Page 304 - Failure Analysis Case Studies II
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                       3.1.  Calcanic corrosion
                         The mixture  of  copper  pipes and  steel radiators  makes  up  a galvanic couple.  The  Pourbaix
                       diagram for copper is shown in Appendix A. Copper will be immune from corrosion in mains water
                       as long as its potential is kept below 0 V. This is 0.6 V higher than the corrosion potential of iron.
                       The copper is in excellent electrical contact with the steel through soldered joints or compression
                       fittings. Because of this, the iron corrodes in preference to the copper, and acts as a sacrificial anode.
                       The copper is protected by cathodic protection and provides an inert surface at which the cathodic
                       oxygen-reduction reaction takes place. In practice, the extent of galvanic corrosion is limited by the
                       ionic conductivity of the water. If the conductivity is low, the electrical resistance of the galvanic
                       cell is high, and the steel will only corrode galvanically near to a copper surface. On the other hand,
                       if  the conductivity is high galvanic attack  will  occur some distance away from the copper.  The
                       solution conductivity can be decreased considerably if insoluble corrosion products form.
                         There is another way in which the copper pipes can lead to galvanic corrosion. The bore of the
                       tubes corrodes slowly, and releases copper ions into the circulating water. At steady state, it is quite
                       common to find concentrations  of Cu2+ of 0.14,2mgl-’  [4]. Because steel is more reactive than
                       copper, the following reaction takes place where the water passes over the steel surfaces:
                                                   Cu2+ + Fe = Fe2+ + Cu.                      (1)
                        The copper metal produced by the reaction deposits on the surface of the steel as an extremely
                       thin layer. Galvanic cells are then set up between the islands of deposited copper and the steel in
                       between [3, 61. However, opinions vary as to how important this mechanism really is.


                       3.2.  Dissolved ions
                         Mains water typically contains approximately 50ppm C1-  and SO:-  in association with Na+,
                       Ca2+ and Mg2+. The ions increase the conductivity of the water, and help the corrosion processes.
                       The metal ions migrate to the cathodic surfaces where they neutralize the OH-  ions produced by
                       the oxygen-reduction reaction. The C1-  ions are small and highly mobile: they migrate rapidly to
                       the anodic areas, and neutralize the Fe2+ ions produced when the iron dissolves. When mains water
                       enters the system to make up for evaporation, it brings dissolved ions with it, and over time the
                       concentration  of the ions in the circulating water will increase. Both CI-  and SO:-  are aggressive
                       ions: they  help to stop passive oxide films forming on the  surface of  steel, and  this encourages
                       corrosion even more.


                       3.3.  Pitting
                        The surface of the steel tends to divide itself into anodic areas (where the iron corrodes) and
                       cathodic areas (where the oxygen-reduction reaction takes place). This separation is encouraged by
                       anything  which makes  the  environment  of  the  steel non-uniform.  In  most  places,  the  metal  is
                       exposed to the flowing water (and the oxygen it contains), and behaves cathodically. However, steel
                       in crevices has almost no exposure to oxygen, and behaves anodically. Crevices are present in many
                       places: under deposits of sludge, next to welds, and in screwed connections. Obviously, the current
                       of  electrons produced by  the anodic areas must balance the current of electrons delivered to the
                       cathodic  area. Since the  anodes  are  small compared  to  the cathodes,  the current density at the
                       anodes will be large compared to the current density at the cathodes. The steel will corrode rapidly
                       over a small area, and localized pits will form.


                                             4.  REDUCTION  OF  HYDROGEN

                        Figure 7 shows the line for the hydrogen-reduction reaction superposed on the Pourbaix diagram
                       for iron. The open-circuit potential for the hydrogen-reduction reaction in mains water is -0.4V.
                       The voltage difference available to drive the corrosion process is -0.4  - (- 0.6) = 0.2 V. The hydro-
                       gen-reduction reaction polarizes rapidly: an “overvoltage” is needed to make the reaction go at a
                       reasonable rate. The extent of the polarization depends strongly on the metal or alloy concerned,
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