolution curves for Ni3S2 at 550°C at the reduced pressure cycle (O), 1st (H ), 2nd (A), 6th.

The intersections of the respective anodic dissolution exudes and hydrogen evolution curves give the corrosion potentials and corrosion rates of M and N, j corr.M. and icorr,N. hi the uncoupled condition. 

Hydrogen evolution for binary Mg-Y alloys in 0.1 M NaCI. The corrosion rate can be evaluated as an instantaneous value from the slope of the hydrogen evolution curve or can be evaluated as an average value over a selected time period [10]. 

In oxygen-free seawater, the J(U) curves, together with the Tafel straight lines for hydrogen evolution, correspond to Eq. (2-19) (see Fig. 2-2lb). A limiting current density occurs with COj flushing for which the reaction ... 

Fig. 1.30 Corrosion of a metal in an acid in which both metal dissolution and hydrogen evolution are under activation control so that the .log i curves are linear, (a) Effect of pH on and I o Hi increase in pH (decrease in an + ) lowers E and decreases / o (b) Effect of...

Fig. 1.34 Corrosion and passivation of Fe-18Cr-SNi stainl s steel. Potentiosiatic anodic curve JKLM, hydrogen evolution reaction, curve Hl low concentration of dissolved oxygen, curve t> FG, high concentration of dissolved oxygen, curve AflC (Section 3...

However, when the second stage in the hydrogen evolution reaction is electrochemical desorption, the rate of this reaction is increased as the potential falls, and the adsorbed hydrogen concentration may remain constant or fall, according to the detailed electrochemistry. This results in curves such as that shown in Fig. 8.38 for steel in sodium chloride solution. 

The presence of hydrogen in pre-exposed specimens was revealed by straining specimens in vacuo. Hydrogen evolution occurred in the elastic region of the stress/strain curve, an effect that had been shown to be very much reduced by electropolishing pre-exposed specimens prior to testing... 

The relation between E and t is S-shaped (curve 2 in Fig. 12.10). In the initial part we see the nonfaradaic charging current. The faradaic process starts when certain values of potential are attained, and a typical potential arrest arises in the curve. When zero reactant concentration is approached, the potential again moves strongly in the negative direction (toward potentials where a new electrode reaction will start, e.g., cathodic hydrogen evolution). It thus becomes possible to determine the transition time fiinj precisely. Knowing this time, we can use Eq. (11.9) to find the reactant s bulk concentration or, when the concentration is known, its diffusion coefficient. 

Adsorption of surface-active substances is attended by changes in EDL structure and in the value of the / -potential. Hence, the effects described in Section 14.2 will arise in addition. When surface-active cations [NR] are added to an acidic solution, the / -potential of the mercury electrode will move in the positive direction and cathodic hydrogen evolution at the mercury, according to Eq. (14.16), will slow down (Fig. 14.6, curve 2). When I ions are added, the reaction rate, to the contrary, will increase (curve 3), owing to the negative shift of / -potential. These effects disappear at potentiafs where the ions above become desorbed (at vafues of pofarization of less than 0.6 V in the case of [NR]4 and at values of polarization of over 0.9 V in the case of I ). 

FIGURE 14.6 Influence of surface-active ions [N(C4H9)4]+ (curve 2) and I (curve 3) on the polarization curve for hydrogen evolution at a mercury electrode in acidic solutions (curve 1 is for the base electrolyte). 

Figure 15.2 shows polarization curves for hydrogen evolution at electrodes of different metals in acidic electrolyte solutions. The results of polarization measurements are highly sensitive to the experimental conditions, in particular to the degree of solution and electrode surface purification for this reason, marked differences exist among the data reported by different workers. The curves shown still provide the correct picture of the common features. 

FIGURE 15.2 Polarization curves for hydrogen evolution with various metals in acidic solutions. 

The polarization curves for the oxygen evolution reaction are more complex than those for hydrogen evolution. Usually, several Tafel sections with different slopes are present. At intermediate CD their slope b is very close to 0.12 V, but at low CD it sometimes falls to 0.06 V. At high CD higher slopes are found at potentials above 2.2 V (RHE) new phenomena and processes are possible, which are considered in Section 15.6. 

FIGURE 22.2 Schematic polarization curves for spontaneous dissolution (a) of active metals (h) of passivated metals. (1,2) Anodic curves for active metals (3) cathodic curve for hydrogen evolution (4) cathodic curve for air-oxygen reduction (5) anodic curve of the passivated metal. 

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.

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