Module 4.6 — Erosion-corrosion in high-velocity, low-oxygen piping: why the very chemistry that protects against oxidizing corrosion enables FAC elsewhere.
Click the pipe geometry or the thinning zone to see FAC's mechanism. It concentrates at flow-disruption points where turbulence is highest.
Flow-accelerated corrosion was named in this course's very first planning discussion as one of the corrosion mechanisms Track 4 would eventually cover, described then as "erosion-corrosion in high-velocity, low-oxygen piping." That description turns out to be exactly right, and understanding why requires bringing together the magnetite protection concept from Module 1.1 with the flow and metallurgy concepts introduced across Tracks 2 and 3.
The protective magnetite layer, central to nearly every corrosion prevention strategy in this course, isn't perfectly insoluble — it has a small, genuine solubility in water, and that solubility increases somewhat under low-oxygen (reducing) conditions, which describes most feedwater and condensate piping running under AVT chemistry (Module 2.4). Under normal, low-velocity conditions, magnetite dissolves slowly and reforms roughly as fast as it dissolves, maintaining a stable protective layer. Under high-velocity, turbulent flow — particularly at geometric flow-disruption points like elbows, tees, reducers, and locations downstream of control valves or orifices — the magnetite layer can be physically and chemically stripped away faster than it can reform, exposing fresh metal to continued dissolution.
FAC risk is highest in a specific temperature window, commonly cited in the range of roughly 130 to 300°C (around 265 to 570°F), where magnetite solubility peaks under reducing conditions — outside that range, in either direction, the mechanism is markedly less active. High flow velocity compounds this by increasing the mechanical stripping force at the metal surface and increasing mass transfer rates that carry dissolved iron away faster, both of which accelerate net metal loss at susceptible locations.
Just as Module 4.1 explained that localized corrosion concentrates at points of anode/cathode differential, FAC concentrates at points of flow disruption — elbows (especially at the outer radius, where flow separation and turbulence are greatest), tees, reducers, and locations immediately downstream of orifices or partially closed valves. These are predictable, inspectable locations precisely because the mechanism is driven by geometry as much as by chemistry, which is why FAC inspection programs focus heavily on these specific component types rather than random piping sampling.