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PT Chart — Superheat & Subcooling Calculator

Pressure-temperature data and charge diagnostics for R-410A, R-454B, R-32, R-22, R-134a, R-404A and R-407C. Separate vapor and liquid columns, because blends have two saturation pressures and using the wrong one is a real error. Jump to the printable charts ↓

Built and verified by Kyle Lorinos, PE — HVAC design engineer. See the method and validation →

Measurements

Suction side → superheat

psig
°F

Liquid side → subcooling

psig
°F
Superheat
Subcooling

Detail

Pressure-temperature charts

All values in psig (gauge pressure at sea level). Italic negative values are inches of vacuum territory — below atmospheric. Generated from NIST-referenced equations of state; see method.

Vapor / dew point pressures — use these for superheat The suction line carries fully evaporated vapor, so the dew point column is the correct saturation reference.
°FR-410AR-454BR-32R-22R-134aR-404AR-407C
-4010.78.511.00.6-7.34.3-2.3
-3514.011.514.42.6-6.16.8-0.4
-3017.714.918.24.9-4.89.61.6
-2521.818.622.37.5-3.412.73.9
-2026.222.726.810.2-1.816.06.5
-1531.027.131.713.2-0.019.69.3
-1036.332.037.116.51.923.612.3
-542.037.242.920.14.127.915.7
048.242.949.224.06.532.619.4
554.949.156.128.39.137.723.5
1062.255.763.532.811.943.127.9
1570.062.971.537.815.049.032.7
2078.470.680.043.118.455.337.9
2587.478.989.248.822.162.143.5
3097.087.899.155.026.169.349.6
35107.397.3109.761.530.477.156.1
40118.4107.5121.068.635.085.463.2
45130.1118.3133.076.140.094.270.7
50142.6129.9145.884.145.4103.678.8
55156.0142.2159.592.651.2113.687.5
60170.1155.3174.1101.657.4124.296.8
65185.1169.2189.5111.264.0135.5106.7
70201.1183.9205.8121.471.1147.4117.3
75217.9199.5223.2132.278.7160.1128.5
80235.7216.0241.5143.686.7173.4140.5
85254.6233.5260.9155.795.2187.5153.2
90274.5251.9281.3168.4104.3202.4166.7
95295.4271.4302.9181.8114.0218.1181.0
100317.6291.9325.7195.9124.2234.7196.1
105340.9313.5349.6210.8135.0252.1212.1
110365.4336.3374.9226.4146.4270.4229.0
115391.2360.3401.4242.8158.4289.7246.9
120418.3385.5429.3260.0171.2309.9265.8
125446.8412.1458.7278.0184.6331.2285.6
130476.8440.0489.5296.9198.7353.6306.6
135508.4469.3521.8316.7213.6377.1328.7
140541.5500.2555.8337.4229.2401.7352.0

Blends shown: R-410A, R-454B, R-404A, R-407C. Pure refrigerants (R-32, R-22, R-134a) have identical vapor and liquid pressures.

Liquid / bubble point pressures — use these for subcooling Blends only. For R-32, R-22 and R-134a the liquid pressure equals the vapor pressure above — a pure refrigerant has one saturation pressure.
°FR-410AR-454BR-404AR-407C
-4010.89.84.92.8
-3514.113.07.55.1
-3017.816.610.37.7
-2521.920.513.410.6
-2026.324.816.813.7
-1531.229.420.517.2
-1036.534.524.620.9
-542.240.028.925.0
048.445.933.729.5
555.252.438.834.3
1062.459.344.339.5
1570.266.850.245.2
2078.774.856.651.2
2587.783.563.457.7
3097.492.770.764.7
35107.7102.678.672.2
40118.8113.286.980.2
45130.6124.595.888.8
50143.2136.4105.397.9
55156.5149.2115.3107.6
60170.7162.7126.0117.9
65185.8177.1137.3128.9
70201.7192.3149.3140.5
75218.6208.4162.0152.8
80236.5225.4175.4165.8
85255.4243.4189.6179.6
90275.3262.3204.5194.1
95296.4282.3220.2209.4
100318.5303.3236.8225.5
105341.9325.4254.2242.4
110366.4348.6272.6260.2
115392.3373.0291.8278.9
120419.5398.6312.1298.6
125448.0425.5333.4319.2
130478.0453.6355.7340.7
135509.5379.1363.3
140542.6514.0403.7387.0

