OFFSHORE CATHODE PROTECTION
What is it and how does it work?
Why does steel corrode in sea water?
To fully understand the importance of cathode protection , the mechanism of corrosion itself must be understood in the first place. There are three factors that underlie the occurrence of corrosion:
- two dissimilar metals
- one electrolyte (water with any type of salt or salts dissolved in it)
- a conducting path between the metals
The two different metals can be entirely different alloys such as steel and aluminum. However, it is usually a question of microscopic and macroscopic metallurgical differences on the surface of one and the same piece of metal.
If this is the case ( let us bear in mind that steel does not corrode evenly), then these will be places with increased activity and the following reaction will take place ( two iron ions plus four free electrons):
2Fe => 2Fe+++ 4e-
The free electrons pass through the metal moving towards less active sites, where the following reaction takes place- oxygen in the form of gas combines with four free electrons and turns into an oxygen ion , which in turn combines with water to form hydroxyl ions:
O2+ 4e-+ 2H20 => 4 OH-
Recombination of these ions on the active surface produces the following reaction, which lead to the formation of iron-corrosion product – ferrous hydroxide.
2Fe + O2+ 2H2O => 2Fe (OH)2
This reaction is more commonly described as current flow through the water from the anode ( the more active site) to the cathode ( the less active site).
How does cathode protection stop corrosion?
Cathode protection prevents corrosion by converting all anode sites (active) on the metal surface into cathode sites ( passive) by means of electric current ( or free electrons) coming from an external source of electricity. This is usually in the form of galvanic anodes, which are more active than the steel. This technique is also known as a cathodic protection system by means of sacrificial anodes, i.e. the galvanic anodes are sacrifice themselves to protect the steel structure or pipeline from corrosion.
In the case of alumina anodes the reaction on the surface of alumina is the following – 4 alumina ions plus 12 free electrons.
4Al => 4AL++++ 12 e-
On steel surfaces oxygen in the form of gas, turned into oxygen ions , combines with water to form hydroxyl ions:
3O2+ 12e-+ 6H20 => 12OH-
As long as the current ( free electrons) reaches the cathode ( steel) faster than the oxygen, no corrosion will occur.
Figure 1: Sacrificial anode system in seawater
Basic considerations when designing sacrificial anode system
The electric current an anode discharges is controlled by Ohm’s Law:
I = E/R
I is the current flow measured in Amps /A/
E is the difference in potential between the anode and the cathode measured in Volts/V/
R total circuit resistance measured in Ohms /Ω/
Initially , the electric current will be high, because the difference in potential between the anode and the cathode is big. But the flow of electric current onto the cathode will make that difference smaller, thus, resulting in gradual decreasing of the current due to the polarization of the cathode.
The circuit resistance includes any water path , metal path, and any cable in the circuit. The dominant value in this case is the resistance of the anode to the seawater. For most applications, the resistance of the metal is so insignificant as compared to that of water that it can be easily ignored ( this does not refer to sleds or long pipelines protected from both ends).
In general, the long, thin anodes have less resistance than the short, thick ones. They will discharge more electric current but they are not that durable. This is the reason why a designer of a cathodic protection system must be capable of determining the size of the anodes so that they would have the right shape and surface area to discharge enough current to protect the structure. In addition, the anodes must have the appropriate weight so as to endure the desired lifetime when discharging that current.
A general rule: The length of the anode determines how much current they will produce. Therefore, this will determine how many square meters of steel will be protected. The cross section ( weight) determines how long the anode will be capable of sustaining this level of protection.
Impressed current Cathodic protection systems
Due to the high currents involved in many of the systems with sea water, impressed current systems are commonly used. These systems use a type of anodes, which are not easily dissolved into metallic ions. This causes the following alternative reaction: oxidation of dissolved chlorine ions.
2Cl-=> Cl2+ 2e-
Power is supplied by an external DC power unit.
Figure 2 : Cathodic protection system with injected current
How do we know that we have efficient cathodic protection?
To make sure that the current value is sufficient, we have to compare the potential ( pressure) in the steel against the potential of a standard reference electrode, usually silver or silver chloride (Ag/AgCl) sea water, or sometimes zinc (Zn sea water).
The current flow in any metal changes its potential in the negative direction. It has been proved by experience that if the steel receives enough current so as to change the potential to – 0,800V vs silver/silver chloride, corrosion is actually stopped.
Due to the nature of the films formed, the minimum pressure ( -0.800V) is rarely achieved, so the designers try to achieve a potential between – 0,950 V and - 1,000V vs Ag/AgCl sea water.
Figure 3: Measuring the potential of cathodic protection
( Unprotected – on the left / protected- on the right)
Sleds with anodes for impressed current cathodic protection
Protection of metal rabbets in harbours and shore structures with static metal surfaces by impressed current is a challenge in terms of anchoring the anodes ( iron, silica or titanium anodes). The sleds are designed for placing anodes on the seabed or riverbed.
The anode bed is held in place by counterweights , and in some cases anchors are added for better fixation, especially in cases of moving shore masses.