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Electrochemical corrosion redox reaction

Ox and Red are general symbols for oxidation and reduction media respectively, and n and (n-z) indicate their numerical charge (see Section 2.2.2). Where there is no electrochemical redox reaction [Eq. (2-9)], the corrosion rate according to Eq. (2-4) is zero because of Eq. (2-8). This is roughly the case with passive metals whose surface films are electrical insulators (e.g., A1 and Ti). Equation (2-8) does not take into account the possibility of electrons being diverted through a conductor. In this case the equilibrium... [Pg.33]

Electrochemical corrosion of metals Since the aggressiveness of salt melts is governed by redox equilibria, and is often controlled by composition of the external atmosphere, effects analogous to electrochemical or oxygen-concentration corrosion in aqueous systems can occur in salt melts. Tomashov and Tugarinov determined cathodic polarisation curves in fused chlorides and concluded that the cathodic reactions of impurities could be represented as ... [Pg.439]

In normal battery operation several electrochemical reactions occur on the nickel hydroxide electrode. These are the redox reactions of the active material, oxygen evolution, and in the case of nickel-hydrogen and nickel-metal hydride batteries, hydrogen oxidation. In addition there are parasitic reactions such as the corrosion of nickel current collector materials and the oxidation of organic materials from separators. The initial reaction in the corrosion process is the conversion of Ni to Ni(OH)2. [Pg.145]

Oxidation—reduction reactions, commonly called redox reactions, are an extremely important category of reaction. Redox reactions include combustion, corrosion, respiration, photosynthesis, and the reactions involved in electrochemical cells (batteries). The driving force involved in redox reactions is the exchange of electrons from a more active species to a less active one. You can predict the relative activities from a table of activities or a halfreaction table. Chapter 16 goes into depth about electrochemistry and redox reactions. [Pg.71]

It differs, thereby, from simple redox reactions such as Fe3+ + e Fe2+. Such reactions do not involve an intermediate radical and lack consecutive steps and alternative pathways. Study of their kinetics, therefore, omits characteristics of most electrochemical reactions met, e.g., in electrochemical synthesis, energy conversion and storage, or corrosion. [Pg.481]

Because corrosion is electrochemical, we can use our knowledge of redox reactions to combat it. The simplest way to prevent corrosion is to protect the surface of the metal from exposure to air and water by painting. A method that achieves greater protection is to galvanize the metal, which involves coating it with an unbroken film of zinc (Fig. 12.16). Zinc lies below iron in the electrochemical series, so if a scratch exposes the metal beneath, the more strongly reducing zinc releases electrons to the iron. As a result, the zinc, not the iron, is oxidized. The zinc itself survives exposure on the unbroken surface because, like aluminum, it is passivated by a protective oxide. [Pg.728]

In this chapter we will examine oxidation-reduction stoichiometry, equilibria, and the graphical representation of simple and complex equilibria, and the rate of oxidation-reduction reactions. The applications of redox reactions to natural waters will be presented in the context of a discussion of iron chemistry the subject of corrosion will provide a vehicle for a discussion of the application of electrochemical processes a presentation of chlorine chemistry will include a discussion of the kinetics of redox reactions and the reactions of chlorine with organic matter finally, the application of redox reactions to various measurement methods will be discussed using electrochemical instruments as examples. [Pg.316]

Corrosion is an electrochemical process. Therefore, some understanding of the fundamentals of electrochemistry is necessary [11-13]. Electrochemistry is the study of reactions that occur at the interface of an electrode, which is a metallic or semiconducting solid or liquid, and an electrolyte, which is a liquid or solid ionic conductor. These reactions typically involve the transfer of charge across the interface. There are two types of charge transfer reactions. Ion transfer reactions involve the transfer of ions from the electrode to the electrolyte, or vice versa. Electron transfer reactions involve the transfer of charge between ions in the electrolyte (or adsorbed on the surface), and typically occur heterogeneously at an electrode surface. Redox reactions are pure electron transfer reactions that occur at inert electrode surfaces. A more detailed discussion of electrochemical concepts can be found in the other volumes of this encyclopedia. A simplified view of certain aspects relevant to corrosion will be presented in this section. [Pg.5]

