Page 210 - Corrosion Engineering Principles and Practice
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184   C h a p t e r   6                R e c o g n i z i n g   t h e   F o r m s   o f   C o r r o s i o n    185



                 6.4  Velocity Induced Corrosion
                      Velocity induced corrosion refers to problems caused or accelerated
                      by the relative motion of the environment and the metal surface. It is
                      characterized by surface features with a directional pattern which are
                      a direct result of the flowing media.
                         With the exception of cavitation, flow-induced corrosion problems
                      are generally termed erosion–corrosion, encompassing flow enhanced
                      dissolution  and  impingement  attack.  The  fluid  can  be  aqueous  or
                      gaseous,  single  or  multiphase  [23].  There  are  several  mechanisms
                      described by the conjoint action of flow and corrosion that result in
                      flow-accelerated corrosion (FAC) [24;25]:
                         Mass  transport–control:  Mass  transport–controlled  corrosion
                         implies that the rate of corrosion is dependent on the convective
                         mass-transfer processes at the metal/fluid interface. When steel
                         is exposed to oxygenated water, the initial corrosion rate will be
                         closely related to the convective flux of dissolved oxygen toward
                         the surface, and later by the oxygen diffusion through the iron
                         oxide layer. Corrosion by mass transport will often be streamlined
                         and smooth.
                         Phase  transport–control:  Phase  transport–controlled  corrosion
                         refers to conditions when wetting of the metal surface by a cor-
                         rosive  phase  is  flow-dependent.  This  may  occur  because  one
                         liquid phase separates from another or because a second phase
                         forms from a liquid. An example of the second mechanism is the
                         formation of discrete bubbles or a vapor phase from boiler water
                         in horizontal or inclined tubes in high heat-flux areas under low
                         flow conditions. The corroded sites will frequently display rough,
                         irregular surfaces and be coated with or contain thick, porous
                         corrosion deposits.
                         Erosion–corrosion:  Erosion–corrosion  has  been  associated  with
                         mechanical removal of the protective surface film resulting in a
                         subsequent corrosion rate increase via either electrochemical or
                         chemical processes. It is often accepted that a critical fluid velocity
                         must be exceeded for a given material. The mechanical damage by
                         the impacting fluid imposes disruptive shear stresses or pressure
                         variations on the material surface and/or the protective surface
                         film. Erosion–corrosion may be enhanced by particles (solids or
                         gas bubbles) and impacted by multi-phase flows. The morphol-
                         ogy of surfaces affected by erosion–corrosion and FAC may be in
                         the form of shallow pits or horseshoes or other local phenomena
                         related to the flow direction (Fig. 6.37).
                         Cavitation:  Cavitation  sometimes  is  caused  by  the  formation
                         and collapse of vapor bubbles in a liquid near a metal surface.
                         Cavitation removes protective surface scales by the implosion of
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