Home › Calculators › R-454B vs R-410A
R-454B runs about 8 to 10 percent below R-410A. That is close enough to feel familiar and far enough to matter — the same gauge reading is roughly five degrees off, and five degrees of saturation temperature is five degrees of superheat.
Saturated vapor (dew point) pressures, in psig, from −60 to 145 °F at 1 °F resolution in the full PT chart. R-32 is included because several manufacturers use it, and it sits on the other side of R-410A.
| Sat. temp | R-410A | R-454B | R-452B | R-32 |
|---|---|---|---|---|
| 20 °F | 78.4 | 70.6 | 72.0 | 80.0 |
| 40 °F | 118.4 | 107.5 | 109.4 | 121.0 |
| 45 °F | 130.1 | 118.3 | 120.5 | 133.0 |
| 110 °F | 365.4 | 336.3 | 341.5 | 374.9 |
| 120 °F | 418.3 | 385.5 | 391.4 | 429.3 |
Pressures in psig, saturated vapor.
The pattern is consistent: R-454B and R-452B sit below R-410A, R-32 sits slightly above it. R-452B is the closer match to R-410A of the two A2L blends, which is why it appears in equipment lines where the manufacturer wanted minimal change to the rest of the system. R-454B, which is the more widely adopted of the two, sits further away.
This is the table that actually matters in the field, because it is the direction a technician reads a gauge.
| Gauge reads | R-410A | R-454B | R-452B | R-32 |
|---|---|---|---|---|
| 70 psig | 15.0 °F | 19.6 °F | 18.7 °F | 14.1 °F |
| 118 psig | 39.8 °F | 44.8 °F | 43.9 °F | 38.7 °F |
| 200 psig | 69.7 °F | 75.2 °F | 74.1 °F | 68.3 °F |
| 300 psig | 96.1 °F | 101.9 °F | 100.8 °F | 94.3 °F |
| 400 psig | 116.7 °F | 122.8 °F | 121.6 °F | 114.7 °F |
Saturation temperature at a given gauge pressure, saturated vapor.
The error compounds in the direction that does damage. Adding charge to a correctly charged system raises head pressure, floods the condenser, reduces capacity and puts the compressor under load it was not selected for. The failure is slow, so it does not get connected back to the gauge reading that caused it.
R-410A is near-azeotropic. Its dew point and bubble point differ by about 0.2 °F, which is to say they do not differ. Twenty years of practice built on that, and PT charts for R-410A print one column because a second one would be identical.
Zeotropic blends behave differently. Their components boil at different temperatures, so at any fixed pressure the refrigerant starts evaporating at the bubble point and finishes at the dew point. The spread between them is glide.
| Refrigerant | Glide at 40 °F | Practical effect |
|---|---|---|
| R-410A | 0.19 °F | One column is fine |
| R-404A | 0.89 °F | Effectively one column |
| R-452B | 2.20 °F | Two columns matter |
| R-454B | 2.66 °F | Two columns matter |
| R-449A | 10.08 °F | Wrong column is a large error |
| R-407C | 11.10 °F | Wrong column is a large error |
| R-454A | 12.23 °F | Wrong column is a large error |
Dew point minus bubble point at 40 °F saturation.
On R-454B, using the wrong one costs about 2.7 °F. That is tolerable but not free. On R-454A it costs more than 12 °F, which is enough to make a correctly charged system unrecognizable. The habit is worth building now on the refrigerant where the penalty is small, because the same habit is what protects you on the refrigerant where it is not.
Fourteen refrigerants including R-454B, R-452B, R-454A, R-32 and R-410A, at 1 °F resolution from −60 to 145 °F, with a superheat and subcooling calculator. Free, no signup.
Open the PT chart →Under the AIM Act, the EPA is phasing down high global-warming-potential refrigerants. R-410A has a GWP around 2,088; R-454B is around 466 and R-32 around 675. Manufacture and import of R-410A equipment ended at the start of 2025, with a sell-through period allowing existing inventory to be installed into 2026.
Nothing about that phase-down obligates anyone to replace working equipment. R-410A remains available for servicing systems already in the field, and will be for a long time. What changed is what ships new.
A2L is an ASHRAE 34 safety classification: lower toxicity, lower flammability. The flammability is real but narrow — these refrigerants need a sustained, high-energy ignition source and a specific concentration range to burn. They are considerably harder to ignite than the natural gas already piped into most buildings.
What it changes in practice is procedural rather than dramatic: equipment is listed with refrigerant detection and mitigation, recovery equipment and gauges must be rated for A2L service, storage and transport rules differ, and brazing procedures account for it. None of that is exotic, but none of it is optional either.
All pressures and saturation temperatures were computed from the Helmholtz-energy equations of state implemented in CoolProp 8.0. Blends were evaluated as HEOS mixtures at their nominal mass fractions — R-454B as 68.9% R-32 / 31.1% R-1234yf, R-452B as 67% R-32 / 7% R-125 / 26% R-1234yf. Dew point corresponds to vapor quality 1 and bubble point to quality 0.
As a check on the mixture construction, R-410A was rebuilt as a 50/50 mass mixture of R-32 and R-125 and compared against CoolProp's predefined R410A fluid. The two agreed to 0.00 psi at 20, 40 and 60 °F.
Refrigerant classification follows ASHRAE Standard 34. Phase-down dates follow the EPA's AIM Act technology transitions rule. Manufacturer service literature governs on any specific piece of equipment and takes precedence over any general chart, including this one.