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Galvanic
Corrosion
Galvanic corrosion
results when two different metals are electrically connected and
surrounded by the same electrolyte.
This is the electrochemical basis for the lead acid battery.
The material with the highest electrochemical energy level
would experience corrosion, called the anode, and the other material,
called the cathode, would not experience corrosion.
In the water
industry, galvanic corrosion could be expected from connections
between ferrous materials such as, steel and ductile iron, and copper,
stainless steel and brass. In this corrosion cell the ferrous materials
would corrode relative to the other materials. This relationship
is normally depicted in a table referred to as the galvanic series.
The following
table lists the common piping and construction materials in order
of galvanic activity:
| Material
|
Potential
(mV) |
Activity
|
| Magnesium |
1.70 |
Most active, Anodic |
| Steel |
0.50 0.60 |
|
| Ductile
iron |
0.30 0.40 |
|
| Corroded
steel |
0.30 0.40 |
|
| Cast
iron |
0.10 0.20 |
|
| Copper |
0.15 0.20 |
|
| Brass |
0.15 0.20 |
|
| Stainless
steel |
0.10 0.20 |
Least active, Cathodic |
This chart indicates
that for two dissimilar metals being electrically connected, the
one towards the most active end would be anodic or experience corrosion,
and the one towards the least active end would be cathodic or not
experience corrosion. For
the corrosion cell to establish, both materials need to be in a
common electrolyte and electrically connected.
Common examples would be a copper service connected to a
ferrous metal main in soil and stainless steel pipe repair clamp
with alloy steel bolts. In these examples, the copper and stainless
steel would be cathodic, and the ferrous materials anodic and experience
corrosion.
This is the
fundamental concept of cathodic protection. Cathodic protection
causes certain electrochemical reactions to occur on the structure
that is being protected against corrosion. The protected structure becomes cathodic relative to the anode
material. For sacrificial
anode cathodic protection, this is typically effected through the
use of magnesium anodes on steel or ductile iron pipe.
Cathodic protection will be presented in more detail later
in this paper.
A condition
that is similar to the corrosion exposure that results from dissimilar
metals, arises when new pipe materials are installed within old
piping systems. Because
the old materials have developed a corrosion layer or film, their
corrosion activity has slowed.
The new materials are more active, as there is no corrosion
film present, and therefore when connected to the old pipe they
can experience corrosion.
Stray
Current
Stray current
corrosion results from sources outside the influence of the pipe
and its environment. To
cause stray current on a pipeline, the current must flow onto the
pipe at one location and then flow off the pipe at another location.
Where the stray current leaves the affected pipe, corrosion
will occur. Common
sources of stray current in the water industry are primarily rapid
transit systems and transmission pipeline operations that employ
impressed current cathodic protection.
Current flow
in a pipeline which provides a continuous metallic path to the power
neutral ground grid will not cause corrosion damage.
If the current discharges from the pipeline into the environment,
it will cause corrosion loss at the rate of 20 pounds of metal loss
in one year per ampere of discharge.
Therefore, a current discharge of 0.5 amperes for 1 year
would remove 10 pounds of metal. At a density of 450 lbs/ft3 of cast iron for example,
this equates to 38 in3 of metal removed in one year.
This type of corrosion manifests itself on the pipe surface
by a clean, sharp, pocked surface.
The primary
source of stray current in large metropolitan areas comes from the
operation of rapid transit systems.
Those that operate on direct current, DC, with the running
rail or track functioning as the negative return are capable of
generating stray current.
Because these systems operate at 700 to 1,000 volts, and
trains draw upwards of 15,000 amperes when accelerating, the possibility
of small amounts of stray current flowing into the ground is clear.
Stray current patterns from this type of operation are dynamic,
they constantly fluctuate.
The other source
of stray current comes from the operation of impressed current cathodic
protection systems. Impressed current cathodic protection is utilized to protect
long pipelines, poorly coated structures, above ground storage tank
farms and other type of structures.
This type of protection is required where sacrificial anode
cathodic protection would not provide adequate protection.
As these are DC current systems, stray current can be generated
from their operation. Stray current patterns from this type of operation
are static, they do not fluctuate over time unless adjusted.
Stray current
corrosion exposure can be very localized within the piping network.
Because of the variable magnitude of the stray current, corrosion
loss can be far greater than any of the other corrosion mechanisms
acting on the pipe.
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