Upon polarization of either electrode, the cell potential moves along the oxidation and reduction curves as shown in Fig. 1.1. When the current through the cell is f, the potential of the copper and zinc electrodes is Cj cu and e zn > and each of the electrodes have been polarized by (Ceq.cu i.Cu) and (Ceq.zn i,z )- Upon further polarization, the anodic and cathodic curves intersect at a point where the external current is maximized. The measured output potential in a corroding system, often termed the mixed potential or the corrosion potential (Tcorr)> h the potential at the intersection of the anodic and the cathodic polarization curves. The value of the current at the corrosion potential is termed the corrosion current (Icon) and can be used to calculate corrosion rate. The corrosion current and the corrosion potential can be estimated from the kinetics of the individual redox reactions such as standard electrode potentials and exchange current densities for a specific system. Electrochemical kinetics of corrosion and solved case studies are discussed in Chapter 3. [Pg.5]

Current flows through the corrosion system (electrochemical cell) only when the redox reaction is not at equihbrium. The difference between the operating electrode potential, E, and the equihbrium potential, e q, is defined as the electrode polarization, AE. Thus, the electrode polarization is a deviation from the equihbrium potential in the presence of current. When a cathodic current is imposed, the potential is displaced to the negative side, causing cathodic polarization to be negative. When an anodic current is apphed, polarization is positive. The electrode polarization and defined nature of the hmiting step is called electrode overpotential or overvoltage. [Pg.99]

According to mixed potential theory, any electrochemical reaction consists of partial reduction and oxidation reactions. In any redox reaction, such as the corrosion of a metal, there is no net accumulation of electric chaise and the rate of the oxidation must equal the rate of reduction. At the intersection of the cathodic and anodic kinetic lines (see Fig. 3.8), the rates of oxidation and reductions are equal. This point represents the corrosion potential, Eco .> and the corrosion current, At the... [Pg.120]

In the active region, the anodic electrochemical reaction is the metal oxidation. In this region, the corrosion potential and corrosion current are defined by Tafel kinetics of individual redox reactions. The corrosion rate, 4oir. md the corrosion potential, corr>... [Pg.144]

SECTION 20.8 Electrochemical principles help us understand corrosion, undesirable redox reactions in which a metal is attacked by some substance in its environment The corrosion of iron into rust is caused by the presence of water and oxygen, and it is accelerated by the presence of electrolytes, such as road salt. The protection of a metal by putting it in contact with another metal that more readily undergoes oxidation is called cathodic protection. Galvanized iron, for example, is coated with a thin layer of zinc because zinc is oxidized more readily than iron, the zinc serves as a sacrificial anode in the redox reaction. [Pg.864]

A plumber s handbook states that you should not connect a brass pipe directly to a galvanized steel pipe because electrochemical reactions between the two metals will cause corrosion. The handbook recommends you use instead an insulating fitting to connect them. Brass is a mixture of copper and zinc. What spontaneous redox reaction(s) might cause the corrosion Justify your answer with standard emf calculations. [Pg.871]

Figure 10 signifies the electrochemical analysis (Tafel plot) of MS panels coated with neat alkyd resin, and coated with 2 and 4 wt % loading of ZMP nanocontainer incorporated in alkyd resin. Above analysis was carried out in 5 wt % aqueous NaCl solution at room temperature. The Tafel plot is plotted as log (current density) as a function of applied potential. In Tafel plot analysis current density is measured in corrosion process for simultaneous redox reactions occurs at the surface of cathode and anode of MS plate. Icorr i.e. corrosion current density and Ecorr i.e. corrosion potential, values were found from the Tafel plot analysis. It is observed that corrosion current... [Pg.394]

Abstract Since the corrosion phenomenon is basically an electrochemical redox reaction, it can be evaluated and analyzed by many electrochemical methods as well as non-electrochemical traditional ones. In this chapter, we describe some representative evaluation methods for corrosion from practical methods to scientific ones using electrochemical methods. [Pg.23]

F is the Faraday constant, and n is the number of electrons transferred in the redox reaction. F, named after Michael Faraday, has a value of 96,485 J mol or 96,485 C moLh (Remember that 1 J = 1 C V.) Equation 13.3 bears a resemblance to Equation 12.7, which we used to derive the relationship between AG° and the equilibrium constant. We can apply the Nernst equation to estimate the potential of the electrochemical system in the corrosion of steel at more realistic concentrations. Example Problem 13.2 explores the use of the Nernst equation in an electrochemical cell that models corrosion. [Pg.545]


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