Stainless steel in seawater is the material decision that catches out more people than any other on a vessel. The confusion is understandable, because 316 genuinely performs well in fast-moving aerated seawater and the published corrosion rates look excellent. What those figures do not describe is what happens the moment the pump stops. Chlorides concentrate in any crevice, oxygen is consumed and not replaced, the passive film cannot repair itself locally, and the attack becomes autocatalytic and fast.
The mechanism is worth understanding because it explains the pattern of failure. Pitting starts under a deposit, a gasket edge, a scale flake or the tiny annular gap where a tube enters a tubesheet. Inside that shielded volume the chemistry turns acidic and aggressive while the metal a millimetre away stays bright and apparently perfect. The result is a pinhole through a wall that shows no general thinning at all, which is why a stainless tube can leak while looking new.
So we do not build raw seawater tube bundles in 316. For tube service in seawater the answer is copper-nickel, which resists chloride by growing a different kind of film that does not depend on flow, or titanium, which is simply immune. 316 remains a perfectly sensible material elsewhere on the same cooler: shells and tubesheets on the HC frames, closed fresh water and glycol circuits, and duty where the fluid moves continuously and is not chloride-bearing.
Stainless steel in seawater is protected by moving oxygenated water, and every vessel shuts down, so the design condition is stagnation.
| CONDITION | 316 BEHAVIOUR | COPPER-NICKEL | TITANIUM |
| Flowing aerated seawater | Good | Good | Immune |
| Stagnant seawater | Pits and perforates | Fair with anodes | Immune |
| Under deposits or scale | Crevice attack | Slowed but resistant | Immune |
| Warm chloride water | Pitting risk rises sharply | Use 70/30 grade | Immune |
| Closed glycol loop | Excellent | Unnecessary | Unnecessary |
Stainless steel is not inherently unreactive. It is protected by a very thin chromium oxide layer that repairs itself when damaged, and repair needs dissolved oxygen at the metal surface. In moving aerated water that supply is continuous and the film keeps up with chloride attack easily.
Shield a patch of surface under a deposit and the local oxygen is used up. The film cannot repair, chloride migrates in, the trapped solution acidifies, and metal dissolution accelerates because the corrosion products themselves make the environment more aggressive. That self-reinforcing loop is why stainless pitting is fast once it starts, in contrast to the slow general attack people expect from corrosion.
Industrial seawater plant often runs continuously, and stainless can be made to work there with care. A vessel does not. It runs for hours, then sits for days or months with the seawater circuit full and still, warm from the machinery space, with whatever silt and organic matter came in through the strainer settling onto the tube bores.
That is the worst possible condition for 316 and a survivable one for copper-nickel with maintained zinc anodes. It is also why a stainless cooler can pass a sea trial, complete a season, and then leak during recommissioning after winter layup. The failure was set up during the idle period, not during operation.
On the HC Series the shell can be steel or 316, the tubesheet steel or 316, and the bonnets cast iron, bronze or 316. Because we always put seawater on the tube side, the shell and its internals see engine coolant or oil, and there 316 is a strong material with real advantages in strength and cleanliness.
316 is also the sensible choice on closed fresh water and glycol circuits, on brackets and fasteners in the machinery space, and on any duty where flow is continuous and chlorides are absent. The rule to remember is not that stainless is bad but that stainless plus still seawater is bad.
The published performance assumes flowing aerated water, which keeps the passive film repaired. Marine service does not provide that. Once flow stops, oxygen under deposits is consumed, chlorides concentrate, and localised pitting or crevice attack proceeds quickly. The alloy is not defective; the service condition is different from the test condition.
Higher alloyed grades resist chlorides considerably better than 316, but they carry cost close to the point where titanium becomes the sensible comparison, and they still foul biologically. For marine cooler tubes we specify copper-nickel or titanium and use 316 for shells, tubesheets and closed circuits.
Cathodic protection helps, but it does not reliably stop crevice attack in shielded volumes where the protecting current cannot reach, which is precisely where stainless fails. Anodes are essential on copper alloy coolers because they protect accessible surfaces and tube-end joints. They are not a substitute for choosing the right tube alloy.
Because the damage was done while it sat. Seawater left standing under fouling deposits creates the low-oxygen high-chloride pocket that drives pitting, and months of that will put a pinhole through a tube that looked perfect at haul-out. Flushing with fresh water and draining before layup makes a large difference.
On the shell side and the structure. Because we always run seawater through the tubes, 316 shells and tubesheets on the HC frames see engine coolant or oil and perform excellently there. It is also correct for closed glycol loops, brackets and fasteners. The seawater passages get copper-nickel or titanium.
Frames offering 316 shells with copper-nickel or titanium tubes
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How stainless behaves when coupled to bronze and steel
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Intermittent duty and long idle periods on pleasure hulls
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