export@ezsteelpipe.com
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A practical, side-by-side walkthrough of 90/10 vs 70/30 copper nickel grades, the standards that actually matter on a real RFQ, and the coordinated pipe flanges, industrial valves, and gasket stud bolt nut set that turns a tube-only order into a pressure boundary you can actually bolt up on site.
For shipboard cooling water, offshore platform fire-fighting mains, ballast and bilge lines, refinery overhead condensers, and power-plant auxiliary circuits, copper nickel alloy remains the default material where long service life matters more than first cost. The 90/10 and 70/30 grades both develop a thin, adherent, self-healing surface film in seawater that resists biofouling, impingement attack and stress-corrosion cracking in a way that carbon steel and even standard austenitic stainless struggle to match in real, dirty service water. That film is the entire reason the alloy has stayed in naval and offshore specifications for more than half a century, and it is also the reason that a CuNi line, once specified correctly, tends to be quietly forgotten by the maintenance team for the next twenty years.
The catch is that specifying the tube is only the front of the problem. On most real projects, a CuNi line has to terminate in a CuNi flange, sit behind an isolation or check valve, and live inside a bolted joint that includes the right gasket and the right stud bolt and nut. Treating the line as "just tube" is where most procurement teams lose both money and schedule — and where most receiving-inspection rejections actually start.
The 90/10 grade (UNS C70600, CuNi10Fe1Mn) is the workhorse for shipboard and offshore cooling water, sanitary and fire-fighting systems, and the majority of power plant auxiliary circuits. It combines good seawater resistance, reliable weldability, and reasonable cost, and it is the default referenced in EEMUA 234, BS 2871, the corresponding ASTM B466 / B111 specifications, and most GB/T grades used by Chinese shipyards.
The 70/30 grade (UNS C71500, CuNi30Fe1Mn) is reserved for higher temperatures, higher velocities and more aggressive chemistry — desalination brine heaters, certain refinery overhead condensers, and high-temperature heat exchanger bundles. It tolerates higher flow rates before the onset of impingement attack and holds mechanical strength better at elevated temperature. If a line is genuinely 70/30 service, do not substitute 90/10 to save material cost; the operating cost of a leak in a refinery condenser will dwarf the saving within a single turnaround.
Quick rule of thumb
Seawater cooling at moderate temperature and velocity → 90/10. Higher temperature, higher velocity, or more aggressive brine chemistry → 70/30. When in doubt, ask the operating team for the maximum sustained design temperature and velocity, not the nominal number on the data sheet.
A serious CuNi procurement document references more than one standard, and the references must agree. For seamless and welded pipe and tube, the baseline is ASTM B466 / B467 (pipe) and ASTM B111 / B395 (tube for condensers and heat exchangers). For marine applications, EEMUA 234 is the de-facto reference in Europe, while naval and shipbuilding work typically layers in GB/T, DIN or BS grades depending on the yard. For nuclear and aerospace-adjacent service, RCC-M II and ASTM B407 / B163 (Inconel / Monel families) come into the picture, and the same logic of full material traceability and ASME IX welding qualification applies.
A common RFQ mistake is to write "CuNi 90/10 to ASTM" without specifying seamless vs welded, temper (annealed vs as-welded), dimensional standard (ASME B36.19 vs EN ISO 1127) and the test package (hydrostatic, eddy current, PMI, hardness). Each of these items changes price and lead time, and most rejections at incoming inspection trace back to one of them being left implicit in the line item.
CuNi is weldable, but it is not forgiving. The right filler metal is a CuNi 30 (for 90/10 base) or a matched 70/30 filler — for example AWS A5.7M ERCuNi — not a generic bronze rod. Preheat and interpass control matter; gas shielding on the root side matters even more, because a single back-side oxidation layer is enough to start a crevice-corrosion site that will not show up until hydrotest or first commissioning. For tube and pipe in the 4–10 mm wall range, the practical envelope is interpass temperature at or below 150 °C and a heat input not exceeding roughly 2.0 kJ/mm, with short arc length, 99.99% argon backing, and an oxygen monitor on the purge side reading well below 0.1% before the arc starts.
