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Special Report                                                                   Special Report


 invested in corrosion monitoring, control   Table 1: Causes for failure of engi-  fi ed  as  ‘wet’  or  ‘dry’. A  liquid  or   of  corrosion.  Further distinction bet-  sion resistance, fabricability, aesthetic  plants for  determining the corrosion
 and management will save Rs. 7 worth   neering structures  moisture  is necessary for the  for-  ween macroscopically localized cor-  appearance,  ease of availability, and  allowances  to be provided so that  the
 of corrosion losses.  Cause  Share  mer, and dry corrosion usually in-  rosion and microscopic local attack can  costs.  plants can be operated and maintained

 High temperature corrosion   7%  volves reaction with high tempera-  be made as shown in Figure-3. Macro-  optimally  throughout their  economic
 Indirect losses occur due to the   ture gases.  scopic forms of corrosion affect greater  Alteration of environment  lifetime. Corrosion tests are also needed
 following reasons:  Stress corrosion cracking (SCC)   6%     Mechanism of corrosion: This  in-  areas of corroded metal and are gene-  Several alterations can be made in the  to troubleshoot corrosion problems
    Loss in revenue due to downtime.   Other forms of corrosion   29%   volves either electrochemical or   rally observable with the naked eye or  medium for controlling corrosion:   during normal operation of the plant in

    Loss in product through leakage.  Fatigue    25%  direct chemical reactions.  can  be viewed  with the  aid  of a low   Lowering the temperature;  order to increase operational reliability

    Loss in effi ciency.  Brittle fracture   16%     Appearance of the corroded metal:   power  magnifi cation.  In  microscopic   Reducing the velocity of the medium  of the assets.
    Contamination of product(s).  It is either uniform (entire surface   attack, the amount of metal dissolved is   and removing solid particles;
    Loss incurred due to over-design of   Overload   11%  is attacked uniformly) or localised   minute, and considerable damage can   Removing oxygen or oxidisers;  Well planned and  executed tests

 assets (huge corrosion allowances   Creep    3%  (small area is affected).  occur before the problem becomes   Changing the concentration; and  usually  results in reproducibility  and

 and selection of costly corrosion   Wear/abrasion/erosion  3%  visible to the naked eye.      Dozing corrosion inhibitors.  reliability. It is very important for the
 resistant materials).  Classifi cation by appearance, which               tests to duplicate the actual plant ser-
 leads to partial or complete damage of  is particularly  useful in failure analy-  The factors infl uencing corrosion in  Other strategies include:  vice conditions as closely as possible.
 Another important  indirect  cost of  assets, incurring huge economic losses  sis, is  based  on identifying  forms  of   any asset can be summarized as: stress   Selecting adequate design of the  The  greater  the deviation  from plant

 corrosion is safety and environmental  and creating safety hazards for the plant  corrosion by visual observation.  The   factors, material  factors, and environ-  equipment and  selecting adequate  conditions  the less reliable  the tests.
 hazards. Lots of accidents  take place  people and also people at large living in  morphology of  attack is  the basis  for   mental factors. Corrosion occurring due   wall thickness;  Corrosion testing  include  laboratory
 due to failure  of assets due to corro-  the society.  classifi cation.   Figure-2,   illustrates   to the interaction of the above factors is   Applying cathodic and anodic pro-  tests including acceptance or qualifying

 sion, particularly when handling hazar-  schematically the most common forms   depicted schematically in Figure-4.  tection for protecting critical assets;  tests; pilot-plant  tests; plant or  actual
 dous chemicals. For example, in the   Table 1 clearly shows that corrosion   and  service tests; and fi eld tests.
 Bhopal gas accident, corroded methyl  problems cause majority of failures in   Asset integrity management by      Applying protective coatings on the
 isocyanate (MIC) storage tanks and  assets. However, in chemical  industry   corrosion control  assets.   Laboratory  tests  are  classifi ed  by
 valves allowed water ingress  leading  the majority of failures affecting asset   small specimens and small volumes
 to a fi ve-fold increase in pressure in an  integrity are due to corrosion of static   The following methods are gene-  Corrosion testing for asset integrity   of solutions, and actual conditions are
 hour. In addition, the fl are system could  equipment subjected to aggressive   rally applied for controlling  corrosion  management  simulated in sofar as conveniently pos-
 not be used due to a corroded pipeline.  environments.  in assets:  Corrosion tests are necessary to  sible. They serve as screening tests to
 The disintegrated (ruptured) storage    select materials  of  construction for  determine which  materials warrant
 tanks (assets) led to immediate death  Mechanism and classifi cation of   Proper material selection  equipment used in the process industry.  further investigation.  Figure-5 shows
 of 2,259 people and caused exposure of  corrosion  The criteria for proper material  The test results (corrosion rate, etc.) are  a laboratory setup where samples are
 MIC vapour to about 5,00,000 people   It is convenient to classify corrosion   selection are mechanical strength, corro-  used at the design stage of the process  subjected to boiling solution.
 in December 1984.  by the forms in which it manifests itself
 in order to manage it. Classifi cation is
 Figure-1 shows the schematic view  usually based on one of three factors:
 of the different kinds of losses encoun-     Nature of corrodent: It can be classi-  Fig. 3: Broad  Classifi cation of Corrosion
 tered due to corrosion.




 ECONOMIC  CONSERVATION  HUMAN SAFETY
 INDIRECT LOSSES (3.5%)   DIRECT LOSSES (4.2%)
 LOSS IN REVENUE DUE TO DOWNTIME.                                          Fig. 5: Laboratory tests in boiling solutions
 LOSS IN PRODUCT THROUGH LEAKAGE.
 LOSS IN EFFICIENCY                                                          Pilot plant tests are usually the best
 CONTAMINATION OF PRODUCT                                                 and most desirable. Here the tests are
 OVER-DESIGN                                                              made in a small-scale plant, which es-
                                                                          sentially duplicates the intended large-
 Fig. 1: Signifi cance of Corrosion Control &
 Asset Integrity MGT                                                      scale operation. Actual raw  materials,
                                                                          concentrations, temperatures, veloci-
 Failures of structures due to lack of                                    ties, and volume  of liquor to area of
 asset integrity management                                               metal exposed are involved. Pilot plants
 Lack of asset integrity management   Fig. 2:  Common forms of corrosion  Fig. 4:  Factors infl uencing corrosion  are usually run long enough to ensure


 176  Chemical Weekly  July 2, 2024  Chemical Weekly  July 2, 2024                                     177


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