Advanced Power Plant Chemistry — Track 4

Oxygen Pitting

Module 4.2 — The corrosion mechanism behind Module 1.1's dissolved oxygen warnings, and why pitting is one of the most dangerous corrosion patterns despite low total metal loss.

PASS THRESHOLD 80% EST. TIME 20 MIN TRACK 4 / 7
≡ Course IndexModule 22 of 48 · Track 4 — Corrosion Mechanisms & Failure Analysis
Pit Anode:Cathode
1:1000+
area ratio, typical
Common Location
Idle/Standby
stagnant, oxygenated water
Appearance
Deep, Narrow
often tubercle-capped
TUBERCLE (Fe corrosion product cap) DEEP, NARROW PIT — ANODE SURROUNDING SURFACE = LARGE CATHODE large cathode area drives concentrated attack at small anode

Click any element to see its role in pit formation. The area mismatch between a tiny anode and a huge cathode is what drives such rapid, concentrated penetration.

Select an element to learn more.

Where This Connects Back

Module 1.1 established that dissolved oxygen is aggressive toward carbon steel and explained why deaeration and oxygen scavenging (Module 2.6) exist. This module explains the specific mechanism: oxygen pitting, one of the most classically destructive corrosion patterns in fossil plant systems, and a direct application of the anode/cathode framework from Module 4.1.

How a Pit Initiates

Pitting typically begins at a small, localized surface imperfection — a scratch, a break in a protective oxide film, a deposit, or a minor manufacturing defect — where dissolved oxygen can initiate localized attack. Once a tiny anode forms at that point, oxygen reduction on the vast surrounding surface (the cathode reaction from Module 4.1's electrochemistry) drives continued dissolution at the anode site specifically, rather than spreading the attack out. The reaction is self-reinforcing: metal dissolving at the pit releases iron ions, which react with water and available oxygen to form corrosion products that can cap the pit opening as a tubercle, creating a stagnant pocket underneath.

Why the Pit Environment Gets Worse, Not Better

Once a tubercle forms, the water trapped beneath it becomes isolated from the bulk system's normal chemistry. Metal dissolution inside the pit produces metal ions that hydrolyze, generating acidity locally — meaning the pit interior can become significantly more acidic than the bulk water, even on a well-controlled alkaline AVT or phosphate system. This local acidification accelerates further metal dissolution, and the tubercle cap can also restrict oxygen from re-entering the pit even as it protects the pit from beneficial bulk water chemistry — a genuinely self-sustaining, worsening local environment.

The area mismatch is the real danger: A pit anode might be a fraction of a square millimeter, while the surrounding cathodic surface supporting it could be square meters. All the electrochemical current the large cathode area can generate concentrates onto that tiny anode, driving metal loss rates at the pit far higher than any uniform corrosion rate calculation would suggest — this is precisely the localized-vs-general danger described in Module 4.1.

Where Oxygen Pitting Is Most Common

Why Lay-Up Practices Matter So Much

An operating unit under normal AVT or phosphate chemistry control, with functioning deaeration and scavenging, is relatively well protected against oxygen pitting. An idle unit is a different story entirely — no continuous flow, no active deaeration, and often no active chemical feed, while oxygen from air in-leakage or simply atmospheric contact can slowly saturate stagnant water. This is exactly why plants use lay-up procedures: either draining and drying equipment completely (dry lay-up) or filling with treated, oxygen-scavenged, alkaline water and maintaining it in a sealed, monitored condition (wet lay-up) during extended outages, specifically to prevent the stagnant, oxygenated conditions that invite pitting.

Field note: Oxygen pitting found during an inspection often traces back not to an operating chemistry failure but to an outage — equipment that sat wet, stagnant, and improperly protected between overhauls. Reviewing lay-up practices is frequently as important to pitting prevention as anything done while the unit is running.
Pitting
A localized corrosion pattern producing narrow, deep cavities rather than general surface thinning, driven by a small anode area supported by a much larger cathodic surface.
Tubercle
A mound of iron corrosion product that can form over a corrosion pit, trapping stagnant, oxygen-depleted, locally acidified water beneath it.
Local Acidification
A drop in pH occurring within a pit or crevice due to metal ion hydrolysis, distinct from and often far more severe than bulk water pH.
Anode:Cathode Area Ratio
The relative surface area of anodic versus cathodic sites in a corrosion cell; a small anode relative to a large cathode concentrates corrosion current and accelerates local metal loss.
Lay-Up (Dry)
An outage preservation method involving draining and thoroughly drying equipment to eliminate the water needed for corrosion.
Lay-Up (Wet)
An outage preservation method involving filling equipment with treated, oxygen-scavenged, alkaline water maintained in a sealed, monitored condition.
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