Shop welding is strongly preferred over field welding for the pressure boundary. Field welds should be limited to the joints that genuinely have to be made on site, and those welds should be radiographed or at least dye-penetrant tested before commissioning. For shop-fabricated spool pieces, the supporting documentation — weld map, WPS, welder qualifications, and the MTR set for base metal and filler — should be delivered as one package, not as loose PDFs. The same logic applies to the pipe flanges and the gasket / stud bolt set: one heat-number story, one traceability document, one acceptance certificate.
A CuNi line does not live alone. On a typical seawater cooling train you also need: CuNi flanges (commonly to ASME B16.5 / B16.47 or the European equivalent), spiral-wound or RTJ gaskets matched to the flange class, stud bolts and nuts in the correct material (B7 / B8 / B8M / B16 depending on service), and the upstream and downstream industrial valves — usually a butterfly or ball for isolation and a check valve for pump protection.
Procurement teams that buy these items from five separate suppliers consistently end up with mismatched facing (RF vs FF), mismatched bolt circle, and bolts that are "almost the right length". The fix is to bundle. Treating the line as a single coordinated pressure-boundary package — CuNi tube, copper nickel alloy flanges, gasket, stud bolt and nut, and valve set — lets the specifier lock heat-number traceability, MTR packaging, and delivery timing onto a single project docket.
In marine service — shipbuilding, offshore platforms, coastal refineries — three failure modes dominate CuNi lines: impingement attack at bends, tees and pump discharge; galvanic corrosion at the transition to steel or stainless components; and biofouling where velocity is too low to keep the surface film clean. The right fix for each is not "more alloy":
For impingement attack, stay within the velocity limits in EEMUA 234, and on long runs consider welded CuNi bends with the correct heat-affected zone treatment rather than repeatedly welded mitre joints. For galvanic corrosion, isolate the CuNi flange from the steel flange with a proper gasket and insulating kit, and use CuNi flanges with the correct facing and bolt pattern on the CuNi side, not a carbon steel flange adapted after the fact. For biofouling, the answer is system design — chlorination, flow management, periodic pigging — not material substitution.
In refinery and petrochemical service, the CuNi grade is chosen against the actual chemistry, not the generic label. In overhead condensers and sour-water stripper preheaters, 70/30 is common; in lean amine and caustic service, plain carbon steel sometimes still wins on cost. Heat-exchanger tubes are typically ordered to ASTM B111 with a defined temper and a defined surface finish; the wrong surface finish is the single most common reason for early tube-side fouling in refinery bundles.
If a bundle is being retubed, this is also the moment to review the tube support sheets, the header design, and the inlet box — and to ask whether the existing valve arrangement on the channel is actually adequate for the new operating window. A retube that ignores the industrial valves on the water side usually means the next turnaround comes earlier than the planned five-year interval.
Before issuing the purchase order for a CuNi line, confirm: (1) the grade and standard are written explicitly in the line item, not implied by "CuNi"; (2) the test package matches the standard and is listed in the PO, not in a separate email; (3) the flange type, facing, class and bolt pattern are explicit, and match the mating valve or equipment; (4) the gasket and stud-bolt material match the flange class and the operating temperature; (5) the valve body, seat and trim are specified for the actual fluid (seawater vs hydrocarbon), not for a generic "industrial" label; (6) MTR and traceability requirements are listed, including the requirement that the mill certificate is delivered before shipment, not after.
If any one of these is left to "as standard", expect at least one clarifications round, one schedule slip, and one deviation report at the receiving warehouse.
Sourcing the CuNi tube, the flanges, the gaskets and stud bolts, and the valves from a single integrated supplier does not just remove paperwork. It removes the most common class of project failure: the pressure-boundary stack that looks correct on paper but does not actually bolt together on site, or that arrives with mismatched certifications. EZ Steel Industrial has been producing CuNi tube, pipe, flanges and fittings since 1994 to ASTM, EN, GB/T and EEMUA standards, with full-cycle control from melt to finished spool, and can ship the matching valve and gasket package on the same MTR set.
For shipbuilding, offshore, refinery and power-plant projects, the right question is rarely "what alloy should I use" — it is "how do I make sure every joint on the CuNi line is from the same spec, with the same paper trail, and lands on the same dock at the same time". A bundled CuNi package answers that.
Send your CuNi line list — grade, size, length, flange class, valve schedule — to export@ezsteelpipe.com and we will return a bundled quotation with the tube, flanges, gaskets, stud bolts and valves on a single MTR package, with EEMUA 234 / ASTM B466 references written into the line items, not buried in the small print.
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