Page 191 - CW E-Magazine (12-12-2023)
P. 191

Special Report                                                                   Special Report


 140°C under dry conditions, while a   Usually, crude oil is separated into  lized general thinning and pitting cor-  of process parameters such as pH, tem-  line carrying crude oil depicting forma-
 normal FBE coating is used from -30°C  three categories based on the API gra-  rosion are possible  as well.  Figure-2   perature and the pressure of the pipeline.  tion of heavy deposit.
 to 80°C.  vity scale. They are light crude, medium  shows the  appearance  of a typical
 crude and heavy crude. Specifi c gravity  ‘Mesa-corrosion’ at 6 o’clock position in   H S or sour corrosion  If unfamiliar with MIC, corrosion
        2
 In the case of a dual-layer polyvinyl  and API gravity evolve in opposite  a crude oil pipeline. Another example   H S  in crude oil comes from the   problems may be misdiagnosed as con-
           2
 chloride (PVC)-PE system, the PVC  directions.  Therefore, the smaller the  of Mesa attack in internal surface of a   reservoir or  wells.  The deterioration   ventional chloride-induced corrosion
 layer can fail due to its brittle nature  API number, the heavier the fl uid.  crude oil pipeline is shown in Figure-3.  of metal due to contact with H S and   or CO  corrosion. One prominent
                                 2
                                                                                2
 as it loses its plasticizer due to aging.   moisture is called sour corrosion, which   Fig. 5: Cross section of a carbon steel pipeline   indicator of  MIC  is  a higher rate of
 Disbondment from the steel surface can   There  are several  causes of corro-  is  the most  damaging to drill pipes.   from petroleum process stream showing  a   attack than one would generally expect.
 start early in such cases due to the loss  sion in crude oil pipelines(2, 3).  Although H S is not corrosive by itself, it   large hydrogen blister  MIC is affected presence or activity (or
                2
 of adhesive strength.   becomes a severely corrosive agent in  ing a large hydrogen blister due to pres-  both) of microorganisms in biofi lms on
 CO  or sweet corrosion  the presence of water, leading to pipe-  ence of H S in the process stream. In  the corroding material’s surface. Many
                                                 2
 2
 Even the PE with butyl rubber dual-  This is a type of corrosion that   line embrittlement (loss of toughness).  fact, the hydrogen blister took place on  materials, including  most  metals and
 layer coating can fail due to the loss of  typically occurs in pipelines when   the surface where H S penetrated.    some non-metals,  can be degraded in
                                                         2
 adhesive  in  the  carrier  fi lm,  and  dis-  dissolved CO  gases in the crude oil   When dissolved in water,  H S   this manner. MIC can result from the
 2
                                    2
 bondment can begin gradually.  react with water to form carbonic acid.   Fig. 2: The appearance of a typical ‘Mesa-  tends to form a weak acid. As such, it   There are some key ways to mini-  activities of  the  microorganisms,
 This eventually corrodes the internal   corrosion’ at 6 o’clock position in a crude oil   is a source of hydrogen ions and is cor-  mize H S corrosion damage  in  pipe-  including bacteria, Archaea, and fungi
                                               2
 Field coating vs. factory-produced   surface  of  the  pipe.  CO   corrosion   pipeline.  rosive. The corrosion products are iron  lines. They include:  in  biofi lms,  or  the  local  environment
 2
 coating  increases in the presence of both oxygen   sulphides and hydrogen. Iron sulphides  1.  Use normalized electric resistance  directly connected with the corrod-
 Factory coatings are produced  and organic acids, which can dissolve   form a scale that, at low temperature,   welding (ERW) line pipe that  ing material. Depending on  the  envi-
 under standard conditions and automatic  iron carbonate scale and prevent further   can act as a barrier to slow corrosion.   meets the industrial steel selection  ronment,  these microbes  may include
 controls to ensure a high degree of  scaling. When CO  is present, there are   The forms of sour corrosion are uni-  code requirements.  metal-oxidizing bacteria, sulphate-
 2
 reliability. However, if a coating has  various types of corrosion mechanisms   form, pitting and stepwise cracking(8, 9).  2.  Conduct periodic pigging of pipe-  reducing bacteria  (SRB), prokaryotes
