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Oxidation corrosion rates, yearly

As indicated above, the bicarbonate ion inhibits the process, which does not occur, therefore, in many supply waters attack is most likely in waters which by nature or as a result of treatment have a low bicarbonate content and relatively high chloride, sulphate or nitrate content. The number of points of attack increases with the concentration of aggressive anions and ultimately slow general corrosion may occur. During exposure of 99-75% tin to sea-water for 4 years, a corrosion rate of 0-0023 mm/y was observed . Corrosion in soil usually produces slow general corrosion with the production of crusts of oxides and basic salts this has no industrial importance but is occasionally of interest in archaeological work. [Pg.805]

C) for cast iron and up to 140 °F for marstenitic SS (60 °C). It is widely used where silicates are present with the iron oxides. Typically, 5 to 7.5% HC1 is employed. The ammonium bifluoride normally is present at 0.5%, but it may be increased to a maximum of 1.5% for a boiler that has not been cleaned for many years. The presence of hydrofluoric acid (HF), which is formed by the reaction of ammonium bifluoride with HC1 (see equation), tends to increase the rate of iron oxide dissolution and reduce the corrosion rate of exposed steel, when compared to using HC1 alone. This is due to the stability of the hexafluoroferric ion (FeFg3 ), which prevents the ferric ion from corroding exposed steel. [Pg.639]

It has long been recognized that local environmental characteristics influence the rates of material corrosion. After two years of measurements at 39 sites in Europe and North America, significant relationships have been shown between corrosion rates of building materials and atmospheric pollutants( 5). While direction of exposure relative to weather and other factors such as frequency and duration of wetting significantly influence corrosion, Kucera (46) has shown that sulphur oxides are strongly correlated with deterioration of structural materials. [Pg.57]

The oxidation which occurs in the hot environment rapidly reduces the thickness of the metal components and leads to component failure. Corrosion rates as high as 0.1 to 0.2 inches/year have been demonstrated at 1,300°F (704.4°C) operating temperatures. [Pg.69]

While thick film passivity has been documented and understood for many years, the difficulties in studying thin film passivity were daunting. It took many years to determine that indeed a film was responsible for the effect, as these films are so thin that they are invisible to the eye (i.e., transparent to radiation in the visible region). Two main types of theories were developed in order to explain the phenomena observed theories based upon the idea of adsorption reducing the corrosion rate, and theories based upon the formation of a new phase, an oxide of the base metal, on the surface. In all cases, an increased barrier to dissolution results upon the increase in potential. This increased kinetic barrier upon anodic polarization contrasts with the exponentially decreased barrier which develops during anodic polarization of an active material. [Pg.60]

Corrosion of the glass-making melters must be maintained at an absolute minimum to increase the lifespan of the melter. Laboratory-measured corrosion rates indicate that melter lifetimes of several years can be achieved with high chrome oxide or zircon refractories metallic melters may have lifetimes of several months if alloys such as Inconel 690 are used. These conclusions have been reached on the basis of extrapolation of laboratory tests. Long-term tests, particularly with waste glasses in engineering-scale continuous melters, have not yet been made. [Pg.99]

The success of the Type 300 series stainless steel in molten carbonates is a result of the protective LiCr02 film which forms a compact, tenacious, and self-healing layer. This film forms in about 500 hrs and decreases the corrosion rate to a few mils per year. It has been shown that this film is essentially chromium oxide, with the vacant interstices filled with lithium. Lithium is the only stable ionic species present in the melt which is capable of filling the vacant interstice without expanding the oxide lattice (5). Thus a stable diflFusion barrier is formed which limits further corrosion. [Pg.180]

It is a well known fact that formation of the green patina takes a substantially shorter time in urban than in rural atmosphere, where often very long time elapses before the surface is covered by patina or in very pure atmospheres the surface remains covered by a black oxide layer. Also the corrosion rate in rural atmosphere is usually lower (<1 um/year) than in urban or industrial atmospheres (1-3 /Lim/year) (8 . [Pg.108]