Superheat and subcooling in one paragraph each

Superheat is how many degrees the refrigerant vapor has been heated above the temperature at which it finished boiling. You measure it on the suction line. It exists to guarantee that everything reaching the compressor is vapor, because liquid does not compress and a compressor asked to compress liquid destroys itself.

Subcooling is how many degrees the liquid has been cooled below the temperature at which it finished condensing. You measure it on the liquid line. It exists to guarantee that what arrives at the metering device is solid liquid with no bubbles, because a metering device fed flash gas cannot meter properly.

Both are the same idea measured from opposite ends: how far is this refrigerant from the state where it would start changing phase? Superheat measures distance above the boiling line. Subcooling measures distance below the condensing line.

Why this chart has two pressure columns

Most PT charts online give one pressure per temperature. That is correct for a pure refrigerant and wrong for a blend.

A pure substance — R-22, R-32, R-134a — boils at a single temperature for a given pressure. Water at sea level boils at 212 °F, start to finish. One number.

A zeotropic blend is a mixture of refrigerants with different boiling points, and it does not do that. As it evaporates, the more volatile component boils off first, the remaining liquid becomes richer in the less volatile component, and the boiling temperature climbs as evaporation proceeds. It starts boiling at the bubble point and finishes at the dew point. The spread between them is called glide.

RefrigerantTypeGlidePractical consequence
R-22Pure0.0 °FOne column, no ambiguity
R-32Pure0.0 °FOne column, no ambiguity
R-134aPure0.0 °FOne column, no ambiguity
R-410ANear-azeotropic0.2 °FNegligible — treat as single-column in practice
R-404ANear-azeotropic0.9 °FSmall but real
R-454BZeotropic2.7 °FUse the correct column — matters at this magnitude
R-407CZeotropic11.1 °FWrong column = 11 degrees of error. Enormous

Glide is not a fixed property — it varies with temperature and with how much of the charge has evaporated. The values above are computed at 40 °F saturated conditions, which is representative of a cooling evaporator.

The rule: superheat uses the vapor / dew column. Subcooling uses the liquid / bubble column. On R-410A you can be sloppy about this and lose two tenths of a degree. On R-407C you cannot.

R-454B is not R-410A, and your gauges will lie to you

New residential and light commercial equipment has moved to A2L refrigerants under the HFC phasedown — principally R-454B (roughly 68.9% R-32 / 31.1% R-1234yf by mass) and R-32. For a technician whose instincts were built on R-410A, the pressures are close enough to feel familiar and different enough to produce wrong answers.

Saturation tempR-410AR-454BDifferenceR-32
20 °F78.4 psig70.6 psig−7.780.0 psig
40 °F118.4107.5−10.9121.0
50 °F142.6129.9−12.7145.8
110 °F365.4336.3−29.1374.9
130 °F476.8440.0−36.9489.5

R-454B runs lower than R-410A everywhere, and the gap widens with temperature. R-32 runs slightly higher. Now read it the way you actually work — gauge first:

Gauge readsOn R-410A that'sOn R-454B that'sOn R-32 that's
118 psig39.8 °F44.8 °F38.7 °F
300 psig96.1 °F101.9 °F94.3 °F
400 psig116.7 °F122.8 °F114.7 °F
Reading an R-454B system on an R-410A chart puts your saturation temperature about 5 °F too low — which makes superheat read about 5 °F too high. On a fixed-orifice system that is the difference between "slightly undercharged, add refrigerant" and "correctly charged, leave it alone." Adding charge to a correct system on the strength of a wrong chart is how you end up with a flooded compressor.

