Heat Exchanger Tubes: GR1 Titanium vs Stainless Steel vs Copper Alloy

May 20, 2026

Material Full name Typical spec Corrosion resistance Cost
GR1 titanium Commercially pure titanium ASTM B338 Excellent in chlorides High
316L stainless steel Low carbon austenitic stainless ASTM A213 Moderate in chlorides Medium
C70600 90/10 copper-nickel ASTM B111 Good in seawater Medium

 

Corrosion Resistance Comparison

GR1 titanium: Excellent in seawater, brackish water, and chlorides. No pitting. No crevice corrosion. No stress corrosion cracking. Resists impingement attack at high velocities.

316L stainless steel: Prone to pitting and crevice corrosion in stagnant seawater or chlorides. Limited to about 50 degrees Celsius in chlorides. Risk of stress corrosion cracking.

C70600 (copper-nickel): Good in clean seawater. Susceptible to erosion at high velocities. Requires minimum flow to prevent sediment buildup. Pits in polluted or sulfidated seawater.

 

Environment GR1 316L C70600
Clean seawater, low velocity Excellent Acceptable Excellent
Seawater, high velocity Excellent Erosion risk Erosion risk
Stagnant seawater Excellent Pitting risk Pitting risk
Brackish water Excellent Pitting risk Acceptable
Chlorides at 60°C+ Excellent Failure risk Acceptable
Polluted seawater Excellent Pitting risk Corrosion risk

ASTM B338 grade 1

 

Mechanical Properties Comparison

Property GR1 316L C70600
Tensile strength (MPa) 240 485 275
Yield strength (MPa) 170 170 105
Elongation (%) 24 40 30
Hardness (HV) 120-200 150-200 80-110
Modulus (GPa) 105 193 135

 

GR1 has similar yield strength to 316L but lower modulus. Tubes deflect more under pressure.

316L is stiffer but work-hardens during bending.

C70600 is softer and has lower yield strength. Thicker walls may be needed.

 

Formability for U-Bends

U-bend tubes require ductility. The material must stretch on the outside of the bend and compress on the inside.

Material Elongation (%) U-bend capability Bend radius recommendation
GR1 24 Excellent 1.5 x OD
316L (annealed) 40 Excellent (annealed) 1.5 x OD
316L (hard) 20 Marginal 2.5 x OD
C70600 (annealed) 30 Excellent 2.0 x OD

 

GR1 bends easily. No cracking with proper bend radius. Weld seam (for welded tube) must be on neutral axis.

316L bends well in annealed condition. Work-hardens during bending. Must be solution annealed after bending to restore corrosion resistance.

C70600 bends well. Softer than GR1. Lower springback.

 

Heat Transfer Performance

Material Thermal conductivity (W/m·K) Relative to GR1
GR1 16 1.0x
316L 15 0.94x (slightly worse)
C70600 40 2.5x (much better)

 

C70600 transfers heat much better than titanium or stainless steel. Smaller heat exchangers for the same duty.

GR1 and 316L are similar. Titanium is slightly better than 316L.

 

Cost Comparison

Material Relative cost per kg Relative tube cost (installed)
GR1 High (1.8x to 2.5x 316L) High
316L Medium (baseline) Baseline
C70600 Medium (similar to 316L) Slightly higher than 316L

 

But cost per kg is not the full picture. Consider:

Wall thickness: C70600 may need thicker walls due to lower yield strength

Fabrication: 316L requires post-bend annealing. GR1 does not.

Life expectancy: GR1 lasts 20+ years. 316L may fail in 2 to 5 years in seawater.

Replacement cost: Retubing a heat exchanger is expensive.

 

Lifecycle cost comparison (example for seawater service):

Material Initial cost Life expectancy Replacement cost Total 20-year cost
GR1 High 20+ years None High (one time)
316L Medium 2-5 years High (multiple times) Very high
C70600 Medium 8-12 years High Medium to high

 

Fabrication Considerations

Welding:

Material Weldability Post-weld treatment
GR1 Good None
316L Good Solution anneal to restore corrosion resistance
C70600 Fair None (but filler metal must match)

 

Rolling into tubesheet:

GR1: Soft, work-hardens quickly. Use light passes.

