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On a ship, in a coastal power station, or on an offshore platform, the tubing that touches seawater has to do two things at once: resist corrosion for the full docking interval, and keep the heat exchanger running at the rated duty. Copper-nickel alloy tubes are still the most predictable answer to that brief. This article is a practical walk-through of how they are specified, fabricated, and proved, so the next bundle you install does not come back early from the dry dock.
The seawater side of a heat exchanger is unforgiving. Chloride ions pit unprotected stainless steel, galvanic couples eat aluminium within a season, and titanium costs more than the rest of the bundle combined. Copper nickel alloy sits in a narrow band of materials that form a stable, self-healing surface film in aerated seawater. The 90/10 grade (UNS C70600) is the workhorse for shipboard piping, condensers, and coolers; the 70/30 grade (UNS C71500) takes over when the water is warmer, faster, or carries more suspended solids.
In practical terms, the difference is roughly 10% nickel versus 30% nickel. The extra nickel tightens the protective oxide layer and pushes the threshold velocity up, so 70/30 is preferred for high-velocity service, fire-water mains, and oil-platform cooling where the consequence of a leak is severe. 90/10 covers the great majority of merchant-ship and onshore-plant duty, which is why it is the grade most buyers see on the quotation.
A copper-nickel tube order travels through three specification layers. Skip any one of them and a class surveyor will reject the delivery. They are, in order of authority:
The trick is that the mill and the buyer must agree on which document governs in case of conflict. The mill will default to the material standard; the buyer often intends the classification rule to be binding. A clean RFQ names all three and explicitly states the hierarchy.
Most seawater-cooled exchangers run the tube at 1–3 m/s. Past about 3.5 m/s, even 90/10 begins to suffer from erosion–corrosion, and the surveyor will want the velocity proven by calculation. Two numbers worth memorising: 90/10 is comfortable up to about 3.5 m/s in clean seawater; 70/30 is comfortable to about 4.5 m/s and tolerates a higher silt load. Below 0.5 m/s, biofouling starts to dominate and the heat-exchanger maintenance interval shortens regardless of which alloy you choose.
| Alloy | UNS | Typical duty | Velocity ceiling |
|---|---|---|---|
| 90/10 Cu-Ni | C70600 | Ship condensers, coastal coolers, fire mains | ~3.5 m/s clean seawater |
| 70/30 Cu-Ni | C71500 | High-temperature condensers, oil-platform cooling | ~4.5 m/s, tolerates silt |
| Monel 400 | N04400 | HF acid, hydrofluoric alkylation, marine shafts | Use where stainless would fail under chloride |
| Inconel 600 / 690 | N06600 / N06690 | Steam generators, nuclear PWR auxiliary lines | Selected for high temperature + chloride |
A 90/10 tube that meets ASTM B466 with full B466 EN 10204 3.1 certification is, in survey terms, an easy acceptance. A 70/30 tube delivered to B543 with the same paperwork is, in most projects, a one-day review. The slip-ups happen when a mill ships a copper-nickel heat-exchanger tube to ASTM B543 but the surveyor was actually looking for B552, or vice versa. They sound similar and are not interchangeable for class survey.
Copper nickel alloy welds well, but only with the right filler. The default is a 65% Cu – 30% Ni – 2% Fe – 2% Mn rod (AWS A5.7 ERCuNi) for 90/10 base metal, and a 70/30 filler for 70/30 base metal. A small iron content in the filler is essential — it is what stabilises the protective oxide film in the weld zone. Iron-free filler is a frequent cause of accelerated attack right next to the weld.
Back purging with argon is non-negotiable for tube-to-tubesheet joints. Even a 1% oxygen contamination inside the tube during the root pass leaves an oxide layer that pitts in service. So is preheat control: copper-nickel has high thermal conductivity, so the heat you put in walks away fast. A 60–80 °C preheat is the practical minimum on heavy wall, and an interpass cap around 150 °C protects against hot cracking.
For the connections outside the bundle, the alloy must transition to something that can be flanged to the shell piping. Pipe fittings in matching 90/10 or 70/30, or a bronze/gunmetal transition fitting, keep the galvanic series continuous. A stainless stub end bolted between two copper-nickel flanges is a familiar source of through-wall pitting on the copper-nickel side within three years.