A2L refrigerants are mildly flammable. That changes leak detection, ventilation, storage, recovery equipment and service procedure, and it is governed by codes and manufacturer instructions that are outside the scope of a pressure chart. Do not treat A2L service as R-410A service with a different number.

Which one tells you about the charge?

This depends entirely on the metering device, and getting it backwards produces confident wrong conclusions.

Fixed orifice or piston → charge by superheat

A fixed orifice has no feedback mechanism. It passes what pressure difference pushes through it. Superheat therefore floats with charge: add refrigerant and superheat falls, remove it and superheat rises. That responsiveness is exactly what makes it a usable charging indicator.

It also means superheat on a fixed-orifice system depends heavily on load — indoor wet bulb and outdoor dry bulb. This is why manufacturers publish a target superheat table rather than a single number, and why charging one of these on a mild day is unreliable.

TXV or EEV → charge by subcooling

A thermostatic or electronic expansion valve exists specifically to hold superheat constant. It modulates to maintain its setpoint regardless of charge, right up until it runs out of range. So on a properly functioning TXV system, superheat tells you the valve is working — it does not tell you the charge. Subcooling does, because surplus refrigerant backs up in the condenser and raises it.

A TXV system holding steady superheat with low subcooling is undercharged, and superheat will not warn you about it until the charge is low enough that the valve loses control. This is the single most common misdiagnosis in the field.

Target values — where they come from

Use the equipment's data plate or charging chart. Not a rule of thumb, and not this page. Targets are specific to the equipment, the line set, the metering device and the operating conditions, and manufacturers publish them for exactly that reason.

The calculator above flags broad ranges only — roughly 8–12 °F subcooling and 8–14 °F evaporator superheat are common design targets — and they are there to catch gross errors, not to charge a system. A reading far outside them means something is wrong. A reading inside them does not mean the charge is right.

What the numbers point at when they're wrong

SuperheatSubcoolingUsually means
HighLowUndercharge, or a leak
LowHighOvercharge
HighHighRestriction between condenser and evaporator — often the metering device or a plugged filter drier
LowLowLow load, poor evaporator airflow, or an oversized/stuck-open metering device
Near zeroStop. Liquid is reaching the compressor

Note that low superheat and low subcooling together frequently means airflow, not refrigerant — a dirty filter, a collapsed flex duct, an undersized return. Which is a good reason to check static pressure before you connect gauges at all. If that describes the system in front of you, the duct sizing and static pressure calculator is the more useful tool.

Measurement errors that ruin the reading

What this page does not do

Method and validation

Where the data comes from

Saturation properties were generated with CoolProp 8.0 using multiparameter Helmholtz-energy equations of state — the same formulations underlying NIST REFPROP. Values are not transcribed from another chart. Pressures are converted to gauge by subtracting standard atmospheric pressure (14.696 psi).

For blends, dew point pressure is evaluated at vapor quality Q = 1 and bubble point pressure at Q = 0, giving the two columns published above.

R-454B

R-454B is not a predefined fluid in CoolProp, so it was constructed as a mixture of R32 and R1234yf at mass fractions 0.689 / 0.311.

To validate that this approach is sound, R-410A was rebuilt the same way 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, confirming the mixture construction reproduces the predefined blend exactly.

Validation against published values

RefrigerantTempComputedPublished
R-410A40 °F118.4 psig~118.5
R-410A45 °F130.1~130.7
R-2240 °F68.6~68.5
R-2245 °F76.1~76.0
R-134a40 °F35.0~35.0
R-404A40 °F85.4~84.3
R-3240 °F121.0~120.4

Interpolation in the calculator is linear between 1 °F tabulated steps over the range −60 to 150 °F. Across that spacing the saturation curve is close enough to linear that interpolation error is well under 0.1 °F.

Limitations