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Glycol water mixture calculator

Pick the glycol and the coldest temperature the loop can see. The page gives the concentration with a safety margin, the solution properties and how much flow, pressure drop and pump power rise compared with water.

Pre-sizing and estimating tool: results do not replace design, calculations or reports signed by a licensed professional, nor verification against the applicable codes and standards.

Pre-sizing
Glycol and freeze protection
Loop
Pumping

Typical properties of commercial inhibited glycols (Dow), by % volume; the page also shows % by mass.

—Recommended glycol concentration
—

Freezing point versus concentration

Inhibited ethylene and propylene glycol, as % of solution volume.

Tap the chart to see the values.

What changes compared with water

Same heat load and temperature difference; 100% = value with water.

Tap the chart to see the values.

Solution properties by temperature

Next step

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Method, assumptions and references

Equations used

Concentration: lowest % by volume with Tfreeze ≤ Tmin − margin (interpolated in the freezing table), and at least the inhibitor minimum
Flow: V = Q ÷ (ρ · cp · ΔT); flow ratio: Vg ÷ Vw = (ρ cp)water ÷ (ρ cp)glycol
Head with glycol: Hg = Hw · (fg · ug²) ÷ (fw · uw²), with Colebrook f in the main pipe (Re = ρ u D ÷ μ)
Power: P = ρ · g · V · H ÷ η; capacity at the water flow: Q′ = Q · (ρ cp)glycol ÷ (ρ cp)water
Properties: linear interpolation in T and concentration (ρ, cp) and in ln μ versus 1/T (viscosity); water from IAPWS

Assumptions and limits

  • Typical properties of commercial inhibited glycols (Dow tables by % volume); another maker’s or uninhibited glycol may differ by a few percent. Outside the tabulated range, the page extrapolates.
  • The friction correction uses one representative pipe and applies the same ratio to the whole loop head, including coils and exchangers; it is an estimate.
  • The water comparison uses the same mean temperature, with a 39 °F (4 °C) minimum. Freezing point is the onset of crystal formation; burst protection needs less glycol but does not allow pumping.

Standards and technical documents

  • ASHRAE Handbook — Fundamentals, chapter “Physical Properties of Secondary Coolants (Brines)”
  • Dow, Engineering and Operating Guide for DOWTHERM SR-1 and DOWTHERM 4000 Inhibited Ethylene Glycol-based Heat Transfer Fluids
  • Dow, Engineering and Operating Guide for DOWFROST and DOWFROST HD Inhibited Propylene Glycol-based Heat Transfer Fluids
  • ASHRAE Handbook — HVAC Systems and Equipment, chapter on hydronic heating and cooling (antifreeze solutions)
  • Melinder, Å. Properties of Secondary Working Fluids for Indirect Systems, IIR, 2010

U.S. regulations

  • OSHA 29 CFR 1910.1200: hazard communication and safety data sheets for glycol
  • EPA Safe Drinking Water Act and local cross-connection control rules: backflow protection between glycol loops and potable water
  • ASHRAE Standard 90.1: hydronic system design and pump power requirements

Frequently asked questions

How much glycol should I add?

Enough for the solution to freeze a few degrees below the coldest temperature the loop can see. In the example, for a 14 °F minimum with a 5 °F margin, ethylene glycol needs 25.7% by volume (27.9% by mass), freezing at 9 °F. More glycol than needed only adds viscosity, pump energy and cost.

Ethylene or propylene glycol?

Ethylene glycol transfers heat better and is less viscous, but it is toxic; propylene glycol is the choice where food, beverages or potable water could be contacted. For the same protection, propylene glycol needs a little more concentration (29.5% versus 25.7% in the example) and more pumping energy. Either way, use inhibited industrial glycol, never automotive antifreeze.

Why do flow and pump power go up?

The solution has a lower specific heat than water, so each gallon carries less heat and more flow is needed for the same load: in the example, 260 gpm instead of 239. It is also about twice as viscous in the cold, which increases friction. The result is 29% more head and 47% more pump power, about $1,240 a year in the example.

What if I just add glycol to an existing water system?

If flow stays the same, heat-carrying capacity drops at least 8% in the example, and coils and exchangers also perform worse. The existing pump may deliver less flow because of the higher loss. Check the pump, the heat exchangers and the expansion tank before switching fluids.

Is there a minimum glycol concentration?

Yes. Below about 25% to 30% by volume, corrosion inhibitors get too diluted and the solution can even feed bacterial growth, so the page uses 25% as the default minimum. Check the exact value on the product data sheet.

Where do the properties come from, and what are the limits?

They are typical values for commercial inhibited glycols from manufacturer tables, interpolated by temperature and concentration; above 50% and outside the tabulated range they are extrapolated. Other makers’ products can differ by a few percent. The friction correction uses one representative pipe and is an estimate for the whole loop.

How do I check the concentration in the system?

With a glycol refractometer, or by measuring density and comparing with the manufacturer’s table. A yearly fluid analysis (concentration, pH and inhibitor reserve) is recommended, because topping up with plain water dilutes the glycol over time.