316L: Harder. More force needed.

C70600: Soft. Easy to roll but easy to over-expand.

 

Bending:

GR1: No post-bend treatment needed.

316L: Post-bend solution anneal required for seawater service.

C70600: Stress relieve may be needed for tight bends.

 

Selection Guide

Choose GR1 titanium when:

Tube side is seawater, brackish water, or high chloride content

Stagnant or low flow conditions exist

High velocity (over 3 m/s) is expected

Temperature exceeds 50°C in chlorides

Tube will be U-bent to tight radius

Long life (20+ years) is required

Failure cannot be tolerated

 

Choose 316L stainless steel when:

Tube side is clean, low chloride water (under 200 ppm chlorides)

Temperature is below 50°C

Velocity is moderate (under 3 m/s)

No stagnant conditions exist

Lower initial cost is the priority

Regular replacement or maintenance is acceptable

 

Choose C70600 copper-nickel when:

Tube side is clean seawater

Velocity is controlled (2 to 3 m/s)

No polluted or sulfidated conditions

Higher thermal conductivity is needed to reduce exchanger size

Moderate life (8 to 12 years) is acceptable

 

FAQ

1. Is GR1 titanium worth the extra cost over 316L for seawater service?

Yes. 316L will likely fail within 2 to 5 years in seawater. GR1 lasts 20+ years. The replacement cost of a heat exchanger bundle is much higher than the initial material savings.

 

2. Can I use 316L for U-bend tubes in seawater?

Not recommended. U-bending work-hardens the stainless steel. The bend area is more susceptible to stress corrosion cracking in chlorides. Solution annealing after bending is required.

 

3. Is copper-nickel a good alternative to titanium?

For clean seawater at moderate velocities, yes. For polluted or stagnant conditions, no. Copper-nickel also has lower strength and may need thicker walls.

 

4. Why does GR1 titanium cost more than stainless steel?

Titanium is more expensive to produce. The sponge is costly. Melting and processing require specialized equipment. But the lifecycle cost in aggressive service favors titanium.

 

5. Does GR1 have better heat transfer than stainless steel?

Slightly. GR1 thermal conductivity is 16 W/m·K. 316L is 15 W/m·K. The difference is small. Copper-nickel is much better at 40 W/m·K.

 

6. Can I mix materials in the same heat exchanger?

Yes. Tubes can be one material. Tubesheet and shell can be another. But galvanic corrosion must be considered. Titanium tubes with a steel tubesheet require isolation.

 

7. What is the maximum temperature for GR1 in seawater?

GR1 is excellent up to 120°C in seawater. Above that, consult a corrosion engineer. 316L fails above 50°C in chlorides.

 

8. How does GR1 handle high velocity seawater?

Very well. GR1 can handle 5 to 7 meters per second in seawater. 316L is limited to 3 to 4 m/s. Copper-nickel is limited to 2 to 3 m/s.

 

9. Does GR1 require post-bend heat treatment?

No. GR1 does not work-harden significantly during bending. U-bend tubes can be used as bent. 316L requires solution annealing after bending.

 

10. Which material is easiest to roll into a tubesheet?

GR1 and C70600 are soft and roll easily. 316L is harder and requires more force. GR1 work-hardens quickly, so use light passes.

 

11. Can I use GR1 for fresh water cooling?

You can, but it is expensive overkill. 316L or copper alloys work fine in fresh water with low chlorides. Save titanium for aggressive service.

 

12. What about galvanic corrosion with titanium tubes?

Titanium is noble. It will not corrode. But it can cause galvanic corrosion on connected less noble metals like steel or copper. Use isolation or sacrificial anodes.

 

13. How do I know if I need GR1 or 316L?

Check your chloride level and temperature. If chlorides exceed 200 ppm and temperature exceeds 50°C, use GR1. If both are lower, 316L may work.

 

14. What is the life expectancy of GR1 vs 316L in seawater?

GR1: 20 to 30 years or more. 316L: 2 to 5 years before pitting or cracking appears. Copper-nickel: 8 to 12 years in clean seawater.