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may occur at stagnant conditions.



                      If,  however,  there  is  a  possibility  of  H2S  contamination,  Cu-Ni  is  not

               recommended. As a follow-up, exotic materials such as 22 Cr and 25 Cr duplex

               and 6 Mo stainless steels, Ni base austenitic alloys and titanium alloys began

               to be introduced. These new alloys offered excellent corrosion resistance and

               are weldable.



               Materials for Seawater Systems

                      *      The  recommended  materials  for  seawater  service  below  60°F

               (15°C) are 6 Mo and 25 Cr duplex stainless steels, and for service greater than

               60°F  (15°C)  Ti  or  fibre-reinforced  polymer  (FRP).  Some  problems  were

               encountered with early application of FRP that were attributed to improper design,

               handling and installation. For stainless steels, a minimum PRE value (PRE = % Cr

               + 3.3 x % Mo + 16 x % N) of 40 must be specified.

                      *      The  6  Mo  or  25  Cr  duplex  stainless  steel  piping  can  be  used  in

               higher temperature service up to 95°F (35°C), if crevices are avoided or they

               are  overlaid  by  Inconel  625.  Flanges  and  threaded  connections  must  also  be

               manufactured  from  crevice  corrosion-resistant  alloys  such  as  the  superaustenitic

               material (654 SMO or UNS S34565).

                      *      A  small  amount  of  oxygen  in  the  water  causes  pitting  and  crevice

               corrosion in 22 Cr, while 25 Cr and 6 Mo will stand higher oxygen content.



               Materials for Process Piping and Equipment

                   *  Produced  fluids  are  generally  corrosive  due  to  the  presence  of  water,

                      CO 2,  H 2S  and  chlorides.  Assessment  of  the  corrosivity  of  the  produced

                      fluids  is  established  using    prediction  models.  The  most  widely  used

                      models are for predicting CO 2 corrosion. The common practice is to use

                      carbon steel if the predicted corrosion rates can be accounted for by the

                      addition of less than 0.25" (6 mm) as a corrosion allowance. If a higher

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