If you are specifying copper-nickel piping or tubing for a seawater system, you have probably faced this question: should I go with 90/10 (C70600) or step up to 70/30 (C71500)? The safe answer is always “70/30 — it’s better.” The smart answer depends on your actual service conditions.
Over-specifying to 70/30 when 90/10 would do the job means paying 30–50% more on material for no measurable gain in service life. Under-specifying to 90/10 in a high-velocity, high-temperature, or heavily polluted system means premature failure. This article breaks down the real performance differences between these two alloys so you can make a defensible, cost-effective decision.
The Core Difference: Nickel Content Drives Everything
Both alloys are copper-based, single-phase solid-solution alloys that cannot be hardened by heat treatment. They rely on a protective surface film — primarily cuprous oxide with incorporated iron and nickel — to resist corrosion in seawater.
The higher nickel content in 70/30 provides greater inherent strength and enhanced corrosion resistance, particularly in more aggressive conditions. But “more aggressive” is where the nuance lives.
Performance Comparison: Where Each Grade Actually Excels
Corrosion Resistance
A common assumption is that 70/30 is universally more corrosion-resistant. The data tells a more layered story.
In chlorinated seawater heat exchanger service, research found that 90/10 was globally more resistant to localized corrosion than 70/30 at both tested temperatures. The most corrosion-resistant configuration was 90/10 with internally finned geometry. However, when dissolved oxygen concentration drops below 6.6 ppm, 70/30 shows significantly higher corrosion resistance than 90/10. This means the advantage flips depending on water chemistry.
For general corrosion rates, both alloys stabilize at very low values — around 0.002 mm/year after the protective film matures, which typically takes up to three months. For most applications, both alloys will outlast the design life of the system.
Flow Velocity Limits
This is where the practical difference becomes concrete. Maximum safe flow velocities to avoid erosion-corrosion:
| Alloy | Piping (>80mm dia.) | Heat Exchanger Tubing |
|---|---|---|
| 90/10 CuNi | 3.0–3.5 m/s | 2.0–3.0 m/s |
| 70/30 CuNi | 3.5–4.0 m/s | 2.5–3.5 m/s |
Data from the Nickel Institute, based on CDA Publication 225.
The gap is roughly 0.5 m/s for piping and 0.5 m/s for tubing. For short-duration excursions (e.g., flushing, hydrotesting), velocities of 10–15 m/s are acceptable for both alloys. The velocity difference matters most in continuous-duty systems running near the upper limit — if your design flow is 3.3 m/s in piping, 90/10 is at the edge while 70/30 has margin.
Mechanical Strength
70/30 has higher inherent strength, though both alloys are typically supplied annealed and gain strength through cold working:
-
90/10 annealed: proof stress ~100–160 N/mm²; as-drawn ~345–485 N/mm²
-
70/30 annealed: higher than 90/10 but the exact values depend on temper and product form
For most piping and heat exchanger applications, the annealed strength of 90/10 is more than adequate. Higher strength becomes a factor only in high-pressure systems or where thinner wall thickness is needed to reduce weight.
Thermal Conductivity
90/10 has higher thermal conductivity than 70/30, which partly explains its greater popularity in heat exchanger and condenser service where heat transfer efficiency matters more than maximum strength. If your primary application is heat exchange, 90/10 is often the better technical choice for this reason alone.
Cost Reality Check
Current market pricing (as of 2025–2026):
| Alloy | Price Range (USD/kg) |
|---|---|
| Cu-Ni 90/10 (C70600) | $12–$18 |
| Cu-Ni 70/30 (C71500) | $18–$26 |
Source: NC Alloys price list, May 2025.
That is a 30–50% material cost premium for 70/30. For a typical 100-meter seawater piping run in 76.2mm seamless pipe, the price difference works out to roughly $2,000–$3,700 — real money that needs to be justified by actual service requirements.
When 90/10 Is the Right Choice
Choose 90/10 when all of the following apply:
-
Flow velocity stays below 3.0 m/s in piping and 2.0 m/s in tubing
-
Seawater temperature is moderate (below 30°C typical)
-
Water quality is clean or lightly chlorinated, with no significant sulfide contamination
-
Heat transfer efficiency is a priority (condensers, cooling systems)
-
Cost sensitivity is a factor and the system design life can be met with 90/10
90/10 is the workhorse grade for the majority of seawater piping, HVAC cooling, and condenser tubing applications. It has been the industry default for decades for good reason: it handles most conditions and costs significantly less.
