Stainless Steel World Americas October 2024 | Page 12

Technical Article

Understanding the Key Differences Between Pitting Corrosion and Crevice Corrosion

Identifying problems early empowers technicians to save facilities time and money while improving safety for everyone involved . By Buddy Damm , Senior Scientist , Swagelok Company
Metal components in industrial fluid systems often have to operate in harsh conditions . If left unchecked , adverse conditions can trigger and aggravate the corrosion of these components and cause physical and financial harm to an operation . In metal tubing , for example , the National Association of Corrosion Engineers ( NACE ) estimates the profit loss to offshore and nearshore operations from corrosion is more than $ 1 billion per year .
Recognizing corrosion early and addressing the root causes can help mitigate the worst damage , before repair and replacement costs accumulate . It is imperative that facilities ensure their technicians can identify the most common types of corrosion quickly , and understand what actions to take . Technicians can often take simple actions to remediate the damage if they know what to look for .
Two common types of corrosion are pitting and crevice , and they are normally responsible for the most expensive damage over time . Before determining how to fix the problem , it is important to understand why corrosion occurs , how pitting and crevice corrosion differ , and how to protect components from corrosion , to help avoid premature failures and costly replacements .
Corrosion is a set of electrochemical reactions that involve oxidation ( loss of electrons ) at an anode and a reduction ( gaining of electrons ) at a cathode ( Figure 1 ). For example , iron in tubing may oxidize , yielding two electrons and dissolving into water as a Fe 2 + ( positive ) ion . Simultaneously , the electrons from oxidizing iron may participate in a reduction reaction that uses O 2 dissolved in H 2 O to form OH-
( negative ) ions .
Anodic Oxidation : Fe ‣ Fe 2 + + 2e -
Cathodic Reduction : ½ O 2
+ H 2 O + 2e- ‣ 2 ( OH- )
Overall Corrosion Reaction : Fe + ½ O 2
+ H 2 O ‣ Fe 2 + + 2OH -
The most common applications for metal tubing are analytical and process instrumentation , hydraulic lines , and control and utility . These tubes are often made from stainless steel with more than 10 % chromium ( Cr ), which builds a passive oxide layer on the surface and inhibits corrosion ( Figure 2 ). Stainless steel corrosion does occur , however , when environmental conditions or mechanical damage causes that layer to break down . If the protective oxide cannot reform in a given solution ,
corrosion reactions may progress rapidly . In both pitting and crevice corrosion , the local breakdown of the passive oxide layer creates a region where corrosion damage is greatly accelerated .
How Pitting Corrosion and Crevice Corrosion Differ
The types of corrosion possible on oil and gas installations are myriad and depend on what component materials are used , the operating environment , and what fluids the components transport . However , two forms of corrosion are most common : pitting corrosion and crevice corrosion .
Pitting Corrosion - This type of corrosion occurs when the protective chromium-rich oxide layer on the surface of stainless steel breaks down , allowing the bare metal underneath to become susceptible to continued attack in a corrosive solution ( Figure 3 ). Cavities form as the stainless steel corrodes and creates pits .
Although the entry point of a pit may be detectable via thorough visual inspection , there may be a deep network of lost material lurking below the surface . Without appropriate remediation , pits continue to expand and can sometimes create holes in tubing walls . If process fluids leak out of these holes , it costs money in lost fluid , creates environmental and safety hazards , and can be expensive to fix . Additionally , pitting corrosion can cause cracks in already strained components . Environments with higher chloride ( Cl- ) concentrations , including those created by evaporation from deposited saltwater droplets , are likely to cause pitting corrosion – especially at high temperatures .
is reddish-brown iron oxide deposits and pits on the metal surface . Special attention ought to be paid to upward-facing surfaces where chlorine-bearing water ( e . g ., seawater ) may pool and evaporate , or downward-facing regions where hanging droplets dry . As water evaporates in these regions , the chlorine concentrations in the remaining water will increase and become more corrosive , resulting in pitting corrosion .
Crevice Corrosion - This type of corrosion is similar to pitting corrosion ; the protective oxide film on components deteriorates as it is exposed to corrosive fluids . The particularly insidious nature of crevice corrosion is that it frequently occurs out of sight , in crevices under clamps or similar tight spaces , making it hard to identify ( Figure 4 ). After crevice corrosion has started , wide and shallow pits form , weakening the component material and increasing the chances of mechanical failure .
In a typical fluid system , crevices exist between tubing and tube supports or clamps , between adjacent tubing runs , and underneath dirt and deposits that may have accumulated on surfaces . No matter how well the system is designed , crevices are practically inevitable , and the tighter they are , the harder they are to service . Catching crevice corrosion is far trickier than seeing pitting corrosion on the surface and , because it happens out of sight , it can quickly devastate systems .
In coastal or offshore applications , crevice corrosion often occurs when seawater diffuses into a crevice , leading to a chemically aggressive environment out of which corrosion-causing ions cannot readily dif-
The most obvious sign of pitting corrosion
Figure 1 . Corrosion occurs when a metal atom is oxidized by a corrosive fluid , which leads to a loss of material in the metal surface . It may appear in the form of general corrosion or rust on carbon steel , as well as pitting or crevice corrosion on stainless steel .
Why Stainless Steel Corrodes
All metals are liable to corrode when exposed to certain operating conditions , but proper planning and preventive maintenance can keep the damage to a minimum . Taking simple steps to halt corrosion before it spreads requires that technicians possess knowledge of how different types of corrosion occur , and which surfaces should be most frequently examined . Careful observation and remediation efforts can save time and money in the long run .
Figure 2 . In ambient air , stainless steels automatically form a passive , chromium-rich oxide layer on the surface that protects the material from corrosion ( top ). If that layer is damaged ( middle ), it will reform automatically ( bottom ). If the environmental conditions are severe , localized damage to the passive oxide layer can render the metal below susceptible to pitting or crevice corrosion .
Figure 3 . With localized pitting corrosion , electrochemical reactions initiate the formation of small cavities within the surface of stainless steel that can eventually grow deep enough to perforate a tube wall , or serve as stress concentration points where fatigue or stress-assisted corrosion can be accelerated .
Figure 4 . Localized crevice corrosion forms between a washer and plate under a bolt ( top ), or in tubing and tubing supports ( bottom ), with accelerated reactions taking place within the confines of the crevice .
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