Page 309 - Corrosion Engineering Principles and Practice
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280     C h a p t e r   8                                                                                                           C o r r o s i o n   b y   W a t e r    281


                      Nations Scientific, Education, and Cultural Organization (UNESCO)
                      committee to determine a more precise relation between chlorinity
                      and salinity. The definition of 1969 produced by UNESCO is written
                      in Eq. (8.2):

                                     S (‰) = 1.80655 Cl (‰)                 (8.2)

                         The definitions of 1902 and 1969 give identical results at a salinity
                      of  35‰  and  do  not  differ  significantly  for  most  applications.  The
                      definition  of  salinity  was  reviewed  again  when  techniques  to
                      determine salinity from measurements of conductivity, temperature,
                      and pressure were developed. The Practical Salinity Scale defined in
                      1978 is a complex function related to the ratio (K) of the electrical
                      conductivity  of  a  seawater  sample  to  that  of  a  potassium  chloride
                      (KCl) solution with a mass fraction in KCl of 0.0324356, at the same
                      temperature and pressure.

                                   S = 0.0080 – 0.1692K 0.5  + 25.3853 K
                                      + 14.0941 K 1.5  – 7.0261 K + 2.7081 K 2.5    (8.3)
                                                         2
                         Note that ‰ is no longer used in this definition. In fact, a value of
                      35‰ would simply correspond to a value of 35 on the Practical Salinity
                      Scale.

                      Precipitation of Calcareous Deposits.  The natural presence of calcium
                      and magnesium in seawater has been advantageously used to coat
                      internal walls of vessels such as ballast tanks with a protective film of
                      calcareous deposits. These films, once they are formed by the cathodic
                      polarization of metal surfaces in seawater, greatly reduce the current
                      density needed to maintain a prescribed cathodic potential. For most
                      cathodic surfaces in aerated waters, the main reduction reaction is
                      described by Eq. (8.4):

                                                   −
                                                           −
                                       O + 2 H O + 4e →  4OH                (8.4)
                                         2
                                              2
                         In cases where the potential is more negative than the reversible
                      hydrogen electrode potential, the production of hydrogen as described
                      in Eq. (8.5) becomes possible:
                                       2H O 2e →  H + 2OH                   (8.5)
                                            +
                                                          −
                                               −
                                                    2
                                          2
                         In  either  case,  the  production  of  hydroxyl  ions  results  in  an
                      increase in pH for the electrolyte adjacent to the metal surface. This
                      situation causes the production of a pH profile in the diffuse layer
                      where the equilibrium reactions can be quite different from the bulk
                      seawater  conditions.  Temperature,  relative  electrolyte  velocity  and
                      electrolyte composition will all influence this pH profile. In seawater,
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