When 70/30 Is Worth the Premium
Step up to 70/30 when any of these conditions exist:
-
Sustained flow velocities exceed 3.5 m/s in piping or 2.5 m/s in tubing
-
High seawater temperatures (above 35°C) accelerate corrosion and reduce the safe velocity threshold for 90/10
-
Polluted or sulfide-containing seawater is present, particularly in systems with frequent stagnation periods
-
Higher mechanical strength is needed for pressure containment or structural reasons
-
Dissolved oxygen is consistently low (below 6.6 ppm), where 70/30 outperforms 90/10
Naval and defense applications often specify 70/30 for these reasons, and DEF STAN 02-879 compliance is available for both grades in bar and tubular forms.
The Decision Framework: Three Questions
Instead of defaulting to 70/30, run through these three questions:
1. What is my actual maximum continuous flow velocity?
If it is below 3.0 m/s, 90/10 is likely sufficient. If you are designing at 3.5–4.0 m/s, 70/30 gives you the margin you need without resorting to a more exotic (and expensive) material like super duplex or titanium.
2. Is my seawater clean, or does it carry sulfides, pollutants, or entrained solids?
Clean seawater favors 90/10. Polluted or sulfide-containing water favors 70/30, especially during startup and shutdown cycles. Entrained sand reduces safe velocity by 1–1.5 m/s for both alloys, so account for that in your calculation.
3. What is the primary function — piping or heat transfer?
For heat exchanger tubing, 90/10’s higher thermal conductivity is a genuine advantage. For structural piping where erosion resistance matters most, 70/30’s higher velocity limit is the deciding factor.
What About Alternatives?
For context, it is worth knowing what you are not choosing:
Titanium offers three times the service life of Cu-Ni in some naval applications, but has historically cost significantly more. Recent manufacturing advances are narrowing that gap, and titanium’s weight advantage (74% weight reduction in some FPSO studies) can offset the higher material cost in weight-sensitive installations.
Super duplex stainless steel (PREN > 40) is the default for high-strength seawater components like pump casings and valve bodies, but it does not offer the natural anti-fouling properties of copper-nickel alloys. Biofouling resistance is a real operational advantage of Cu-Ni that is often overlooked during material selection.
Monel 400 costs roughly 1.5–2.5 times more than 90/10 and is only justified where high strength or acid resistance is required.
Practical Specification Tips
Regardless of which grade you choose, these practices determine whether you get the corrosion performance you are paying for:
-
Commission with clean, unpolluted seawater. The protective film forms during initial exposure. Filling with stagnant or polluted water can cause pitting that undermines long-term performance.
-
Maintain minimum flow velocities above 0.5–1 m/s during normal operation to prevent sediment deposition and sulfide generation from sulfate-reducing bacteria.
-
Control chlorination. Continuous residual chlorine should stay at 0.3 ppm (max 1 ppm); intermittent dosing at 0.5 ppm.
-
Avoid local turbulence. Weld bead protrusion and poorly aligned fittings create localized high-velocity zones that can initiate erosion-corrosion even when bulk flow is within limits.
The Bottom Line
90/10 copper-nickel is not a “cheaper substitute” for 70/30. It is a different alloy with different strengths. For the majority of seawater piping and heat exchanger applications — moderate velocities, clean water, heat transfer priority — 90/10 delivers the required service life at 30–50% lower material cost.
70/30 earns its premium when velocity margins are tight, water quality is poor, or mechanical strength requirements are elevated. The key is not to default to the “best” grade, but to match the grade to the actual service conditions.
If you are unsure which grade fits your project, the most reliable approach is to define your maximum flow velocity, seawater chemistry, and temperature profile first — then select the alloy that meets those specific requirements with an appropriate safety margin. That is engineering, not guesswork.
EN
AR
BG
HR
CS
DA
NL
FI
FR
DE
EL
HI
IT
JA
KO
NO
PL
PT
RO
RU
ES
SV
TL
VI
TH
TR
GA
CY
BE
IS