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Electrochemical cells corrosion

In order to avoid surface contamination upon removal of samples from the electrochemical corrosion cell, samples were transferred from the solution to the vacuum entry system in an inert gas chamber. Previous work had shown a tendency of the X-ray beam to slowly reduce U + states on UC>2. McIntyre et al, therefore, checked for such a decomposition and found none within the first 30 minutes of exposure to X-rays. [Pg.266]

Figure 2 Cu Polish rate as a function of glycine concentration Figure 4 shows the copper dissolution rate as a function of H2O2 concentration in the presence of 1 wt % glycine. The variation in the open-circuit potential (OCP) measured with respect to SCE at KXK) rpm rotational speed, as measured in an ex situ electrochemical corrosion cell, is also plotted as a function of H2O2 concentration. The copper dissolution rate decreases with increasing peroxide concentration, which is contrary to the expectation. If copper... Figure 2 Cu Polish rate as a function of glycine concentration Figure 4 shows the copper dissolution rate as a function of H2O2 concentration in the presence of 1 wt % glycine. The variation in the open-circuit potential (OCP) measured with respect to SCE at KXK) rpm rotational speed, as measured in an ex situ electrochemical corrosion cell, is also plotted as a function of H2O2 concentration. The copper dissolution rate decreases with increasing peroxide concentration, which is contrary to the expectation. If copper...
The molten condition of the deposit can allow electrochemical corrosion cells to be established. Furthermore, the problem may be accompanied by a lowering of the melting point of the deposit because of the presence of fluxing agents. It is at the anodic area that corrosion occurs ... [Pg.1049]

Figure 16.4 Electrochemical corrosion cell used for testing the ennobling effect of a conducting polymer. The mild steel sample (1) is coated by a thin epoxy layer and is in contact with a 0.1 M UCIO4 solution (aerated or deaerated) through a small hole. Polymethylthiophene (PMT) is deposited on a Pt electrode (2) a saturated calomel electrode (3) and a Pt counter-electrode (4) are used with either (1) or (2) as the working electrode. Electrodes (1) and (2) are galvanically connected and can be disconnected from the electrical circuit for specific measurements. (Reprinted with permission from Electrochimica Acta, Corrosion protection by ultrathin films of conducting polymers by U. Rammelt, P.T. Nguyen and W. Plieth, 48, 9, 1257-1262. Copyright (2003) Elsevier Ltd)... Figure 16.4 Electrochemical corrosion cell used for testing the ennobling effect of a conducting polymer. The mild steel sample (1) is coated by a thin epoxy layer and is in contact with a 0.1 M UCIO4 solution (aerated or deaerated) through a small hole. Polymethylthiophene (PMT) is deposited on a Pt electrode (2) a saturated calomel electrode (3) and a Pt counter-electrode (4) are used with either (1) or (2) as the working electrode. Electrodes (1) and (2) are galvanically connected and can be disconnected from the electrical circuit for specific measurements. (Reprinted with permission from Electrochimica Acta, Corrosion protection by ultrathin films of conducting polymers by U. Rammelt, P.T. Nguyen and W. Plieth, 48, 9, 1257-1262. Copyright (2003) Elsevier Ltd)...
From the cost point of view, precious metals (such as Au and Pt) are surely out of contention for practical coatings on SS substrates, although they might be used for short laboratory tests. In fact, electrochemical corrosion cells will be generated from the possible pinholes in the coatings due to the electrochemical dissimilarity of the precious metals and SSs in a PEMFC environment. Difficulties encountered with the carbon-based and conductive polymer-based coatings are application at intermediate temperatures, the cold-start issue, and the differences in thermal expansion coefficients between the coating itself and the substrate SS. The risk of... [Pg.372]

Mechanical damage to the pipe can result in localized corrosion where the surface is scratched or dented, due to the formation of differential stress electrochemical corrosion cells. Corrosion can also occur if local damage occurs to the protective oxide film on the metal surface, resulting in an electrochemical corrosion cell between the clean metal and corroded metal. In the case of active-passive alloys, such as stainless steel, local damage to the protective oxide layer can result in an electrochemical corrosion cell. [Pg.700]

Corrosion caused by the connection of two or more different metals also occurs underground. This electrochemical corrosion cell is commonly referred to as bimetallic or galvanic corrosion. Typical examples include brass or bronze valves connected to steel or cast iron pipes and stainless steel fasteners coimected to steel or cast iron. These couplings of dissimilar metals will locally affect the corrosion rate. Aluminum can be severely corroded if directly connected to most other engineering alloys, such as steel, iron, copper, or stainless steel—dielectric isolation must be used. [Pg.700]

Stress differences can result in localized electrochemical corrosion cells. An example is bolts used on joint fittings. The head and threaded areas of the bolt corrode at a faster rate than the body that is at a lower stress level. [Pg.700]

The composition and concentration of a test solution often affect the electrolyte conductivity, the effectiveness of an electrochemical corrosion cell, and thus the rate of corrosion. In an accelerated inhibitor test, electrolyte concentrations are frequently chosen to allow a sufficient degree of corrosion in a short period of time and yet still allow discrimination of inhibitors effectiveness. For this reason, Blin et for example, chose a 0.01 M sodium chloride solution as the... [Pg.39]

In civil engineering structures exposed to moisture, electrochemical corrosion can lead to extensive damage on metal members this damage is due to galvanic connections - so-called corrosion cells - that produce local electric currents in the metal. From equilibrium considerations, the risk of formation of electrochemical corrosion cells in a given civil engineering structure can be predicted and in many cases the risk can be limited. On the other hand, one must realize that equilibrium considerations cannot give information of corrosion rate and thus the extent of a foreseeable corrosion attack. The latter subject is addressed separately under Corrosion kinetics . [Pg.197]


See other pages where Electrochemical cells corrosion is mentioned: [Pg.120]    [Pg.478]    [Pg.208]    [Pg.162]    [Pg.151]    [Pg.166]    [Pg.640]    [Pg.490]    [Pg.496]    [Pg.1310]    [Pg.211]    [Pg.391]    [Pg.187]    [Pg.52]    [Pg.340]   
See also in sourсe #XX -- [ Pg.151 ]




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