| DUTY | TYPICAL SERIES | FLUID | SIZE FOR |
| Glycol Systems | WU | Ethylene or propylene | Cold condition |
Glycol appears wherever a circuit is exposed to freezing ambient: snow melt loops, rooftop equipment, outdoor process cooling, and any system that might sit idle in winter. It also appears where a fluid must not freeze even briefly, because the consequence of a burst coil is out of proportion to the cost of protection.
Glycol is not water with antifreeze in it. It is more viscous, less thermally conductive and has a lower specific heat. All three work against the duty at once: the film coefficient falls, the pressure drop rises, and more mass flow is needed to move the same heat.
Size for the cold condition. Viscosity rises steeply as temperature falls. A loop comfortably turbulent at operating temperature can be laminar at startup on a cold morning, and once flow goes laminar the coefficient collapses and warm-up takes far longer than predicted.
Concentration costs performance permanently. Every percentage point above what the freeze protection genuinely requires reduces heat transfer and raises pumping power for the life of the system. Loops are routinely over-concentrated on the theory that more must be safer.
Propylene or ethylene. Propylene wherever any possibility of food or potable contact exists, since it is far less toxic. Ethylene otherwise, because it is less viscous and performs better thermally at the same concentration.
The actual fluid at the actual temperature, not water properties with a correction.
Establish the design low temperature the system must survive, add a modest margin, and set the concentration to protect against that. Every point above it costs heat transfer and pumping power every hour the system runs, for no additional protection.
Concentration also drifts as make-up water is added over the years, usually downward. Check it periodically rather than assuming it is still what was filled.
A properly sealed and treated glycol loop should stay clean for years. Where fouling recurs, the cause is almost always oxygen ingress and an exhausted inhibitor package, and the deposits are corrosion products from the system itself.
Cleaning the exchanger addresses the symptom. Finding the air ingress and restoring the inhibitor addresses the cause.