The RH in most indoor environments is usually not above 70 percent and, thus, the CRH of most common metals is seldom exceeded. The time-of-wetness will be quite small. The corrosion rate is likely to be comparable to the outdoor rate (at similar contaminant levels) when the surfaces are dry. Such rates are insignificant compared to the wet rates for most metals (18). In many cases, the anions associated with deposited substances may play the dominant role in surface processes (24). The concentrations of sulfate, nitrate, and chloride, which accumulate on these surfaces, are likely to increase continuously. After 10 years exposure, total anion concentrations of five to ten /ng/cm can be expected in urban environments. These anions, especially chloride, are well known to dramatically affect the corrosion rates of many metals in aqueous solutions. This acceleration is often a result of solubilization of the surface metal oxide through complexation of the metal by the anions. Chloride, in particular, can dramatically lower the RH above which a moisture film is present on the surface, since chloride salts often have low CRHs (e.g., zinc chloride - < 10 percent calcium chloride - 30 percent and aluminum chloride - 40 percent). The combination of the low CRHs of chloride salts and the well documented ability of dissolved chloride to break down metal oxide passivation set chloride apart from the other common anions in ability to corrode indoor metal surfaces. Some nitrate salts also have moderately low CRHs (e.g., zinc nitrate -38 percent calcium nitrate - 49 percent aluminum nitrate - 60 percent). [Pg.222]

The sequence of reactions involved in the overall reduction of nitric acid is complex, but direct measurements confirm that the acid has a high oxidation/reduction potential, -940 mV (SHE), a high exchange current density, and a high limiting diffusion current density (Ref 38). The cathodic polarization curves for dilute and concentrated nitric acid in Fig. 5.42 show these thermodynamic and kinetic properties. Their position relative to the anodic curves indicate that all four metals should be passivated by concentrated nitric acid, and this is observed. In fact, iron appears almost inert in concentrated nitric acid with a corrosion rate of about 25 pm/year (1 mpy) (Ref 8). Slight dilution causes a violent iron reaction with corrosion rates >25 x 1()6 pm/year (106 mpy). Nickel also corrodes rapidly in the dilute acid. In contrast, both chromium and titanium are easily passivated in dilute nitric acid and corrode with low corrosion rates. [Pg.224]

Laboratory oxidation-corrosion data indicate that extrapolation of short-term oxidation-corrosion data to yearly rates is difficult. These extrapolations are necessary to provide a basis for comparing oxidation-corrosion data obtained from variable CGA exposure times. Extrapolated data, particularly at high H2S concentrations in the CGA atmosphere, should be employed with caution. Long-term kinetics of the oxidation-corrosion process can result in transitions in corrosion behavior to high rates not predictable by short exposures. Similar behavior, breakaway oxidation, occurs in air primarily at temperatures above 2000 F. [Pg.412]

Copper and copper alloys are highly resistant to atmospheric corrosion because of surface films mainly composed of basic copper salts. The corrosion rate is below 2-3 pm/year [8.9]. Tin as well as nickel and nickel alloys also corrode at similar rates. Lead possesses excellent corrosion resistance in atmospheres due to surface-protecting films (insoluble sulphate, sulphide, carbonate and oxide). [Pg.197]

Figures 29 and 30 show the peak generated as the containers on the pontoon are finally breached in the year 2305. Five hundred GBq of fission products and 1600 GBq of actinides are immediately released to the Kara Sea from the cracks and porosity of the damaged fuel. In the following year, the rate of release reverts to the calculated corrosion rate of the oxide fuel fission product and actinide release rates are 1.7 GBq-a and 5.7 GBq a -, respectively. The fuel slowly corrodes away and the activity of the fuel itself decreases in the year 3300, the release rates for fission products and actinides are 0.05 GBq-a and 2.7 GBq a, respectively. The fuel is finally corroded away by the year 4570. Figures 29 and 30 show the peak generated as the containers on the pontoon are finally breached in the year 2305. Five hundred GBq of fission products and 1600 GBq of actinides are immediately released to the Kara Sea from the cracks and porosity of the damaged fuel. In the following year, the rate of release reverts to the calculated corrosion rate of the oxide fuel fission product and actinide release rates are 1.7 GBq-a and 5.7 GBq a -, respectively. The fuel slowly corrodes away and the activity of the fuel itself decreases in the year 3300, the release rates for fission products and actinides are 0.05 GBq-a and 2.7 GBq a, respectively. The fuel is finally corroded away by the year 4570.
Field exposure test is a very slow oxidation process whereas the accelerated laboratory test is a very fast oxidation process. Several months/years together are required to get measurable mst on surface of steel panels in field exposure. In accelerated laboratory test rate of oxidation is much faster and rust layers/oxides are formed, very quickly. The rust products/oxides formed in both the cases are identical but their manifestations are different. As a result corresponding morphologies and corrosion rates are vastly different. [Pg.188]

