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Corroded metal surface

As a result of the concentration of acidic species, such as chloride and sulfate, material scraped from the inside of tubercles is virtually always acidic when mixed with water. Acidity varies not only from tubercle to tubercle but also from place to place in a given tubercle. Acidity is greatest near the corroded metal surface. The size of the fluid-filled cavity can indicate acidity. The larger the cavity, the more acidic the internal environment. [Pg.52]

It is interesting to see that bismuth ions, Bi3+ or BiO+, inhibit the corrosion of metallic iron, zinc, and cobalt in perchloric acid solution. The bismuth ions are reduced in the cathodic reaction of metal corrosion forming metallic precipitates of bismuth on the corroding metal surface. [Pg.581]

For example, a partially corroded metal surface from which particles of corroded metal can become detached. [Pg.13]

Y.S. Yan, D.E. Beving, High aluminum coatings on corrodible metal surfaces, US Patent... [Pg.175]

RH, by definition, the equilibrium quantity cannot be so great that the water has bulk properties. (Bulk water would evaporate if the RH is less than 100% ) Water adsorption data on corroding metals surfaces is not available. Water adsorption comprises the subject of the second section of this paper. [Pg.243]

In a similar way, the concentration of aggressive anions, such as chloride, sulfate, or nitrate, affects the adsorption or film-forming properties of the inhibitor. It is emphasized that the pH as well as inhibitor and anion concentrations at the corroding metal surface rather than in the bulk of the solution are relevant for the inhibition efficiency, which is especially important in the case of localized corrosion. For example, a linear... [Pg.441]

In most cases, inhibition relies on the interaction of inhibiting species with the corroding metal surface, of which adsorption is the first and often decisive step. A detailed treatment of adsorption at electrochemical interfaces and the resulting structure of the electrochemical double layer is given in Chapter 5 of Volume 1. In the following sections, the most important aspects will be briefly reviewed, with particular emphasis on systems relevant for corrosion inhibition. [Pg.442]

The vast majority of corrosion inhibitors in neutral environment as well as a number of acid corrosion inhibitors form protective 3D films on the metal surface ( interphase inhibition [4]). These films may consist of adsorbate multilayers, ox-ide/hydroxides, salts, or reaction products formed by interaction of the inhibitor with solution species on or near the corroding metal surface (e.g. dissolved metal ions). The type, structure, and thickness of the inhibiting films are strongly influenced by the environmental conditions. The interphase films act as a physical barrier that blocks or retards transport processes and the kinetics of the corrosion reactions at the metal surface. The inhibitive properties could, in some cases, be correlated with the chemical stability of the corresponding insoluble complexes as well as with the solubihty, adsorbabOity, and hydrophobicity of the inhibitor molecules [35]. Often, other ions from the electrolyte, such as... [Pg.450]

Sulfuric acid is especially likely to corrode metal surfaces at high velocity. Carbon steel piping systems are usually designed for maximum velocities of about 1 ms . When more resistant alloys are used (e.g.. Alloy 20), velocities can be increased to about 2ms . ... [Pg.803]

There are four environmental requirements that must be met for an electrochemical corrosion process to proceed an electron path, an ion path, a cathode, and an anode [2]. The electron path can be as obvious as an external circuit cormection between the anode and the cathode in an experimental setup or more subtly the transport of free electrons from an anodic to a cathodic site on a corroding metal surface. The ionic path refers to the medium that transports cations away from the anodic site and anionic or other reactive species transport to cathodic reaction sites. The cathode can be a separate material or a temporary reaction site on the corroding metal where a reduction reaction—such as the oxygen reduction reaction or hydrogen evolution reaction—occurs. [Pg.99]

Without losing sight of filtration requirements, the media manufacturer must also take account of the physical forces that will be imposed on the fabric by the equipment itself in particular, the effect that these forces will have on the fabric s resistance to stretch, its resistance to flexing, or its abrasion resistance, the last in this instance is through contact with rough, possibly corroded metal surfaces. In some cases, special reinforcement patches have to be stitched to the cloth during fabrication to avert potential abrasion damage inflicted by the filter. [Pg.247]

Solid state voltammetric microelectrodes with tip diameters in the range of 10-50 microns are especially useful for measuring chemical profiles within thin biofilms on corroding metal surfaces. Lewandowski and coworkers have used iridium-iridium oxide microelectrodes for measuring... [Pg.515]

Test for Chloride (Bromide) on a Corroded Metal Surface ... [Pg.547]

The mechanism of corrosion involves metal dissolution due to an electrochemical phenomenon. Thus, corrosion is associated with current flow over finite distances from the corroding metal and the amount of corrosion that can be accounted for is quantitatively determined by the amount of current passing through the metal. The electrochemical phenomenon occurs because of differences in potential between areas of the corroding metal surface. Therefore, the driving force of corrosion is the decrease in free energy associated with the formation of corrosion product on the metal surface, hi contrast, preventing corrosion leads to cathodic protection under steady-state conditions. [Pg.247]


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See also in sourсe #XX -- [ Pg.547 ]




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Corroding metals

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