Tuesday, August 28, 2007
As discussed in earlier post <<Pitting Corrosion - Mechanism & Prevention>>, pitting corrosion is one of the most common localized corrosion attack and most destructive form of corrosion in metal and alloy. Out of so many type of alloy, how to differential the 
pitting resistivity of particular metal and alloy compare to the other ? Pitting Resistance Equivalent Number is used.
pitting resistivity of particular metal and alloy compare to the other ? Pitting Resistance Equivalent Number is used.Pitting Resistance Equivalent Number (PREN) is an index common used to measure and compare resistance level of a particular metal and alloy to pitting corrosion.
PREN can be calculated , using the alloy chemical composition, to estimate relative pitting resistance of metal and alloys.
Common equation for PREN calculation as followed :
PREN = %Cr + m.(%Mo) + n.(%N)
Per experiments, m range from 3.0 to 3.3 whilst n range from 12.8 to 30.
For ferritic grades Stainless Steel, the formula employed is :
PRE = % Cr + 3.3 (% Mo)
For austenitic grades Stainless Steel, the formula employed is :
PREN = %Cr + 3.3(%Mo) + 30(%N)
For duplex (austenitic-ferritic) grade Stainless Steel, the formula employed is :
PREN = %Cr + 3.3(%Mo) + 16(%N)
For high Ni-Cr-Mo alloys e.g. Inconel 625, Hastelloy, etc, the formula employed is :
PREN = %Cr + 1.5(%Mo + %W + %Nb)
where...
Cr - Chromium
Mo - Molybdenum
W - Tungsten
Nb - Niobium
Pitting is one of main problem for material expose to seawater. Minimum PREN required for material expose to seawater is 40. Duplex Stainless steel, Super duplex stainless steel, etc are exhibiting PREN > 40.
Related topics
Labels: Corrosion, Corrosion Resistance Material, Pitting
Friday, August 24, 2007
Pitting Corrosion on Metal Surface
Pitting is one of the most destructive forms of corrosion as it will potential cause equipment failures due to perforation / penetration. pitting generally occurs on metal surfaces protected by oxide film such as Stainless steel, aluminum, etc. Typically for boiler and feed water system, pitting corrosion rate increase dramatically with the increase of oxygen content in the fluid.
Pitting can occur in any metal surfaces. Following are some pictures of pitting corrosion.
Pitting corrosion on external pipe surface
Pitting corrosion on external pipe surface
H2S Pitting corrosion on internal pipe surface
Co2 Pitting corrosion on internal pipe surface
Lets look at figure below, oxygen rich fluid in contact with metal surface (at the top of the pit) will becomes the cathode. At the bottom of the pit, low in oxygen level becomes the anode. this will form a complete circuit where metal at the pit (FE) will be ionized to release electron (e) and form ion Ferum (FE2+), this electron will travel to the top of pit to react with Oxygen (O2) (and water, H2O) to form ion hydroxides (OH-). Ion Ferum (FE2+) will react with ion hydroxides (OH-) to form Ferum Oxide (Fe2O3) which typically a brown rust. Deeper the pit leeser the oxygen content and higher the potential and pitting corrosion rate.
Severity of pitting corrosion
Knowing that pitting can cause failure due to perforation while the total corrosion, as measured by weight lossm might be rather minimal, experience shown that rate of penetration may be 10 to 100 times that by general corrosion, pitting corrosion has been considered to be more dangerous than the uniform corrosion damage because it is very difficult to detect, predict and design against. General metal weight loss method almost impossible to detect the internal pitting corrosion.
Pitting corrosion shape
Pits formed due to pitting corrosion can become wide and shallow or narrow and deep which can rapidly perforate the wall thickness of a metal. Following picture demonstrate several types of pitting corrosion shape. This has made it even more difficult to be detected especially undercutting, subsuface and horizontal type.
Preventive measures
There are several preventive approah to avoid pitting. There are :
- Proper material selection e.g. SS316 with molydenum having higher pitting resistance compare to SS304
- Use higher alloys (ASTM G48) for increased resistance to pitting corrosion
- Control oxygen level by injecting oxygen scavenger in boiler water system
- Control pH, chloride concentration and temperature
- Cathodic protection and/or Anodic Protection
- Proper monitoring of oxygen & chloride contents by routine sampling
- Agitation of stagnant fluid
- Chloride stress corrosion cracking and use of correct MOC for seawater
- How Chloride stress corrosion cracking Lookslike ?
- Unified Numbering System for Metals and Alloys
Labels: Corrosion, Corrosion Resistance Material, Material, Pitting
