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Metals Galvanic Series Seawater

Reference data and engineering information about metals galvanic series seawater for material properties applications.

metalsgalvanicseriesseawater

Overview

Engineering reference data for Metals Galvanic Series Seawater in material science and properties.

Key Formulas

Stress

σ=FA\sigma = \frac{F}{A}

Force per unit area.

Strain

ε=ΔLL0\varepsilon = \frac{\Delta L}{L_0}

Change in length per original length.

Hooke's Law

σ=Eε\sigma = E \varepsilon

Stress proportional to strain in elastic region.

Thermal Expansion

ΔL=αL0ΔT\Delta L = \alpha L_0 \Delta T

Length change due to temperature.

Variables

SymbolDescriptionUnit
σ\sigmaStressPa
ε\varepsilonStrain
EEYoung's modulusPa
α\alphaThermal expansion coefficient1/°C
ΔT\Delta TTemperature change°C

Galvanic Series in Seawater

The galvanic series ranks metals and alloys by their electrochemical potential in seawater at 25°C (77°F). Materials at the top are more cathodic (noble), while those at the bottom are more anodic (active). When two metals are coupled in seawater, the anodic material will corrode preferentially.

Electrochemical Potential Ranges

The potential difference (ΔE\Delta E) between two materials predicts galvanic corrosion severity:

ΔE=EcathodeEanode\Delta E = E_{\text{cathode}} - E_{\text{anode}}

Where:

  • EcathodeE_{\text{cathode}} = potential of the more noble metal (V vs SCE)
  • EanodeE_{\text{anode}} = potential of the more active metal (V vs SCE)
28 rows
Galvanic series of metals and alloys in flowing seawater at 25°C (77°F). Potentials shown vs. saturated calomel electrode (SCE).
Material
Potential Range(V vs SCE)
Classification
Platinum+0.20 to +0.30Noble
Gold+0.20 to +0.30Noble
Graphite+0.20 to +0.30Noble
Titanium-0.05 to +0.10Noble
Silver+0.08 to +0.15Noble
HASTELLOY® C-0.05 to +0.10Noble
INCONEL® 625-0.05 to +0.10Noble
316 SS (passive)-0.05 to +0.05Noble
304 SS (passive)-0.10 to 0.00Noble
Monel 400-0.15 to -0.05Intermediate
Copper 90/10 Ni-0.20 to -0.10Intermediate
Red Brass (85% Cu)-0.25 to -0.15Intermediate
Yellow Brass (65% Cu)-0.30 to -0.20Intermediate
Naval Brass-0.35 to -0.25Intermediate
Tin-0.35 to -0.25Intermediate
Lead-0.50 to -0.40Intermediate
316 SS (active)-0.50 to -0.35Active
304 SS (active)-0.55 to -0.40Active
410 SS (active)-0.55 to -0.40Active
Cast Iron-0.65 to -0.50Active
Wrought Iron-0.65 to -0.50Active
Low Carbon Steel-0.65 to -0.50Active
Aluminum 2024-0.75 to -0.60Active
Cadmium-0.80 to -0.70Active
Aluminum 1100-0.80 to -0.65Active
Galvanized Steel-1.05 to -0.90Very Active
Zinc-1.05 to -0.90Very Active
Magnesium Alloys-1.70 to -1.50Very Active

Source: engineeringtoolbox.com

Galvanic Corrosion Risk Guidelines

Potential Difference ΔE\Delta ECorrosion Risk
< 0.15 VLow
0.15 – 0.25 VModerate
0.25 – 0.50 VHigh
> 0.50 VSevere

Practical Considerations

Passive vs. Active States: Stainless steels exhibit dramatically different potentials depending on their surface condition. In the passive state (protective oxide layer intact), they behave as noble materials. In the active state (oxide layer compromised), they shift significantly anodic and may corrode rapidly.

Area Ratio Effect: The galvanic corrosion rate is amplified when a small anode is coupled to a large cathode. The current density on the anode increases, accelerating localized attack:

ianodeicathode=AcathodeAanode\frac{i_{\text{anode}}}{i_{\text{cathode}}} = \frac{A_{\text{cathode}}}{A_{\text{anode}}}

Where ii is current density and AA is exposed surface area.

Environmental Factors: Temperature, salinity, flow velocity, and dissolved oxygen content can shift potentials significantly from laboratory values. Always consider site-specific conditions when selecting materials.

References