Be Corrosion Free
by Engineering Staff, Lytron Inc.
January 1, 2010
|
|
| Aluminum cold plates and plate-fin heat exchangers commonly
are used because of their light weight and high performance, but special care
must be taken to avoid corrosion.
|
|
Proper design and maintenance tasks can help reduce
corrosion in plate-fin heat exchangers.
Because of their light weight
and high performance, aluminum cold plates and plate-fin heat exchangers
commonly are used for liquid cooling. There are many factors to consider when
designing these cold plates and heat exchangers, including:
- Thermal performance.
- Size.
- Fluid pressure drop.
- Weight.
- Burst pressure.
- Corrosion resistance.
Because corrosion is a common problem, a focus on corrosion resistance during
the design, build and operation of aluminum cold plates and plate-fin heat
exchangers should be a priority.
Corrosion of Aluminum
Aluminum is known for its corrosion resistance. Under the
right conditions, aluminum rapidly forms a protective oxide layer. Generally,
this occurs when oxygen is readily available and the surrounding medium has a
moderate pH.
There are two typical manifestations of aluminum corrosion: uniform corrosion
and local corrosion. Uniform corrosion happens when the oxide layer is soluble
in the corrosive medium. According to the ASM Metals Handbook, “The oxide film
is soluble in alkaline solutions and in strong acids…but is stable over a pH
range of approximately 4.0 to 9.0.” With uniform corrosion, the entire oxide
layer is stripped away faster than it can re-form.
Local corrosion, usually in the form of a pit, occurs when there is
non-uniformity in the base metal or the surrounding environment. For instance,
the metal may have a local concentration of alloying elements that creates a
galvanic couple. Similarly, the surrounding environment may have a local
concentration of active elements such as chlorides.
Cold plates and heat exchangers are used with many different fluids and
typically involve the recirculation of the same fluid. One fluid that should
not be used in aluminum cold plates and heat exchangers is water. Tap water, in
particular, can contain active ions such as copper, bicarbonates, chlorides and
other impurities that facilitate corrosion. In addition, over time, the
recirculation of the same fluid in a closed loop will cause the dissolved
oxygen to come out of solution. The resulting lack of oxygen will inhibit the
formation of the oxide layer. Given enough time, aluminum will eventually
corrode if isolated from oxygen and exposed to low-quality water. When water is
the preferred choice for a heat transfer system, distilled water usually is combined
with a glycol to reduce the freezing point and increase the boiling
point.
For the reasons already noted, it is critical that corrosion inhibitors be
used. Corrosion inhibitors are controlled amounts of active ions (usually
phosphates) that take over the role of oxygen in forming a corrosion-resistant
layer. Because these inhibitors depend on a chemical reaction with the
aluminum, using low-quality water such as tap water would reduce the
inhibitors’ effectiveness.
The Importance of Design
|
|
| Proper design can help reduce the chances of corrosion occurring
within an aluminum cold plate and plate-fin heat exchangers.
|
|
For the best corrosion resistance, good design is top
priority. In addition, alloy selection is a key factor in ensuring good
corrosion resistance. For example, braze sheets, which separate the fluid
passages in plate-fin heat exchangers, consist of an internal core and external
clad layer that usually represents about 10 percent of the overall sheet
thickness. The clad layer is a brazing alloy that joins the braze sheet to both
the hot and cold fins and the braze sheet to the side bars. Vacuum brazing
alloys use silicone and other elements to lower the melting point of the alloy.
Because the braze alloy is more anodic than the core, the braze alloy provides
cathodic protection and, thus, corrosion protection.
Cathodic protection is a concept that has been used in the ship-building
industry for decades. For hulls made of steel, a plug made of an active element
like zinc is used to protect the hull. Because zinc is more active than steel,
the zinc corrodes faster than the steel. Among the alloying elements of
aluminum, the alloys with a minimum of copper and iron have the best corrosion
resistance.
Other considerations in cold plate and heat exchanger design also contribute to
reducing corrosion. For instance, internal fluid static pressure and external
stresses put the core components under stress. These stresses often require
that high strength alloys be used for the braze sheets or fins. Selecting the
braze sheet thickness requires trade-offs among performance, weight and
corrosion protection. A thick braze sheet has less strength to withstand
stresses and offers less corrosion protection. Yet if a corrosive environment
is present, thin braze sheets will withstand an attack for less time than a thicker
sheet.
Heat Exchanger Operation
|
|
| Cold plates and heat exchangers are used with many fluids.
Recirculating a volume of fluid can lead to corrosion over time unless it is
accounted for in the system design.
|
|
When operating a water/glycol cold plate or heat exchanger,
it is important to have a maintenance plan. The typical maintenance activity is
flushing and refilling the system with the proper mixture of inhibited ethylene
glycol and water. This should be done on a periodic basis at an interval
determined through system level testing during the operation evaluation
phase.
Periodically, the fluid pH and refractive index should be measured. These
measurements will change over time. From these measurements, a flushing
frequency should be determined.
During deployment, it is common for systems to be “topped off.” This practice
should not harm the cold plate or heat exchanger as long as the glycol
concentration is not diluted to the point of making the inhibitor ineffective.
Inhibitor ineffectiveness is a function of top-off water quality, other metal
types in the fluid loop and the age of the inhibitor in the system. If topping
off is employed, it is advisable to monitor the pH of the fluid. If the pH
falls below 4.0 or rises above 9 in a system, flush/fill should take place as
soon as possible.
Corrosion resistance begins with cold plate or heat exchanger design. By
working with a manufacturer that understands corrosion and how to prevent it,
you will achieve a better product. It also is important to develop maintenance
procedures that will maximize the life of the aluminum cold plate or heat
exchanger.
|