Subcooling by refrigerant
R-410A subcooling from liquid line pressure
- where
- absolute pressure (bar)
- liquid line gauge pressure (bar)
- atmospheric pressure (bar)
- bubble-point saturation temperature (°C)
- table temperature at or below the reading (°C)
- table pressure at T₁ (bar abs)
- next table temperature above (°C)
- table pressure at T₂ (bar abs)
- subcooling (K)
- measured liquid line temperature (°C)
- subcooling in Fahrenheit degrees (°F)
Explain this equation
Works out how far the R-410A liquid line is below its condensing (saturation) temperature. Use it to check or set the charge on TXV and EEV systems and to make sure solid liquid reaches the expansion device.
The gauge reads pressure above the atmosphere, so P_atm is added to get the absolute pressure P_abs that the P-T table uses. T_bub is the temperature at which R-410A liquid starts to boil at that pressure; T_liq is the actual pipe temperature. Every kelvin the liquid sits below T_bub is a kelvin of subcooling. R-410A is a near-azeotropic blend with a small glide, so the bubble point is used, as for any blend.
Saturation pressure rises roughly exponentially with temperature, so ln P is close to a straight line against T over a few kelvin. The calculator finds the two table rows either side of your reading (T₁, P₁ and T₂, P₂) and interpolates in ln P, which is much more accurate than a straight line through the raw pressures. The 1.8 converts a kelvin difference into Fahrenheit degrees for US charging charts.
Sense check: an air-cooled condenser on a 25–30 °C day typically condenses around 40–45 °C, and 3–6 K of subcooling is a common target. Zero subcooling means vapour may reach the expansion device; 15 K or more means liquid is backing up in the condenser.
Watch out: measure pressure and temperature at the same point, shade the probe from the sun and the condenser air, and remember receivers hide subcooling at their outlet.
Works out R-410A subcooling from a liquid line gauge reading and a pipe temperature, using a built-in R-410A pressure-temperature table.
R-410A is a near-azeotropic blend with a small glide; the calculator still uses the correct column. Safety class A1 (lower toxicity, non-flammable).
Enter your values to see the result.
Good to know
Measure at the condenser outlet or liquid service valve, with pressure and temperature taken at the same place. Charge TXV or EEV systems to the manufacturer’s target subcooling; 3–6 K is common for air conditioning. Systems with a liquid receiver usually show little subcooling at the receiver outlet even when correctly charged, so use the sight glass and manufacturer guidance there. Near-azeotropic HFC blend (glide about 0.1 K), so bubble and dew are almost the same. Being phased out of new split systems in favour of R-32 and R-454B. Safety class A1: lower toxicity, no flame propagation.
Common mistake
Using the dew-point (vapour) column for subcooling on a blend, which understates subcooling by roughly the glide. Reading discharge pressure instead of liquid pressure, or measuring the pipe temperature in direct sunlight or a hot condenser air stream.
Limits
Table range 1.1 to 42.53 bar absolute (-50 to 65 °C). Saturation temperatures are interpolated from the published table (ln P against T between rows); checked against published points within ±0.3 K. Accuracy depends on the gauge and probe; pressure drop between the gauge point and the probe point adds error.
Sources
- Chemours: Freon 410A SI thermodynamic properties, Table 1 saturation properties – temperature table (liquid and vapour pressure, kPa abs)
- Arkema: Forane Pressure Temperature Chart (PPC/SDC 05-2025) – saturated liquid and vapour pressures, psig, 5 °F steps
- ANSI/ASHRAE Standard 34 and ISO 817: Designation and safety classification of refrigerants (A1, A2L, A3, B2L)
- ACHR News: Understanding superheat (superheat = measured vapour temperature − saturation temperature at the same point)
- Honeywell: How to manage and take advantage of refrigerant glide (dew point for superheat, bubble point for subcooling)
Results are calculations from the published methods and figures shown, and depend on the data you enter. Follow the equipment manufacturer’s data, CIBSE guidance, BS EN 378, the F-gas Regulations and your company procedures. Refrigerant work needs the correct F-gas certification.