Page 97 - Pipeline Risk Management Manual Ideas, Techniques, and Resources
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Scoring the corrosion potential 4/75
                This part of the risk assessment will apply to metallic pipe   cell can be established between the two metals. Dissimilar soils
               material that is buried or submerged. If the pipeline being eval-   with differences in concentrations of ions, oxygen, or moisture
               uated is not vulnerable to subsurface corrosion, as would be the   can also set up anodic and cathodic regions on the pipe surface.
               case for a plastic pipeline or a totally aboveground pipeline, the   Corrosion cells ofthis type are called concentration cells. When
               evaluator should use the previous two sections and any other   these cells are established, the  anodic region will  experience
               pertinent factors to assess the corrosion risk.   active corrosion. The severity of this corrosion is dictated by
                 Of the three categories of corrosion, this is usually consid-   variables such as the conductivity of the soil (electrolyte) and the
               ered to be the most complex. Several corrosion  mechanisms   relative electronegativities ofthe anode and cathode.
               can be at work in the case ofburiedmetals. This situation is fur-   Common industry practice is to employ a two-part defense
               ther complicated by the fact that corrosion activity is normally   against  galvanic  corrosion  of  a  pipeline.  The  first  line  of
               deduced only from indirect evidence4irect observation is a   defense is a coating over the pipeline. This is designed to isolate
               rather limited option.                     the metal from the electrolyte. If this coating is perfect, the gal-
                The most common danger is from some form of galvanic   vanic cell is effectively stopped-the  electric circuit is blocked
               corrosion. Galvanic corrosion occurs when a metal or metals in   because the electrolyte is no longer in contact with the metal. It
               an  electrolyte (an electrically  conductive fluid) form  anodic   is safe to say, however, that no coating is perfect. If only at the
               and cathodic regions. A cathode is a metal region that has a   microscopic level, defects will exist in any coating system.
               greater  affinity  for electrons  than  the corresponding  anodic   The second line of defense is called cathodicprofecfion (CP).
               region. This affinity  for electrons is called electronegativity.   Through connections with other metals, the pipeline is turned
               Different metals have different electronegativities and even dif-   into a cathode, which, according to the galvanic cell model, is not
               ferent areas on a single piece of metal will have slightly differ-   subject to loss of metal (as a matter of fact, the cathode actually
               ent electronegativities. The greater the difference, the stronger   gains metal). The theory behind cathodic protection is to ensure
               the tendency for electrons to flow. If an electrical connection   that the current flow is directed in such a way that current flows to
               between anode and cathode exists. allowing this electron flow,   the pipeline, and away from an installed bed of metal that is
               metal will dissolve at the anode as metal ions are formed and   intended to  corrode. The installed metal that is to corrode is
               migrate from the parent metal. Chemical reactions occur at the   appropriately called sacrificial anode. The sacrificial anode has
               anode and the cathode as ions are formed and corrosion occurs.   a  lower  affinity  for  electrons than  the  steel  it  is  protecting.
               Such a system, with anode, cathode, electrolyte, and electrical   Depending on electrolyte (soil) type and some economic consid-
               connection between anode and cathode, is called agalvanic cell   erations, a voltage may be imposed on the system to further drive
               and is illustrated in Figure 4.5.          the current flow. When this is necessary, the system is referred to
                 Because soil is often an effective electrolyte, agalvanic corro-   as an impressed current system (Figure 4.6).
               sion  cell  can  be  established between  areas  along a  single a   In an impressed current system, rectifiers  are used to drive
               pipeline or between a pipeline and another piece ofburiedmetal.   the  low-voltage  current  flow  between  the  anode  bed  and
               When a new piece of pipe is attached to an old piece, a galvanic   the  pipeline. The  amount  of current required  is dictated  by

                                                - Current flow (electrical connection)

                                                         migration


                              Electrolyte













                                   Negati  \ \  - 1, ’ /,‘                 ions
                                   ions               ‘-/
                                                                 /
                                                   \    --         /
                                                                 /
                                                     \        I
                                             Figure 4.5  The galvanic corrosion cell
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