|
When used as a heat transfer
fluid in chiller applications, uninhibted ethylene glycol
can degrade, causing problems and increasing costs. Learn
the science behind its properties and why an inhibited ethylene
glycol might be a solution.
Uninhibited ethylene glycol
has been a popular heat transfer fluid choice in chillers
for many years because of its initial low cost and excellent
freeze and heat protection over a wide temperature range.
It also has good heat transfer capabilities and low conductivity,
not to mention that it is completely miscible with water
-- an inexpensive and abundant solvent.
Those are the pros.
There are, however, disadvantages inherent to uninhibited
ethylene glycol, including:
- It is relatively easy
to degrade.
- It promotes corrosion after
it degrades.
- It is difficult to monitor.
- It absorbs water from the
atmosphere.
These disadvantages can
lead to frequent fluid changing, which can cost users money
in labor and parts. There also can be lost production costs
due to shutdown and possible premature failure of the system.
Dow Chemical Co.,
Midland, Mich., distributes a technical bulletin entitled, "Acidic Thermal Degradation
of Ethylene Glycol and Propylene Glycol." This advisory
bulletin references the research of Dr. Walter Rossiter and
his team of the National Bureau of Standards, now named the
National Institute for Standards and Technology (NIST).
Dr.
Rossiter and his team conducted experiments that showed uninhibited
ethylene glycol will degrade into five organic acids -- glycolic,
glyoxylic, formic, carbonic and oxalic -- in the presence
of heat, oxygen, copper and aluminum. Copper and aluminum
act as catalysts in the presence of uninhibited ethylene
glycol. The organic acids then will chemically attack copper
and aluminum in as little as three weeks under the right
conditions to form metal organic compounds in the fluid.
| This mechanical
seal has been scored due to corrosion by products and/or
metal contamination of the fluid. |
 |
Another extensive study
on the degradation of uninhibited ethylene glycol was conducted
by John Beavers and Ronald Diegle of Battelle, Columbus Lab-oratories.
They concluded that degradation of uninhibited ethylene glycol
occurred in absence of contact with various metals, but degradation
was accelerated by the metals' presence.
Many chemical resistance
guides list that copper, aluminum and other metals are acceptable
for use with uninhibited ethylene glycol. Usually, their
recommendations are based on a two-week chemical compatibility
study exposing various metals to uninhibited ethylene glycol
at various temperatures. The above research indicates that
uninhibited ethylene glycol does not begin to degrade and
become acidic until after three weeks under extreme conditions
(212°F [100°C] and oxygen bubbling into the uninhibited ethylene
glycol solution). So, the chemical resistance guides are
based on the "solvency" effects of uninhibited ethylene
glycol rather than the degraded, acidic uninhibited ethylene
glycol effects on metals. The latter is much more corrosive
toward metals.
Corrosion of metals will
commence at locations where metal ions are stripped away
from the base metal by acidic, uninhibited ethylene glycol.
The section of metal that has had its surface metal stripped
away now becomes a metal oxide. Also, once metal ions are
in solution, they can attach themselves to oppositely charged
metals to form a galvanic corrosion cell. Rapid corrosion
can commence at these sites in the cooling loop. Corrosion
byproducts (metal oxides) then can be swept away to cause
damage downstream. Typical problems associated with corrosion
in a chiller cooling-loop system are clogging of a particulate
filter, damage to mechanical seals and premature failure
of the system.
Because uninhibited ethylene
glycol can degrade and become corrosive in as little as three
weeks, preventive maintenance can be time consuming and costly.
It is almost impossible to
achieve an accurate pH reading for 100 percent uninhibited
ethylene glycol because it is an organic liquid. pH meters
are susceptible to errors and instability when exposed to
organic chemicals. According to various manufacturers of
uninhibited ethylene glycol, they state this chemical has
a pH of 5.5 to 8.0. Most uninhibited ethylene glycol manufacturers
do not specify a pH for this chemical; they state not applicable
or not available (NA) on the product data sheet or material
safety data sheet (MSDS). Others state to dilute the chemical
with water to achieve a pH reading. But, by diluting with
water, is one measuring the pH of the added water or the
pH of uninhibited ethylene glycol/water solution?
A pH reading
of an uninhibited ethylene glycol/water solution becomes
less accurate with an increase in the uninhibited ethylene
glycol concentration. Increasing the water concentration
in uninhibited ethylene glycol allows for a more stable and
reliable pH reading. Some inherent problems associated with
using a pH meter to measure pH of an organic chemical are:
- The reference electrode
and internal buffer solutions are both aqueous.
- The activity
of the hydrogen ion can vary dramatically between an aqueous
and organic chemical.
