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corrosion of stainless steel - Damstahl

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Chapter 6 - Corrosion <strong>of</strong> Stainless Steel<br />

6.1.2 Environmental Factors in Acids<br />

The risk <strong>of</strong> general <strong>corrosion</strong> <strong>of</strong> <strong>stainless</strong> <strong>steel</strong>s exposed to acids normally<br />

depends on:<br />

The acid type and concentration (acidity, pH)<br />

The acid's oxidation capacity<br />

Temperature<br />

Type and concentration <strong>of</strong> impurities<br />

Most <strong>of</strong>ten: The<br />

higher the acid<br />

concentration, the<br />

worse the <strong>corrosion</strong><br />

Oxidising and<br />

non-oxidising<br />

acids<br />

The acid's concentration is not as unequivocal as might be expected. For<br />

most types <strong>of</strong> acid, higher concentrations generally mean greater weight loss<br />

<strong>of</strong> the <strong>steel</strong>. However, at extremely high acid concentrations - e.g. > 90% <strong>of</strong><br />

sulphuric acid (H 2<br />

SO 4<br />

) - the lack <strong>of</strong> water actually results in the acid failing<br />

to function properly as an acid, which is to say that water is thus the limiting<br />

factor. This is only the case, however, with sulphuric acid; for almost all other<br />

acids, the following general rule applies: The higher the concentration, the<br />

worse the <strong>corrosion</strong>.<br />

For all non-passivating alloys, it generally follows that the more active the<br />

cathode reaction (see Chapter 5), the worse the <strong>corrosion</strong>, though this is<br />

not necessarily the case with passive alloys. The formation <strong>of</strong> passivating<br />

chromium oxides requires a certain oxidising effect, and, up to a certain<br />

limit, <strong>stainless</strong> <strong>steel</strong> thus performs better in oxidising acids than in nonoxidising<br />

acids.<br />

This effect is illustrated in Figure 5.8 on page 64, where the strong, nonoxidising<br />

acids (sulphuric acid, phosphoric acid, etc.) will typically make<br />

the <strong>steel</strong> fall into the yellow ”active area” with resulting high <strong>corrosion</strong><br />

rates. An oxidising acid, on the other hand, such as a pure nitric acid or<br />

peracetic acid will make the <strong>steel</strong> jump up into the green ”passive area”<br />

where the <strong>corrosion</strong> rate is far lower despite the higher potential (and thereby<br />

theoretically greater driving force). The <strong>corrosion</strong> rate is not only governed<br />

by energy, but just as much by kinetics.<br />

This effect is clearly seen with <strong>stainless</strong> <strong>steel</strong> in sulphuric acid (see<br />

Figure 6.3) where even small amounts <strong>of</strong> the highly oxidising chromic acid,<br />

CrO 3<br />

, has a strong inhibiting effect on the <strong>corrosion</strong> <strong>of</strong> 4307 <strong>steel</strong>. This is<br />

seen by the curve's high location in relation to the pure sulphuric acid. If the<br />

concentration <strong>of</strong> CrO 3<br />

is increased beyond the indicated 0.2-0.5%, the curve<br />

will fall again as a sign <strong>of</strong> ”overdosing”. Other oxidants such as hydrogen<br />

peroxide (H 2<br />

O 2<br />

) has the same beneficial effect and can therefore be used as<br />

a <strong>corrosion</strong> inhibitor in sulphuric acid. Perioxide-inhibited sulphuric acid<br />

is <strong>of</strong>ten used as a substitute for nitric acid in applications where remains<br />

<strong>of</strong> nitrates (NO 3–<br />

) for various reasons are unwelcome, e.g. in the cleaning<br />

<strong>of</strong> milk tanks.<br />

77<br />

RS for alle.indb 77<br />

9/29/2011 12:44:33 PM

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