Galvanic corrosion
Galvanic corrosion can cause severe damages in water and sewage installations

The use and combination of various metals in water and sewage installations can result in galvanic corrosion and very high corrosion rates. In this article, the authors present the general principles of galvanic corrosion with some case studies and solutions.

The standard approach to corrosion prevention is to use coatings and corrosion-resistant materials. These measures are usually satisfactory for the actual structure. It may, however, have an unfavourable effect on neighbouring structures.

At present, a wide variety of materials is available for water and waste water installations. However, combinations of these might, under certain conditions, lead to severely accelerated galvanic corrosion and cause damage within a short time. These effects are highly relevant for new buildings – and extensions or renovations to existing water installations in particular.

While the principal issues of galvanic corrosion are well understood, appropriate preventative measures are seldom adequately applied. In addition, the specific conditions and type of installation typically exercise a considerable influence on the corrosion rate.

The principle of corrosion

Corrosion is usually an electrochemical interaction between a metal and its environment, where the properties of the metal change and thus also its functionality, environment or technical system.

Electrochemical corrosion is mainly an anodic oxidation reaction, where the metal atom is dissolved as a positively charged ion while releasing electrons according to equation (1) and the cathodic oxygen reduction in equation (2):

  • Fe → Fe2+ + 2e-
  • O2 + 2 H2O + 4 e → 4 OH-

To satisfy the condition of electroneutrality, the number of electrons used for each reaction at any time must be equal. This relation is schematically depicted in Figure 1, where the size of the arrows represents the rate of the corresponding reaction. The anodic process is shown as red arrows, while blue arrows indicate the cathodic process.

On certain metals, formation of a protective layer of oxides can lead to passivity. In this case, the anodic corrosion process is decreased to a negligibly low level. An example of a passive metal in water systems is stainless steel.

Corrosion Figure 1
Figure 1: Electrochemical reactions occurring on the metal surface under different conditions

An electrochemical potential is established at the metal’s interface with an electrolyte (eg water). This ‘corrosion potential’ depends on the material, the concentrations of dissolved oxygen and the metal ions in the electrolyte, as well as the formation of passive and other protective layers. Table 1 below gives a few examples of the corrosion potentials of different metals in water.

Metal  Corrosion potential [VCSE]
Copper -0.10
Stainless steel -0.10
Red-bronze and Si-bronze -0.20
Brass -0.35
Iron in aerated water -0.55
Iron in stagnant water  -0.75
Galvanized steel -1.0

Table 1: Examples of corrosion potentials of different metals in water

Where there is an electrically conductive connection between two metals with different corrosion potentials, a galvanic cell is established. The reduction of oxygen occurs on both metal surfaces, while the oxidation reaction takes place primarily on the metal exhibiting the most negative potential, resulting in accelerated dissolution of the metal. Geometric effect plays an important role, since a small anode in contact with a large cathode can lead to corrosion rates up to 2mm/year in typical water applications.

Examples of unfavourable material combinations are shown in Figure 2 below.

Corrosion Figure 2a
Figure 2a) Combination of stainless steel and galvanized steel, with an internal coating

Simultaneous electric and electrolytic contact between stainless and galvanized steel will establish a galvanic element that accelerates the corrosion rate of the galvanized steel due to the increase in current (Figure 2a).

Corrosion Fig 2b
Figure 2b) Combination of stainless steel and galvanized steel, without an internal coating

An internal coating such as a synthetic resin applied to the galvanized steel might even increase local corrosion, since the entire anodic process is confined to the defect in the coating, thereby leading to a high local corrosion rate (Figure 2b).

Mitigation of galvanic corrosion

The following two solutions can be applied to minimise the risk of galvanic corrosion:

1.       Galvanic separation

Electrical separation of material is possible to mitigate galvanic corrosion by using insulating flanges or muffs to interrupt the electric current. In practice, these insulations are, unfortunately, often bypassed, either for reasons of safety (equipotential bonding) or by accident.

Figure 3
Figure 3: Galvanic separation of a cast-iron water meter and a stainless steel pipe by insulating flanges

The use of insulating flanges or muffs is thus often only a feasible solution to separate single devices, as for example a water meter, made from cast iron and internally coated, which is then integrated into a stainless steel pipeline (as shown in Figure 3). The water meter is electrically isolated from the system and will only suffer from galvanic corrosion if it is connected to the equipotential bonding.

2.       Insulation

The other method to reduce the effects of a galvanic cell is by increasing the electric resistance in the electrolyte, for example by incorporating an electrically insulating section between the related metal parts.

Corrosion Fig 4a
Figure 4a) Combination of a stainless steel pipe and a galvanized steel pipe with an insulating plastic pipe

This can, for example, be a plastic pipe between the stainless steel pipe and the galvanized steel pipe (Fig. 4a) or an internal coating of the stainless steel pipe (the cathode) as well as on the flange (Fig. 4b).


Corrosion Figure 4b
Figure 4b) Combination of a stainless steel pipe and a galvanized steel pipe with an internal coating section

The length of insulating section required depends on water conductivity, pipe diameters and the potential difference between the metals. In drinking water installations, a length of at least five times the pipe diameter is typically required.

Additional findings

Water composition

Experience has repeatedly shown that the formation of a thin, insulating layer of calcium carbonate, which is deposited on the metal with the most positive corrosion potential acting as cathode, reduces the risk of galvanic corrosion. The formation of this layer is favoured when a pH increase occurs at the cathode as the result of oxygen reduction as seen in reaction (2) above, which affects the lime-carbonic acid-equilibrium so that precipitation of calcium carbonate occurs.

Use of red-bronze fittings

It has been common to use red-bronze elements between sections of stainless steel and galvanized steel pipe. This might decrease the potential difference of the galvanic cell (Table 1) and thereby reduce the corrosion rate. However, experience of corrosion-related deterioration in such cases has shown that, this approach is not considered as a reliable method of corrosion protection, particularly when no insulating layer can be formed on the red-bronze.

Alloy composition of stainless steel

A variety of stainless steel alloys are admitted to be used for water installations. Electric contacts between them do not accelerate corrosion, even in the case of different corrosion potentials. The protective passive layer prevents corrosion and mitigates the galvanic cell.

Galvanic corrosion can cause severe damages in water and sewage installations. The growing number of different materials being used increases the risk of corrosion. This is especially true when replacing parts of the existing piping made of galvanized steel.

The presented mitigation measures allow eliminating the problem of galvanic corrosion without compromising the safety of electrical installations.



Swiss Society for Corrosion Protection:

CeoCor (The European Committee for the Study of Corrosion and Protection of Pipes and Pipelines Systems Drinking Water,Waste Water,Gas and Oil): 

CEOCOR 2018 Congress, Stratford on Avon, 15-18 May 2018



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