Page 191 - CW E-Magazine (3-12-2024)
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Special Report


                                                                          solutions. These results generally show
                                                                          the corrosion rates to decrease with
                                                                          increasing  nickel content  in the alloy.
                                                                          It should be mentioned that the weight
                                                                          loss data obtained with 310 SS, Ni, and
                                                                          high Ni alloys are not reliable, as they
                                                                          passivate in hot 50% NaOH solutions.
                                                                          The reason for the high corrosion rates
                                                                          of Fe-Cr-Ni alloys was found to be
                                                                          the preferential  dissolution  of Fe and
                                                                          Cr. Cu dissolves from Monel 400 and
                                                                          Mo from Mo-containing alloys such
                                                                          as Type  316  SS  and  alloy  825  in  hot
                                                                          concentrated NaOH.

                                                                             The corrosion behaviour of nickel-
                                                                          based alloys was significantly influen-
                                                                          ced  by thepresence  of oxygen  or
                                                                          hydrogen in the solution. These mate-
                                                                          rials exhibited reversible hydrogen elec-
         Fig. 17: Corrosion rate as a function of the Nickel content in alloys in boiling 40% NaOH
                                    solutions.                            trode  potential  in hydrogen-saturated
        Table 3: Chemical Composition of Austentic  and Ferritic Stainless steels  solutions. However, in oxygen saturated
                                              a
                                                                          solutions, they corroded by the  diffu-
                            Chemical composition (wt %)                   sion of oxygen through the porous
                     C   Si  Mn     P    S   Ni    Cr   Mo     N   Other  β-Ni(OH)  layer formed in the passive
                                                                                  2
       AISI 304    0.06 0.54 0.81 0.031 0.002  8.48  18.91  –             region on the surface.
       AISI 316A   0.04  0.5 1.63  0.03 0.002 13.12  16.5    2.35
       AISI 316B   0.06 0.45 1.67 0.033 0.002 12.91  16.58  2.21  –          Since austenitic stainless steels are
       AISI 305J   0.02  0.4 0.82 0.029 0.002 12.96  17.08  –             susceptible to pitting and intergranular
               1
       Type 405    0.08                           12.5    –     – 0.2 (AI)  corrosion in the presence of chloride
       Type 430    0.08                          14-18    –  0.02         ions, other materials have been exami-
       Type 446    0.08                          23-27    –  0.03         ned for caustic  service.These  include
                                                                          Fe-Cr alloys, which  are  resistant  to
       High purity  0.002                        12-30 0 to 2 0.008       SCC. However, these alloys are brittle.
       Fe-Cr                                                              A popular alloy examined for the caustic
       a Heat treated at 1150 C for 3 to 5 min.                           evaporator service was E-Brite-26-1,
                    o
       using nickel or SS tanks. Non-metallics   pickup of iron in caustic is acceptable.    containing 26% Fe and 1% Mo, which
       useful for caustic service  within their  Corrosion rate as a function of the   exhibited performance characteristics
       normal temperature limits include  Nickel content in  alloys in boiling   comparable to that of nickel. However,
       PVC, polypropylene, phenolics, PTFE,  40% NaOH solutions are presented in    it  suffered from serious intergranular
       FEP, PVDF, natural rubber, neoprene,  Figure-17 and Table-3 depicts the typical   corrosion problems, which were attri-
       halogenated  polyesters, and chloro-  composition of various stainless steels.  buted to changes in the metallurgy and
       sulphonated polyethylene (15, 16).                                 chemistry of this material. E-Brite 26-1
                                           Austenitic stainless steels show uni-  is not used in new caustic evaporators
       Stainless steel                   form corrosion and intergranular  cor-  (15, 16).
          A comparison of corrosion rates in  rosion in NaOH solutions.  Figures-18
       hot  concentrated NaOH solutions  asa  and  19  illustrate  the  corrosion  rate  of    Nickel
       function of  the nickel content in the  materials inboiling 30% NaOH and 50%    Nickel is the ideal material for hand-
       alloys shows  that nickel is  extremely  NaOH solutions, determined by weight   ling caustic at all concentrations  and
       resistant to NaOH. Stainless steels are  loss measurements and linear polariza-  temperatures, including molten  anhy-
       acceptable  for caustic  service if the  tion methods in hydrogen-saturated   drous caustic up to 480°C. Nickel and


       Chemical Weekly  December 3, 2024                                                               191


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