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Salts aqueous corrosion

Greiss, J. C., Crevice Corrosion of Titanium in Aqueous Salt Solutions Corrosion, 24, 96 (1968)... [Pg.482]

Consideration will also be given to attack arising from contact with solids such as refractories, and with molten materials such as salts, glasses, and lower-melting-point metals and alloys. On a fundamental basis, the distinction between some of these latter reactions and normal-temperature aqueous corrosion is not always clear, since galvanic effects may be of significance in both cases, but for practical purposes a distinction can be made on the basis of the temperature involved. [Pg.951]

Aqueous corrosion of tin results in production of oxides of tin. The oxides and hydroxides of tin are stable in the pH range 3-10. The amphoteric nature of the oxides results in attack by mineral acids to produce stannous or stannic salts, stannites and stannates in basic solutions. While borates and bicarbonate render stability to the oxide... [Pg.293]

At higher temperatures and in the presence of salt deposits, the corrosion product may be liquid, in which case the behavior may be more like that of aqueous corrosion. At very high temperatures, the oxide may be volatile, in which case very rapid corrosion can occur. [Pg.550]

The more common classification scheme is to divide the corrosive media into their state of aggregation, that is to subdivide into corrosion by solids, liquids and gases. While solid state corrosion is rarely dealt with, we have vast amount on literature on hot gas corrosion. The case of corrosion by liquids is commonly further subdivided into more specific cases, such as aqueous corrosion (e.g. acids and water), corrosion by glasses, metal melts and salt melts. The last case is for historic reasons known in the form of a rather misleading expression hot corrosion. A special case, which spans from the liquid into the gaseous state is given by the corrosion in hot water systems hydrothermal corrosion. [Pg.143]

Austenitic stainless steels appear to have significantly greater potential for aqueous corrosion resistance than their ferritic counterparts. This is because the three most commonly used austenite stabilizers, Ni, Mn, andN, all contribute to passivity. As in the case of ferritic stainless steel. Mo, one of the most potent alloying additions for improving corrosion resistance, can also be added to austenitic stainless steels in order to improve the stability of the passive film, especially in the presence of Cl ions. The passive film formed on austenitic stainless steels is often reported to be duplex, consisting of an inner barrier oxide film and outer deposit hydroxide or salt film. [Pg.217]

The level of inhibition provided by the R salt in corrosive aqueous environments depends on the type of both anion and cation. Two separate studies by the author and Baldwin et al. (1987) have shown that many of the R chloride salts are good inhibitors i.e. inhibitor efficiencies >75%, though some are better than others (table 2). The reasons for these differences have not been explained. Hinton and Amott (1989) and Amott et al. (1989) have shown that the films which form on the surfaces and which are believed to be associated with the inhibition have very different morphologies and compositions (see sect. 2.5 below). The differences in corrosion inhibition performance may well be associated with these different compositions, structures and the nature of any defects in these films. [Pg.37]

Corrosion inhibitors are substances which slow down or prevent corrosion when added to an environment in which a metal usually corrodes. Corrosion inhibitors are usually added to a system in small amounts either continuously or intermittently. The effectiveness of corrosion inhibitors is partiy dependent on the metals or alloys to be protected as well as the severity of the environment. For example, the main factors which must be considered before apphcation of a corrosion inhibitor to an aqueous system are the compatibility of the inhibitor and the metal(s), the salt concentration, the pH, the dissolved oxygen concentration, and the concentration of interfering species such as chlorides or metal cations. In addition, many inhibitors, most notably chromates, are toxic and environmental regulations limit use. Attention is now being given to the development of more environmentally compatible inhibitors (37). [Pg.282]

Miscellaneous Derivatives. Fimehc acid is used as an intermediate in some pharmaceuticals and in aroma chemicals ethylene brassylate is a synthetic musk (114). Salts of the diacids have shown utUity as surfactants and as corrosion inhibitors. The alkaline, ammonium, or organoamine salts of glutaric acid (115) or C-5—C-16 diacids (116) are useflil as noncorrosive components for antifreeze formulations, as are methylene azelaic acid and its alkah metal salt (117). Salts derived from C-21 diacids are used primarily as surfactants and find apphcation in detergents, fabric softeners, metal working fluids, and lubricants (118). The salts of the unsaturated C-20 diacid also exhibit anticorrosion properties, and the sodium salts of the branched C-20 diacids have the abUity to complex heavy metals from dilute aqueous solutions (88). [Pg.64]

Fig. 4-1 Electrochemical partial and subsequent reactions in corrosion in aqueous media with and without dissolved salt. Fig. 4-1 Electrochemical partial and subsequent reactions in corrosion in aqueous media with and without dissolved salt.
The corrosion resistance of low-alloy steels is not significantly better than that of mild steel for aqueous solutions of acids, salts, etc. The addition of 0.5% copper forms a rust-colored film preventing further steel deterioration small amounts of chromium (1%) and nickel (0.5%) increase the rust... [Pg.64]

A summary of typical experimental conditions used with TSK-PW columns for nonionic polymers is described in Table 20.3. A common mobile phase is an aqueous solution of 0.05 N sodium nitrate. A salt solution of sodium nitrate is a good choice because it is not as corrosive as a solution of sodium chloride. For the descriptions and examples that follow, a bank of either five or six TSK-PW columns in series (G1000-G5000 or G1000-G6000) was used for the aqueous SEC work. These configurations allow for molecular mass characterization from less than 1,000 Da to 1,000,000 Da or greater. [Pg.562]


See other pages where Salts aqueous corrosion is mentioned: [Pg.896]    [Pg.337]    [Pg.276]    [Pg.109]    [Pg.337]    [Pg.221]    [Pg.244]    [Pg.613]    [Pg.642]    [Pg.2249]    [Pg.263]    [Pg.106]    [Pg.148]    [Pg.461]    [Pg.526]    [Pg.611]    [Pg.696]    [Pg.35]    [Pg.70]    [Pg.440]    [Pg.334]    [Pg.163]    [Pg.10]    [Pg.249]    [Pg.255]    [Pg.257]    [Pg.102]    [Pg.188]    [Pg.190]    [Pg.90]    [Pg.369]    [Pg.24]    [Pg.467]   
See also in sourсe #XX -- [ Pg.39 ]




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