Page 757 - Corrosion Engineering Principles and Practice
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708    C h a p t e r   1 5                                                                                                H i g h - Te m p e r a t u r e   C o r r o s i o n    709


                      Chemical  reactions  between  these  deposits  and  the  protective
                      surface oxide can lead to destruction of the oxide and rapid corrosive
                      attack.  In  gas  turbines,  oxidized  sulfur  contaminants  in  fuel  and
                      chlorides from ingested air (marine atmospheres) tend to react to
                      form  salt  deposits.  The  presence  of  sodium  sulfate,  potassium
                      sulfate, and calcium sulfate together with magnesium chloride have
                      been  reported  in  such  deposits  for  compressor-stage  components
                      [14]. Sodium sulfate is usually regarded as the dominant component
                      of the salt deposits.
                         Testing has indicated that in commercial nickel- and cobalt-based
                      alloys, chromium additions play an important role in limiting this
                      type  of  damage. Alloys  with  less  than  15  percent  of  chromium  as
                      alloying addition are considered highly vulnerable to attack.
                         Refinery heaters and boilers that are fired with low-grade fuels may
                      be vulnerable to such corrosion damage, especially if vanadium, sulfur,
                      and  sodium  contaminants  are  present  at  high  levels.  Vanadium
                      pentoxide and sodium sulfate deposits assume an important role in this
                      type of environment. The melting point of one of these mixed compound
                      deposits  (Na SO -V O )  can  be  as  low  as  630°C,  at  which  point
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                      catastrophic corrosion can set in. In these severe operating conditions
                      the use of special high-chromium alloys is required. A 50Ni-50Cr alloy
                      has been recommended over the use of 25Cr-12Ni and 25Cr-20Ni alloys
                      for  hangers,  tube  sheets,  and  other  supports.  Ash  and  salt  deposit
                      corrosion is also a problem area in fireside corrosion of waste incinerators,
                      in calcining operations, and in flue gas streams.
                      15.4.8  Corrosion by Molten Salts
                      Corrosion  damage  from  molten  salts  can  occur  in  a  wide  variety  of
                      materials and by different mechanisms. It has been pointed out that
                      although  many  studies  have  been  performed,  quantitative  data  for
                      materials selection and performance prediction are rarely available [15].
                      Molten salt corrosion is usually applicable to materials retaining the
                      molten salt, as used in heat treating, solar and nuclear energy systems,
                      batteries, fuel cells, and extractive metallurgical processes. Some factors
                      that can make molten salts extremely corrosive include the following:
                          •  By acting as fluxes, molten salts destabilize protective oxide
                             layers (on a microscopic scale, this effect contributes toward
                             fuel ash corrosion described above).
                          •  High temperatures are typically involved.
                          •  Molten  salts  are  generally  good  solvents,  preventing  the
                             precipitation of protective surface deposits.
                          •  Direct chemical reaction between the containment material
                             and the salt.
                          •  The  presence  of  noble  metal  ions  in  the  molten  salt,  more
                             noble than the containment material itself.
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