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Common Types of Metal Corrosion <br />Passive Alloys and Chloride Induced Stress Corrosion <br />To avoid galvanic corrosion to steel, it is common <br />practice to employ stainless steel or other passive alloys. <br />Stainless steel contains at least 10.5% chromium, which <br />passivates the surface with a very thin chrome -oxide <br />film. This, in turn, serves to protect against acids and <br />other inducers of galvanic corrosion. <br />The most practical limitations occur in environments <br />where this chrome -oxide film can be broken down. Very <br />typically this occurs in the presence of the chloride ion, <br />particularly in the vicinity of areas such as welds, where <br />tensile stress is present. Although the mechanism <br />can be complex, the corrosion is accompanied by <br />a distinctive destruction of grain boundaries, which <br />characterize the morphology or metallurgical structure <br />of the stainless steel. This is ordinarily manifested as <br />pitting, crevice corrosion, or corrosion stress -cracking, <br />which may proceed rapidly once initiated. Chlorides can <br />often be present at exceptionally high levels, especially <br />in applications such as flue desulfurization, where there <br />is a net evaporation of water as well as leaching of <br />coal ash. Thus, even though stainless steel will display <br />quite good acid resistance, the corrosion can be severe <br />due to chlorides. Chlorides tend to be quite prevalent <br />in industrial environments, even in places where they <br />might not be obvious, so it is always important to be <br />wary in the use of stainless steels. Another corrosive <br />limitation to stainless steel relates to oxygen depletion. <br />Since the passivity of stainless steel depends on a thin <br />protective chrome oxide film, it is important to keep the <br />surface in an oxidized state. The passive film may no <br />longer be preserved in certain reducing environments, <br />or where the surface is insulated from oxygen by scale <br />or other strongly adhering deposits. <br />The class of stainless steel most commonly considered <br />in corrosive environments is known as austenite, <br />but the other types (martensetic and ferritic) are also <br />common. Over the years, many grades have been <br />developed to improve resistance to chloride and to <br />afford better strength, heat resistance, and welding <br />properties to minimize the effects of stress induced <br />corrosion. Characteristically, increased nickel content <br />alloys are favored for high chloride applications, such <br />as type 317L stainless steel, HastelloyTm, Inconel, or <br />the various Haynes series alloys, such as C-276. Since <br />these alloys are expensive, applications often involve <br />cladding or thin "wallpapering" procedures. The use of <br />these selections involves a great deal of welding, which <br />must be done with a high degree of expertise, expense, <br />and high level inspections with attention to detail, since <br />welds are especially susceptible to stress corrosion. <br />Sulfide Stress Cracking <br />Somewhat akin to chloride -induced stress corrosion <br />is sulfide stress corrosion cracking. This is common <br />in oilfield and other applications, such as geothermal <br />energy recovery and waste treatment. Carbon steel as <br />well as otheralloys can reactwith hydrogen sulfide (1-12S), <br />which is prevalent in sour oil, gas, and gas condensate <br />deposits. Reaction products include sulfides and atomic <br />hydrogen which forms by a cathodic reaction and <br />diffuses into the metal matrix. The hydrogen can also <br />react with carbon in the steel to form methane, which <br />leads to embrittlement and cracking of the metal. <br />CO2 Corrosion <br />Carbon dioxide can be quite corrosive to steel (at times <br />in excess of thousands of mils per year) due to the <br />formation of weak carbonic acid as well as cathodic <br />depolarization. This type of corrosion is especially <br />devastating in oil and gas production and is apt to receive <br />even more attention in the future due to increased <br />use of CO2 for enhanced oil recovery. Additionally, <br />various underground sequestering processes are being <br />inspired by concerns over global warming. Turbulence, <br />or gas velocity, can be a big factor in the CO2 induced <br />corrosion of steel due to the formation and/ or removal <br />of protective ion carbonate scale. On the other hand, <br />FRP is not affected by these mechanisms of corrosion. <br />Other Types of Stress Corrosion <br />Sometimes internal stress corrosion -cracking of steels <br />may occur unexpectedly due to mechanisms which <br />are not yet completely understood. For example, there <br />is some evidence this occurs with ethanol in high <br />concentrations, especially around welds. Likewise, <br />anhydrous methanol can be corrosive to aluminum as <br />well as titanium. <br />