- The dissociation of a compound can
vary dramatically between an aqueous and organic chemical.
- The external buffer solutions (for probe calibration)
are aqueous solutions.
Determining when to change out your uninhibited
ethylene glycol by measuring pH to detect an increase in
acidity is an unreliable measuring tool. Atomic absorption
spectroscopy (AAS) and inductively coupled plasma (ICP) are
two analytical tools that detect specific metals and their
concentrations in a fluid. A sample of the uninhibited ethylene
glycol can be extracted from an application and analyzed
by AAS or ICP to detect the metals that have been chemically
attacked by acidic uninhibited ethylene glycol. However,
this is a reactive approach because if there is a high concentration
of metals found in the fluid, this signifies that the uninhibited
ethylene glycol already has degraded and has turned acidic.
Corrosion already has occurred and internal system damage
is likely to be present.
A gas chromatography/mass spectrometer
(GC/Mass Spec) is used to detect organic compounds in a solution.
This analytical tool can measure the organic acids that develop
when uninhibited ethylene glycol starts to degrade.
Uninhibited ethylene glycol, like other glycols,
is hygroscopic; it will absorb moisture from its environment.
The amount of water absorbed from its environment is proportional
to the percent relative humidity (figure 1). At 50 percent
relative humidity, 100 percent uninhibited ethylene glycol
will absorb 20 percent water at equilibrium. This drops the
concentration of uninhibited ethylene glycol from 100 percent
to 83.3 percent.
Because of this property, ethylene glycol
is used as a humectant for textile fibers, paper, leather,
adhesives and glue. This desirable property helps make these
products softer, more pliable and more durable. However,
water absorption can potentially cause many problems in chiller
applications.
Many users of uninhibited ethylene glycol are
unaware of its hygroscopic property and often leave the cover
off the container. Once this occurs, uninhibited ethylene
glycol will immediately initiate water absorption.
Suppose
you have a new chiller and you fill it up with what you believe
is 100 percent uninhibited ethylene glycol from floor stock.
The relative humidity within your building is 75 percent,
and the application temperature is -4°F (-20°C). Accor-ding
to your freeze protection guide, you can fill the chiller
with 35.5 percent uninhibited ethylene glycol and 64.5 percent
(by volume) deionized (DI) or distilled water to achieve
freeze protection at -4°F. To be safe, you fill the chiller
with 38.5 percent uninhibited ethylene glycol and 61.5 percent
DI or distilled water to achieve freeze protection down to
-10°F (-23°C). If the environment on the floor is 75 percent
relative humidity and the cap has been kept off of the container,
the 100 percent uninhibited ethylene glycol can become 71.4
percent uninhibited ethylene glycol and 28.6 percent water.
Now, you dilute this solution with 61.5 percent water (thinking
you will have a solution of 38.5 percent uninhibited ethylene
glycol and 61.5 percent water) and your true concentration
becomes 27.5 percent uninhibited ethylene glycol and 72.5
percent water. This concentration only allows freeze protection
down to 7°F (-14°C). You now have a solution that you thought
would provide freeze protection to -10°F but in reality,
it only provides freeze protection to 7°F. The decrease in
freeze protection is 17°F (9°C). This error can result in
a system failure.
Conversely, 100 percent uninhibited ethylene
glycol is used for heat protection. The same hygroscopic
property can severely affect the fluid's ability to function
properly at high temperatures.
There are many ways that the
surrounding air can find its way into a closed-loop system.
Air (humidity) can enter a chiller when the cap to the tank
is removed for filling. Also, air can enter when the cap
to the tank is removed to visually inspect the fluid level
and during subsequent top-offs with uninhibited ethylene
glycol. Air also enters the chiller via any left open valves
or any leaks (loose hose clamps) in the system. Finally,
uninhibited ethylene glycol is viscous and will
entrap air when it is poured.
Industrially inhibited
ethylene glycol contains approximately 93 percent uninhibited
ethylene glycol, 3 percent water and 3 percent inhibitors.
The inhibitors serve two purposes: to protect
various metals in the cooling loop from corroding and to buffer the uninhibited
ethylene glycol so that it retards the degradation process.
Inhibited ethylene
glycol does share the same hygroscopic property as uninhibited
ethylene glycol. Preventative steps must be followed to ensure
minimal exposure to air. A disadvantage to inhibited ethylene
glycol, however, is its initial cost.
Using inhibited ethylene
glycol in place of uninhibited ethylene glycol can save money
over the lifetime of the chiller and tool. If uninhibited
ethylene glycol is not allowed to degrade (using inhibitors),
then money is saved by less frequent maintenance to the cooling
loop system (labor, parts and lost production costs) and
change out of the fluid (labor, replacement fluid and lost
production costs).
|