Page 519 - Corrosion Engineering Principles and Practice
P. 519

486     C h a p t e r   1 2                                                                                                        C o r r o s i o n   a s   a   R i s k    487


                      where RL  is  remaining life of current component (years)
                              C
                            RL  is remaining life of replacement components (years)
                              R
                            RL  and RL  are respectively derived from Eqs. (12.4) and (12.5):
                              C      R
                                                CA − DT 
                                          RL =     CR                  (12.4)
                                             C

                                                  CA 
                                            RL =    CR                 (12.5)
                                               R

                      where CA is corrosion allowance* (design or fitness for purpose) (mm)
                            DT is damage to date (mm)
                            CR is measured corrosion rate (mm/y)
                         The above formulae have been developed from an actual pipe-
                      work monitoring and replacement program as a result of internal cor-
                      rosion effects. Both replacement cost (R cost ), component remaining life
                      (RL ), and field life (FL) are key factors in this method and reflect the
                         C
                      need to understand accurate costing of installation and replacement
                      activities. Required field life is not necessarily the difference between
                      installation and design lives but more appropriately the time remain-
                      ing until end of field or production life.

                      12.4.2  Corrosion Inhibition Level Key Performance Indicator
                      This KPI is a measure of the availability of corrosion inhibitors to pro-
                      vide protection against corrosive processes. The inhibitor efficiency
                                                                               †
                      itself should have been determined from a combination of previous
                      laboratory and field testing to determine the optimum concentration








                      * Corrosion allowance depends on the type of defect anticipated, which needs to
                       be identified by inspection. Once the defect geometry is known and the process
                       parameters  identified,  the  maximum  allowable  defect  size  may  be  calculated
                       using fitness for purpose criteria to ensure that failure does not occur.

                      † The efficiency of an inhibitor is expressed as a measure of the improvement in
                       lowering the corrosion rate of a system:
                                                   CR    −  CR  
                                                              h
                                Inhibitor efficiency (%) =   uninhibited  inhibited  × 100
                                                     CR uninhibited  
                       where CR uninhibited  = corrosion rate of the uninhibited system and
                               CR   = corrosion rate of the inhibited system
                              inhibited
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