 to be applied on site, the surface pre-  that could take place. The main ones are   line segments to remove liquids,  (SRP), acid-producing  bacteria  (APB)
 paration, coating, curing and other steps  pitting corrosion, uniform corrosion,   The  appearance of corrosion  dam-  solids and debris.  and metal-reducing bacteria (MRB).
 involved need skilled manpower,  ins-  wormhole attack, ringworm corrosion,   age  from sour corrosion is usually  3.  Periodically apply a batch cor-
 pection, equipment and site super-  erosion corrosion and mesa attack(6).   general thinning. However, localized   rosion inhibitor  to provide  a pro-  Damage is often characterized by
 vision. Some amount of coating for joints  A typical sweet corrosion/CO  pitting   Fig. 3: Mesa attack in internal surface of a   corrosion or localized  under-deposit   tective barrier on the inside surface  cup-shaped pits within pits (halo effect)
 2
 Crude Oil pipeline
 and repair work may have to be done at  attack in a crude oil pipeline is depicted   attack can occur when air or oxygen is   of the pipe(10, 11).  in carbon steel or sub-surface cavi-
 the worksite. The reliability of the sys-  in Figure-1.  CO  corrosion damage related  to   present.  ties in stainless  steel. However,  these
 2
 tem in such cases would depend on the   fl uid fl ow is primarily associated with   Microbiologically induced corrosion   pits are  often indistinguishable from
 quality of work done at the site, which   the separation and accumulation  of a   Depending on the type of corrosion  (MIC)  under-deposit corrosion in carbon steel
 acts as the weakest link in the system.   water phase.  Therefore, longitudinal   mechanism, it can be found in various   MIC in itself is not a unique corro-  and chloride pitting in stainless steel.
 The storage of coating material on site,   corrosion grooving (6 o’clock corro-  locations in the pipelines. A typical fail-  sion mechanism; instead, it produces  Therefore,  pit morphology alone may
 under adverse conditions, is also very   sion) is the primary concern in stratifi ed   ure (sour corrosion) of a pipeline carry-  conditions that increase the susceptibi-  not be a reliable indicator of the cause
 challenging.  Taking care of  environ-  gas/liquid fl ow wet gas pipelines(6, 7).  ing crude oil containing H S is shown  lity of materials to corrosion process-  of MIC corrosion.
                            2
 mental  health  & safety (EH&S) con-  in Figure-4. Similarly, Figure-5 shows  es such as pitting, embrittlement and
 cerns on site needs adequate planning.  CO  corrosion predominantly occurs   cross section of a carbon steel pipeline  under deposit corrosion (UDC). Figure-6   Figure-7  shows  Pitting  corro-
 2
 at surfaces freely exposed to the   from petroleum process stream show-  shows MIC induced corrosion in pipe-  sion found in an internal sour crude
 Oil pipelines  corrosive environment, for example
 shielded areas such as narrow crevice
 Fig. 1: Pitting due to sweet corrosion/CO
 Crude oils are a highly complex   attack in a crude oil pipeline  2  arcs are not attacked even though they
 combination  of hydrocarbons, hetero-  may be wetted by the fl uid. Corrosion
 cyclic compounds of nitrogen, oxygen,   CO  corrosion of steels usually  may occur along the bottom surface of
 2
 sulphur,  organo-metallic compounds,  occurs as shallow pits and grooves, which  a pipe if there is a separate water phase
 inorganic  sediment,  and water. More  sometimes overlap.  While some sur-  or along the top surface of a pipe if con-
 than  600 different  hydrocarbons have  faces may remain unaffected, the cor-  densation in wet gas systems occurs.
 been positively identifi ed in crude oil,  rosion is often remarkably uniform in
 and possibly thousands of compounds  the attacked areas, leading to so-called   CO  corrosion damage is mitigated   Fig. 7: Pitting corrosion found in an internal
 2
 occur, many of which will never be  “mesa-corrosion,”  a characteristic  of  by use of effective pigging and chemi-  Fig. 4: Oil and Gas pipeline under sour   Fig. 6: A pipeline used in an oil & gas industry   sour crude oil pipeline indicating the halo
 identifi ed.  CO  corrosion. In carbon  steels,  loca-  cal inhibition programmes and control   corrosion  attacked by MIC corrosion  effect.
 2

 190  Chemical Weekly  December 12, 2023  Chemical Weekly  December 12, 2023                           191


                                      Contents    Index to Advertisers    Index to Products Advertised
   186   187   188   189   190   191   192   193   194   195   196