Page 327 - Corrosion Engineering Principles and Practice
P. 327

298     C h a p t e r   8                                                                                                           C o r r o s i o n   b y   W a t e r    299


                         Almost all of the components in a supercritical steam plant are
                      made of austenitic stainless steels of the 18-8 variety, for example,
                      S30403 or 31603. These materials are employed to minimize corrosion
                      products  and  their  transport  through  the  system.  The  steam
                      temperature  is  no  higher  than  in  an  ordinary  superheater,  but  the
                      pressures are such that many chemicals and corrosion products may
                      show appreciable solubility in the steam.
                         Many chemicals exhibit an inverse solubility when the temperature
                      of  the  steam  is  above  the  critical  temperature  and  will  therefore
                      deposit out at these higher temperatures. In one supercritical plant,
                      about 140 ppm caustic was accidentally introduced into the plant.
                      Within 30 minutes, caustic stress corrosion cracking (SCC) occurred
                      in that part of the plant where the temperature was about 425°C. This
                      temperature corresponds to the minimum in the caustic solubility-
                      temperature curve. The supercritical steam also undergoes a marked
                      density increase above this temperature range which could accelerate
                      the deposition of chemicals.
                         For such reasons, the dissolved solids content of the water must
                      be kept as close as possible to zero. A large fraction of the water is
                      continuously cleaned up in a bypass circuit containing ion exchange
                      (demineralizer) beds. At start-up, 100 percent of the water may be
                      passed through the cleanup beds. Chlorides and caustic are the most
                      undesirable  salts  because  they  are  known  to  cause  SCC  of  the
                      austenitic stainless steels. Dissolved oxygen may be reduced by the
                      methods described previously to a few parts per billion.
                         Copper  deposition  on  turbine  blades  was  an  early  problem  with
                      supercritical  units.  It  was  found  that  trace  amounts  of  copper  were
                      dissolved  from  the  condenser  tubes  and  recirculated  into  the  boiler
                      section. Because of its excellent solvent properties, the superheated steam
                      carried the dissolved copper into the turbine where, at the lower pressure,
                      copper was deposited upon the turbine blades. This not only affected the
                      efficiency, but threatened to destroy the turbine by mechanical imbalance
                      due to uneven deposition. The problem has been largely eliminated by
                      using stainless steel or titanium in the condenser.

                      8.5.4  Waste Heat Boilers
                      In many chemical or petrochemical processes, economy dictates that
                      superfluous  exotherms  be  utilized  to  generate  steam  as  an  energy
                      conservation measure. Examples are the cooling of a butane oxidation
                      reaction or the condensation of hot sulfur vapors, steam pressure being
                      generated on the shell side of specially designed heat exchangers.
                         Corrosion problems in waste heat boilers usually arise either from
                      unusual materials of construction or from inattention to the required
                      details of water treatment. Austenitic stainless steels may be required
                      from the process-side corrosion aspects, yet be highly susceptible to
                      SCC from boiler feedwater. The most frequent problem, however, is
                      that the operating department personnel, whose primary concern is
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