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Cathodic Protection Of Steel in Concrete

Theory and Mechanism Of Cathodic Protection of Steel In Concrete

The cathodic protection of metal against corrosion was first demonstrated in the early nineteenth century.  Since that time, this process has been used to stop the corrosion of metallic structures and components in a wide variety of environments.

Essentially, cathodic protection is the intentional application of a direct electric current in opposition to the naturally occurring electrochemical corrosion of metal.
Cathodic protection is now a generally accepted and economical practice for reducing or eliminating the corrosion of metals, particularly steel. 

 Steel structures as varied as underground storage tanks, ships' hulls, oil well casings, hot water heaters, gas pipelines, concrete reinforcing steel, and offshore drilling rigs, are successfully protected by cathodic protection.

The natural corrosion of steel involves the formation of an electrochemical corrosion cell.  This cell is made up of an anode and a cathode, typically at two different sites on the steel component, an electrolyte, and an electrical connection between the anode and cathode.

    The chemical reaction at the steel anode site is the oxidation of the metal, followed generally by oxide or hydroxide formation:

Fe                      ®        Fe++ + 2 e-           (1)

Fe++ + 2OH-   ®        Fe(OH)2                     (2)

At the same time, an electrochemical reaction, generally the reduction of atmospheric oxygen, occurs at the steel cathode site:

½O2 + H2O + 2e- ®     2OH-                          (3)

For steel reinforcing bar in concrete, the steel rebar may corrode when the passive (non-corroding) steel surface is exposed to chloride ions which de-stabilize the normal oxide film on the rebars embedded in the alkaline concrete environment. 

The chloride ions may result from the use of deicing salts, exposure to sea water or marine fog, or from chloride added to the fresh concrete.  
The electrochemical corrosion cell is set up when two different parts of the rebar mat, which are electrically bonded together, act as the anode and cathode, as shown in Figure 1 .

The electrolyte in this case is the concrete, which will normally contain enough moisture to conduct the electrical corrosion current.  Since the steel corrosion products, the iron oxides, occupy a larger physical volume than the uncorroded steel, the rebar corrosion will exert tensile stresses on the surrounding concrete, with the stresses increasing until cracks, delaminations, and eventually potholes or spalls are formed.

In order to reduce or stop the corrosion reactions shown above, the steel component must be made cathodic, so that reaction (3), and not reaction (1), will occur on the whole of the steel surface. 

Correspondingly, an anodic reaction must occur on the surface of an anode which is provided for the cathodic protection (CP) system.  There are two forms of cathodic protection: galvanic and impressed current CP.
In galvanic systems, the anode will be intentionally less resistant to corrosion than the steel, and therefore will corrode sacrificially.

 Galvanic systems are limited by the amount of sacrificial metal which is supplied to corrode.  This metal is often a zinc electrode at which zinc oxidation occurs:

Zn        ®     Zn++ + 2e-(4)

In impressed current CP systems, the anode is generally a conductive material which is not consumed.  A typical anode is a titanium substrate covered on its active surface by a noble metal or metal oxide catalyst.  The anode reaction in this case will generally be the formation of oxygen from water:

2H2O      ®          O2 + 4H+ + 4e(5)

For galvanic CP systems, the electrical current is provided by the chemical driving force for the two electrochemical reactions, (3) and (4).  For impressed current CP systems, a separate source of DC current needs to be supplied, and reactions (3) and (5) will occur.   

The choice between a galvanic and an impressed current system depends on the specific characteristics and environment of the metal component to be protected and by the chemical and physical constraints placed by the anode system.  Figure 2    shows the typical components for an impressed current cathodic protection system.

A number of novel anode systems for the impressed current Cathodic Protection of reinforced concrete.

 One system, a unique titanium anode  is embedded directly into the concrete, above, below, or between a set of rebar mats, for either new or rehabilitated concrete structures.

When connected to a suitable DC rectifier, the anode system will provide effective protection for the steel reinforcing bar.

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Figure 1. Electrochemical corrosion cell setup in concrete

Figure 2. Impressed current cathodic protection system.

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