Corrosion is costly! If you doubt this, then you probably have never been
bitten by the "corrosion bug". Imagine specifying Titanium for 10 brand
new heat exchangers or reactors and later realizing that the processing stream has fairly
high concentrations of flourine ions. The Titanium will be destroyed in weeks and
you'll have wasted hundreds of thousands of dollars. There you stand in front of
your supervisor, you'll get that sick feeling in your stomach....that's the
"corrosion bug"! I'd like to think that things like this don't happen, but
I've heard my share of horror stories. If you'd like to avoid a situation like this,
I've got two words for you.....FLUID ANALYSIS. A fluid analysis can save you pain,
embarassment, and in some cases your job. But if you think about, there' really no
excuse for not having one done considering the impact that a material of construction
decision can have. With this in mind, I thought that it may be a good idea to
review some of the most basic forms of corrosion.
Uniform Attack
Uniform attack is a form
of electrochemical corrosion that occurs with equal intensity of the entire surface of the
metal. Iron rusts when exposed to air and water, and silver tarnishes due to
exposure to air. Pontentially very risky, this type of corrosion is very easy to
predict and is usually associated with "common sense" when making material
decisions.
Galvanic Corrosion
Galvanic corrosion is a little more difficult to
keep track of in the industrial world. You'll notice below that simply adding a
screw of the wrong material can have severe consequences. Galvanic corrosion occurs
when two metals having different composition are electrically coupled in the presence of
an electrolyte. The more reactive metal will experience severe corrosion while the
more noble metal will be quite well protected. Perhaps the most infamous examples of
this type of corrosion are combinations such as steel and brass or copper and steel.
Typically the steel will corrode the area near the brass or copper, even in a water
environment and especially in a seawater environment. Probably the most common way
of avoiding galvanic corrosion is to electrically attach a third, anodic metal to the
other two. This is referred to as cathodic protection.
Crevice Corrosion
Another form of electrochemical
corrosion is crevice corrosion. Crevice corrosion is a consequence of concentration
differences of ions or dissolved gases in an electrolytic solution. A solution
became trapped between a pipe and the flange on the left. The stagnant liquid in the
crevice eventually had a lowered dissolved oxygen concentration and crevice corrosion took
over and destroyed the flange. In the absence of oxygen, the metal and/or it's
passive layer begin to oxidize. To prevent crevice corrosion, one should use welds
rather than rivets or bolted joints whenever possible. Also consider nonabsorbing
gaskets. Remove accumulated deposits frequently and design containment vessels to
avoid stagnant areas as much as possible.
Pitting
Pitting, just as it sounds, is
used to describe the formation of small pits on the surface of a metal or alloy.
Pitting is suspected to occur in much the same way crevice corrosion does, but on a flat
surface. A small imperfection in the metal is thought to begin the process, then a
"snowball" effect takes place. Pitting can go on undetected for extended
periods of time, until a failure occurs. A textbook example of pitting would be to
subject stainless steel to a chloride containing stream such as seawater. Pitting
would overrun the stainless steel in a matter of weeks due to it's very poor resistance to
chlorides, which are notorious for their ability to initiate pitting corrosion.
Alloy blends with more than 2% Molybdenum show better resistance to pitting attack.
Titanium is usually the material of choice if chlorides are the main corrosion
concern. (Pd stabilized forms of Ti are also used for more extreme cases).
Intergranular Corrosion
Occuring along grain
boundaries for some alloys, intergranular corrosion can be a real danger in the right
environment. On the left, a piece of stainless steel (especially suspectible to
intergranular corrosion) has seen severe corrosion just an inch from a weld. The
heating of some materials causes chromium carbide to form from the chromium and the carbon
in the metals. This leaves a chromium deficient boundary just shy of the where the
metal was heated for welding. To avoid this problem, the material can be subjected
to high temperatures to redissolve the chromium carbide particles. Low carbon
materials can also be used to minimize the formation of chromium carbide. Finally,
the material can be alloyed with another material such as Titanium which forms carbides
more readily so that the chromium remains in place.
Selective Leaching
When one element or constituent
of a metal is selectively corroded out of a material it is referred to as selective
leaching. The most common example is the dezincification of brass. On the
right, nickel has be corroded out of a copper-nickel alloy exposed to stagnant seawater.
After leaching has occurred, the mechanical properties of the metal are obviously
impaired and some metal will begin to crack.
Erosion-Corrosion
Erosion-corrosion arises from a
combination of chemical attack and the physical abrasion as a consequence of the fluid
motion. Virtually all alloy or metals are susceptible to some type of
erosion-corrosion as this type of corrosion is very dependent on the fluid.
Materials that rely on a passive layer are especially sensitive to
erosion-corrosion. Once the passive layer has been removed, the bare metal surface
is exposed to the corrosive material. If the passive layer cannot be regenerated
quickly enough, significant damage can be seen. Fluids that contain suspended solids
are often times responsible for erosion-corrosion. The best way to limit
erosion-corrosion is to design systems that will maintain a low fluid velocity and to
minimize sudden line size changes and elbows. The photo above shows
erosion-corrosion of a copper-nickel tube in a seawater surface. An imperfection on
the tube surface probably cause an eddy current which provided a perfect location for
erosion-corrosion.
Stress Corrosion
Stess corrosion can result from
the combination of an applied tensile stress and a corrosive environment. In fact,
some materials only become susceptible to corrosion in a given environment once a tensile
stress is applied. Once the stress cracks begin, they easily propagate throughout
the material, which in turn allows additional corrosion and cracking to take place.
The tensile stress is usually the result of expansions and contractions that are caused by
violent temperature changes or thermal cycles. The best defense against stress
corrosion is to limit the magnitude and/or frequency of the tensile stress.
References:
Callister, William D., Materials Science and Engineering, 3rd
Ed., Wiley, New York, 1985