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TECHNICAL PAPER



         however, ensures the production of hydroxyl ions on the surface   low concentrations near the reinforcement as they are being
         of the steel from the cathodic reaction (Equation 1).  repelled away are unlikely to cause depassivation, so only
                                                                modest polarization is needed, typically an impressed current
                                  -
                      ½ O 2  + H 2 O + 2e   →  2OH -   (1)
                                                                density of about 0.4-2 mA/m (1 to 2 in Figure 1), to maintain
                                                                                       2
         The applied electric field also attracts alkali cations, present   the steel at a potential where pits cannot initiate. Bertolini et
         in the pore electrolyte, such as Na , K  and Ca , to the   al termed this Cathodic Prevention . As chloride penetration
                                       +
                                              2+
                                    +
                                                                                             [1]
         now negatively charged steel. The opposite occurs with the   progresses, it must of course be ensured that the potential
         negatively charged Cl  anions which are repelled away from   remains below the upper boundary of the imperfect passivity
                          -
         the steel. The reduction of the destructive Cl  ions renders the   domain (2 to 3 in Figure 1) but much higher chloride levels can
                                            -
         surrounding electrolyte less aggressive to the steel. Aided by   be tolerated at the steel before corrosion can initiate.
         the increase in alkali, which maintains the steel passive, the
         thermodynamic equilibrium moves to the left, as indicated in   Further interesting proposals have also surfaced at different
         Figure 1 by the thick arrow. It would be reasonable to suggest   times. Intermittent CP in marine tidal locations, where remote
         that the chloride concentration axis can be changed to a ratio of   anode systems in seawater might be employed, and the use
         chloride to hydroxyl ionic concentration, enabling the potential   of solar powered impressed current CP where low levels of
                                                                                    [2]
         passivation of the steel with time as [Cl ]/[OH ] reduces, even   polarisation are required  are examples of this. Another
                                             -
                                        -
         if the level of steel polarisation remains the same (5 to 7 to 8,   interesting application on which this paper will concentrate on,
         Figure 1). These aspects will be elaborated further later in the   is the use of galvanic anodes to protect both regions of the steel
         article.                                               reinforcement susceptible to corrosion following a conventional
                                                                patch repair in chloride-contaminated concrete and as a means
         Understanding of these principles was essential for the   of reducing the corrosion activity of the steel reinforcement
         development and evolution of CP of reinforcing steel in   where chlorides have penetrated the cover concrete to the steel
         concrete. As an example, the recognition that the primary   and have initiated corrosion  [3,4] .The use of galvanic anodes to
         objective of CP, unlike cases such as buried pipelines and   prevent re-initiation of corrosion of the steel following a short
         submerged steel structures where total immunity is required   period of intense ICCP with the intension of arresting corrosion
         (Domains D and E in Figure 1), is simply to reduce the   is perhaps the major recent development in the technology
         susceptibility of the metal to pitting in the presence of chloride   which may drive the future of CP.
         ions was a major development. To achieve adequate CP in
         a structure in which chloride-induced corrosion has been
         occurring for some time, it is only necessary to polarize the steel   2.  HISTORICAL DEVELOPMENT OF CP FOR
         from its condition of pitting (Domain A) to Domain C where   STEEL REINFORCED CONCRETE
         pitting is unstable. Thus, complete repassivation of the steel can   The earliest recorded applications of CP to steel in concrete
         be achieved.                                           were for buried pipelines  [5,6] . In such cases, where the material

         A development in Italy, which demonstrated a clear     is surrounded by a conductive electrolyte such as groundwater
         understanding of the principles of CP in reinforced concrete,   or damp soil, it is possible to use discrete anode systems to
         was the application of CP on prestressed concrete viaducts as   distribute the current to the steel reinforcement. Several such
         a means of preventing the initiation of corrosion. In such cases,   uses of CP have been described involving both impressed
                                                                                        [7]
         even though the structures may be exposed to chlorides, their   current and sacrificial anodes .
                                                                In atmospherically exposed reinforced concrete, it is technically
                                                                much more difficult to apply CP because of the need to ensure a
                                                                reasonably uniform current distribution in a concrete electrolyte
                                                                of fairly high resistivity. To comply with this requirement, initially
                                                                only externally applied DC power supplies were considered
                                                                which required the necessary development of inert anode
                                                                systems that meet the following conditions:
                                                                i.   capable of being applied to concrete surfaces or cover
                                                                    concrete in such a way as to allow uniform electrolytic
                                                                    conduction,
                                                                ii.   acceptable in terms of weight, cost and durability in
                                                                    service under a wide range of environmental exposure
                                                                    conditions,

         Figure 1: Approximate domains of electrochemical behaviour of steel in   iii.   resistant to corrosion and acidification of the surrounding
              concretes with increasing levels of chloride contamination  concrete owing to anodic reactions on its surface.


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