A seawater-cooled bundle does not live alone. The inlet and outlet nozzles, the vent and drain, the bypass line, and the isolation industrial valves all share the same corrosion environment. A practical procurement approach treats the bundle and its connectors as one package, with one material-traceable chain from the tube to the last flange bolt.
For the flange side, two formats dominate. Pipe flanges in copper-nickel per EEMUA 234 (typically supplied as a weld-neck flange with a Cu-Ni bore and a steel or aluminium-bronze hub) handle the seawater side. On the freshwater or process side, steel flanges in ASTM A105 or A182 F316L are the standard pick. The bolt material is the next decision: B7 studs with B7 nuts in the freshwater side, B8M or B8 class 2 stainless (often with PTFE or Xylan-coated threads) where galvanic conditions demand it.
Valves deserve a separate line item. The most common failure mode on a seawater circuit is the valve body — not the tube. A ductile-iron butterfly valve on a copper-nickel line can eat itself in two dry-dock intervals. A bronze-body, aluminium-bronze disc, rubber-seated valve on the same line will still be serviceable at the third. Match the valve metallurgy to the tube metallurgy, and the next survey becomes a one-day walk-through instead of a six-week procurement.
Not every tube in a marine plant is copper-nickel. The freshwater side of a condenser, the lube-oil cooler, the HVAC chilled-water loop, and the bilge / ballast treatment skid are all typically stainless steel pipe — usually 316L for the chilled-water and 304 for utility. The same material-traceability logic applies: EN 10204 3.1 or 3.2 certificate, ASTM A312 or A778 as the standard, and a PMI check at goods-in.
A practical rule: keep stainless and copper-nickel on opposite sides of any heat-exchanger partition, and transition in a single flanged joint. Mixing them inside a single bundle is rarely a good answer; the galvanic differences are large, and even with cathodic protection the cost of the protection system usually exceeds the cost of selecting the right alloy for each side in the first place.
Copper-nickel tubes fail surveys for three reasons, in roughly this order of frequency: incomplete documentation, dimensional non-conformance (especially ovality on small-diameter tubes), and surface defects that look like in-service corrosion but are actually mechanical damage from handling. The fix for all three is the same — a disciplined inspection regime before the bundle is boxed.
For nuclear-class or submarine work, add ultrasonic test for sub-surface defects, macro-etch on a sample from each lot, and a documented heat-treatment record. The mill should be able to show these documents in the language of the surveyor who will receive them.
Send these data points to the mill, and the first quotation will already be 80% accurate. The remaining 20% is the engineering conversation that turns a price into a delivery.
On a marine or offshore project, the documentation chain is the deliverable. A mill that produces the copper nickel alloy tube, the matching pipe fittings and flanges, the gaskets, the stud bolts, and the isolation industrial valves can keep the heat number, the chemical analysis, the test plan, and the shipping schedule coherent across all five line items. The buyer receives one certificate book, one point of contact, and one delivery — instead of three, five, and a long list of cross-references.
The other, less visible, benefit is the next dry dock. When the same supplier supplies the spare tube bundle that the operator orders two years later, the chemistry, the tolerances, and the documentation template are identical. The classification surveyor who accepted the first bundle will accept the second on the same data. That is a small saving on every survey, compounded over the life of a vessel or a power plant.
Copper-nickel is a thirty-year material, not a ten-year one. The bundles that work the longest are the ones specified with a clear view of the medium, a clean set of standards, and a documentation chain that the surveyor can sign off without a phone call. Pick the alloy by the duty, not by the catalogue. Pick the connectors from the same material family. Pick the mill that can hand you the whole package on one certificate.
If you are at the stage of comparing quotations, send the duty sheet, the velocity, the medium, the classification requirement, and the connector list. A good supplier will come back with an alloy, a tube geometry, a flange/valve bundle, and a documentation pack that lets the next survey pass without drama.
Send your duty sheet, velocity and medium to our engineering team. We supply copper nickel alloy tubes together with matching pipe flanges, pipe fittings, gaskets, stud bolts and industrial valves for ship, offshore and seawater-cooled power plant service, with full EN 10204 3.1 / 3.2 documentation and class-society-friendly shipping.
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