Page 157 - Corrosion Engineering Principles and Practice
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132    C h a p t e r   5                                                                    C o r r o s i o n   K i n e t i c s   a n d   A p p l i c a t i o n s   o f   E l e c t r o c h e m i s t r y    133


                      intermediate cases the results of the measurement of Z  would show
                                                                    n
                      a mixed behavior and be more difficult to interpret. For example, if
                      hydrogen  bubbles  are  evolving  on  the  cathode  while  the  anode
                      undergoes generalized corrosion, the noise of the cathode is orders of
                      magnitude larger than that of the anode, so that Z  becomes equal to
                                                                n
                      the impedance modulus of the anode, |Z |. In these conditions, while
                                                        a
                      the  time  records  appear  to  show  only  the  cathodic  processes,  the
                      impedance  measured  is  that  of  the  anode,  using  the  noise  of  the
                      cathode as input signal.
                         An opposite case would be a cell where the anode is undergoing
                      pitting, while the cathodic reaction is the reduction of dissolved
                      oxygen or an imposed galvanic situation. Since the anodic noise is
                      preponderant, Eq. (5.27) shows that Z  is equal to the impedance
                                                        n
                      modulus  of  the  cathode,  |Z |.  The  anodic  noise  is  the  internal
                                                c
                      signal  source  utilized  for  the  measurement  of  the  impedance  of
                      the cathode.
                      Coupled Multielectrode Array Systems and Sensors
                      The  use  of  multielectrode  array  systems  (CMAS)  for  corrosion
                      monitoring  is  relatively  new.  The  advantages  of  using  multiple
                      electrodes include the ability to obtain greater statistical sampling of
                      current fluctuations, a greater ratio of cathode-to-anode areas in order
                      to enhance the growth of localized corrosion once initiated. CMAS
                      also provide the ability to estimate the pit penetration rate and obtain
                      macroscopic spatial distribution of localized corrosion [25].
                         Figure 5.38 shows the principle of the CMAS in which a resistor is
                      positioned between each electrode and the common coupling point
                      [26].  Electrons  from  a  corroding  or  a  relatively  more  corroding
                      electrode flow through the resistor connected to the electrode and
                      produce a small potential drop usually of the order of a few microvolts.
                      This  potential  drop  is  measured  by  the  high-resolution  voltage-
                      measuring instrument and used to derive the current of each electrode.
                      CMAS  probes  can  be  made  in  several  configurations  and  sizes,
                      depending on the applications. Figure 5.39 shows some of the typical
                      probes that were reported for real-time corrosion monitoring.
                         Because  the  electrode  surface  area  is  usually  between  1  and
                      0.03 mm , which is approximately 2 to 4 orders of magnitude less
                             2
                      than that of a typical LPR probe or a typical electrochemical noise
                      (EN) probe, the prediction of penetration rate or localized corrosion
                      rate by assuming uniform corrosion on the small electrode is realistic
                      in most applications. CMAS probes have been used for monitoring
                      localized corrosion of a variety of metals and alloys in the following
                      environments and conditions:
                          •  Deposits of sulfate-reducing bacteria
                          •  Deposits of salt in air
                          •  High pressure simulated natural gas systems
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