Page 119 - Corrosion Engineering Principles and Practice
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94    C h a p t e r   5                                                                    C o r r o s i o n   K i n e t i c s   a n d   A p p l i c a t i o n s   o f   E l e c t r o c h e m i s t r y    95


                      This is represented by the horizontal line where C = C . There is also a
                                                                  O
                      region where the concentration drops, falling to zero at the electrode
                      surface.  The  Nernst  diffusion  layer  associated  with  this  drop  has  a
                      specific thickness (d ) that depends upon the nature of the solution into
                      which it extends. For stirred aqueous solutions the thickness of the
                      diffusion layer varies between 0.01 and 0.001 mm.
                         For a chemical species O that is consumed by the cathodic reaction
                      at  the  corroding  surface,  the  concentration  gradient  (d C /d x)  is
                                                                         O
                      greatest when the concentration of that species is completely depleted
                      at the surface, that is, C  = 0. It follows that the cathodic current is
                                          O
                      limited in that condition, as expressed by Eq. (5.14).

                                         i =  i = − nFD O  C bulk          (5.14)
                                                      O
                                          c
                                                      d
                                             L
                         For  intermediate  cases,  that  is,  when  the  cathodic  current  is
                      smaller than i , h conc  can be evaluated using an expression [Eq. (5.15)]
                                 L
                      derived from Nernst equation:
                                           2 303 × RT       i
                                            .
                                     h conc  =  nF  log 10   1 −  i L       (5.15)
                      where 2.303 × R × T/F = 0.059 V when T = 298.16 K.


                 5.4  Ohmic Drop
                      The ohmic overpotential appears in Eq. (5.2) as the simple product of
                      a resistance and a current between the anodic and cathodic sites of a
                      corrosion  process.  For  many  corrosion  situations  these  sites  are
                      adjacent to each other and the ohmic drop is negligible, particularly
                      so when the environment itself is a good electrolytic conductor, that
                      is,  seawater.  However,  there  are  special  conditions  where  the
                      separation of the anodic and cathodic sites can be an important factor
                      in the corrosion progress, for example, galvanic corrosion, or even an
                      integral part of a particular protection scheme, for example, anodic
                      and cathodic protection.

                      5.4.1  Water Resistivity Measurements
                      The conductivity of an environment can itself be a complex function.
                      When a salt dissociates, the resulting ions interact with surrounding
                      water molecules to form charged clusters known as solvated ions.
                      These ions can move through the solution under the influence of an
                      externally applied electric field. Such motion of charge is known as
                      ionic  conduction  and  the  resulting  conductance  is  the  reciprocal
                      function of the resistance of an environment.
                         The dependence upon the size and shape of the conductor can be
                      corrected by using the resistivity r rather than the resistance R, as
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