A number of coolant gases can be used in direct contact with BeO at high temperatures in gas-cooled reactors using BeO as a moderator. Problems of erosion or volatility of BeO in such gases as He, CO2, or N2 are not significant if the water-vapor content of the coolant is sufficiently low. Corrosion of BeO by water vapor is not a serious problem below 850°C. At 1000°C and a Reynolds number of 10, a corrosion rate of only about 2.5 ju/year is reported in 30 atm CO2 with 330 ppm of water vapor (2i). Beryllium oxide is reported not to react with pure CO2, O2, or N2, and obviously helium, at temperatures in excess of 1200°C. [Pg.12]

Atmospheres change considerably with time, however, as is shown in Fig. 2.4 for the first 80 years of this century. Environmental controls now ensure lower sulfur oxides. Present levels in Europe are half those of the peak period and zinc corrosion is substantially reduced. Recent data, notably from the ISOCORRAG tests (Table 2.7B, Knotkova, 1993), indicate that current corrosion rates in Europe are much less than the rates given in Tables 2.3-2.6, which reflect the high acidic pollution of 30 years ago. Knotkova and Porter (1994) have documented this in detail and show that zinc coatings now last 30-50% longer. [Pg.107]

Zirconium has corrosion rates of less than 0.127 mm/year. Zirconium is totally immune to attack by hydrochloric acid at all concentrations and at temperatures well above boiling. Aeration has no effect, but oxidizing agents such as cupric or ferric ions may cause pitting. Zirconium also has excellent corrosion resistance to hydrobromic and hydroiodic acid. [Pg.333]

The duration of the test can have a significant effect on the test data. Most materials wiU corrode most rapidly in the early stages of exposure to an enviromnent—before oxide films are developed that may inhibit the corrosion rate by limiting the diffusion rate of reacting species to and from the metallic surface. Thus, tests of 24-h duration extrapolated to 30-day or f-year behavior may be extremely conservative. Where time allows, multiple test durations may be evaluated to determine the actual effect of exposure time on uniform corrosion. [Pg.207]

Analysis of the results after 1 and 2 years exposure indicates that the influence of SO2 on the corrosion rate of carbon steel, weathering steel, zinc, bronze, sandstone, limestone, and nickel is significant. Conversely, no influence of NO2 has so far been observed in any of the materials studied. This discrepancy between the laboratory exposures and the field tests must be investigated. Perhaps as a result of catalysts or oxidizers in field exposures, which aid in promoting the oxidation of S(IV) to S(VI), the effect of NO2 was hidden. [Pg.245]


See other pages where Oxidation corrosion rates, yearly is mentioned: [Pg.401]    [Pg.229]    [Pg.993]    [Pg.478]    [Pg.71]    [Pg.143]    [Pg.221]    [Pg.1808]    [Pg.192]    [Pg.314]    [Pg.315]    [Pg.212]    [Pg.428]    [Pg.540]    [Pg.541]    [Pg.76]    [Pg.217]    [Pg.507]    [Pg.369]    [Pg.3]    [Pg.187]    [Pg.116]    [Pg.228]    [Pg.360]    [Pg.196]    [Pg.316]    [Pg.327]    [Pg.569]    [Pg.109]    [Pg.1026]   
See also in sourсe #XX -- [ Pg.401 ]




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Oxides Corrosion

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