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Electrode galvanically coupled

A nonuniform distribution of the reactions may arise when the metal s surface is inhomogeneous, particularly when it contains inclusions of other metals. In many cases (e.g., zinc with iron inclusions), the polarization of hydrogen evolution is much lower at the inclusions than at the base metal hence, hydrogen evolution at the inclusions will be faster (Fig. 22.3). Accordingly, the rate of the coupled anodic reaction (dissolution of the base metal) will also be faster. The electrode s OCP will become more positive under these conditions. At such surfaces, the cathodic reaction is concentrated at the inclusions, while the anodic reaction occurs at the base metal. This mechanism is reminiscent of the operation of shorted galvanic couples with spatially separated reactions Metal dissolves from one electrode hydrogen evolves at the other. Hence, such inclusions have been named local cells or microcells. [Pg.382]

From this equation it can been seen that as the ohmic resistance increases, the remaining voltage driving force available to increase the overpotentials of the anode or cathode is diminished. Consequently smaller total current, I, flows through the cell. This is shown in Fig. 2, where in the absence of a finite Ra there is a single galvanic couple potential. A similar argument can be developed for the case of a driven two-electrode system. [Pg.178]

Figure 30 The general form of the crevice current (7C), crevice potential (Ec), and planar electrode potential (E ) measured using a galvanic coupling technique. (A) Range of planar electrode (corrosion) potentials (Ef) measured for passive corrosion under oxidizing conditions (B) range of Ef. values measured for passive corrosion under anoxic conditions (C) range of crevice potentials (Ec) measured during active crevice propagation. Figure 30 The general form of the crevice current (7C), crevice potential (Ec), and planar electrode potential (E ) measured using a galvanic coupling technique. (A) Range of planar electrode (corrosion) potentials (Ef) measured for passive corrosion under oxidizing conditions (B) range of Ef. values measured for passive corrosion under anoxic conditions (C) range of crevice potentials (Ec) measured during active crevice propagation.
Note the potentials of the graphite and the aluminum alloy that you determined. If these two are connected with an electrical contact, their potentials should move toward each other. Further, since the solution is relatively conductive, and assuming that the electrical lead connecting them was highly conductive, they would come to the same potential. Therefore connect the leads of the two electrodes together and connect them both to the positive (or V) lead of the voltmeter. Measure the potential of this galvanic couple relative to one of the reference electrodes and confirm that the couple potential does indeed rest somewhere in between the corrosion potentials of the two materials. [Pg.362]

Figure 6 - Galvanic couple potential and ZRA vs. time at 100 rpm agitation, pH 10.5, 0.01 M cyanide cone., saturated atmospheric oxygen, 25 °C, (a) RGO (roasted gold ore electrode 4.9 cm2) and Mag (magnetite disc electrode 4.9 cm2) (b) RGO (roasted gold ore electrode 4.9 cm2) and Hem (hematite disc electrode 4.9 cm2)... Figure 6 - Galvanic couple potential and ZRA vs. time at 100 rpm agitation, pH 10.5, 0.01 M cyanide cone., saturated atmospheric oxygen, 25 °C, (a) RGO (roasted gold ore electrode 4.9 cm2) and Mag (magnetite disc electrode 4.9 cm2) (b) RGO (roasted gold ore electrode 4.9 cm2) and Hem (hematite disc electrode 4.9 cm2)...
Figure 8 - SEM (a) and EDS (b) images of Au electrode surface after galvanic coupling with Mag disc electrode, pH 10.5 at 100 rpm, cyanide cone. 0.01 M, 25 °C, saturated atmospheric oxygen, Au electrode... Figure 8 - SEM (a) and EDS (b) images of Au electrode surface after galvanic coupling with Mag disc electrode, pH 10.5 at 100 rpm, cyanide cone. 0.01 M, 25 °C, saturated atmospheric oxygen, Au electrode...
The conventional approach to corrosion is to start directly with the concept of a mixed electrode of indistinguishable distribution of sites for the anodic and cathodic reactions. The approach taken in this chapter is to first examine the behavior of distinguishable anodic and cathodic sites. This is the classical case of galvanic couples of joined dissimilar metals in contact with a common solution. In this case, local movement of a reference electrode through the solution can map the... [Pg.128]

When two metals or alloys are joined such that electron transfer can occur between them and they are placed in an electrolyte, the electrochemical system so produced is called a galvanic couple. Coupling causes the corrosion potentials and corrosion current densities to change, frequently significantly, from the values for the two metals in the uncoupled condition. The magnitude of the shift in these values depends on the electrode kinetics parameters, i0 and (3, of the cathodic and anodic reactions and the relative magnitude of the areas of the two metals. The effect also depends on the resistance of the electrochemical cir-... [Pg.164]

The concepts in Chapters 2 and 3 are used in Chapter 4 to discuss the corrosion of so-called active metals. Chapter 5 continues with application to active/passive type alloys. Initial emphasis in Chapter 4 is placed on how the coupling of cathodic and anodic reactions establishes a mixed electrode or surface of corrosion cells. Emphasis is placed on how the corrosion rate is established by the kinetic parameters associated with both the anodic and cathodic reactions and by the physical variables such as anode/cathode area ratios, surface films, and fluid velocity. Polarization curves are used extensively to show how these variables determine the corrosion current density and corrosion potential and, conversely, to show how electrochemical measurements can provide information on the nature of a given corroding system. Polarization curves are also used to illustrate how corrosion rates are influenced by inhibitors, galvanic coupling, and external currents. [Pg.492]

Ohmic potential drops also play a role in galvanic corrosion and other forms of localized corrosion, in which the anodes and cathodes are spatially separated. Ionic current must then flow some distance through the electrolyte. Two galvanically coupled electrodes will not reach the exact same potential as a result of the ohmic potential drop that will occur along the current path through the electrolyte. [Pg.44]

Galvanized steel is a common example of galvanic coupling where steel (Fe) with a standard electrode potential of—0.440 Vvs. SHE is cathodicaUy protected by a coating of zinc with a more active standard electrode potential of—0.763 V. Obviously, zinc is not a corrosion-resistant metal and cannot be classified as a barrier coating. It protects the steel from corrosion because of its sacrificial properties. Because zinc is less noble than steel, it acts as the anode. The sacrificial anode is continuously consumed by anodic dissolution and protects the more positive metal from corrosion. In practice, sacrificial anodes are... [Pg.10]


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See also in sourсe #XX -- [ Pg.133 , Pg.134 , Pg.135 , Pg.136 , Pg.137 , Pg.138 , Pg.139 , Pg.140 ]




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Electrode couple

Galvanic couple

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