Refrigerant · HFC

R-143a pressure-temperature chart and data

Trifluoroethane. Safety class A2L, GWP 4,470. Blend component of R-404A and R-507A. Not charged alone.

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R-143a data sheet

NameTrifluoroethane
TypeHFC
Safety classA2L — lower toxicity, mildly flammable (burns slowly)
Ozone depletion (ODP)0
Global warming (GWP, 100 yr)4,470
Boils at 1 atm-53 °F (-47.2 °C)
Critical temperature162.9 °F (72.7 °C)
Temperature glidenone / very small
Low side at 5 °F evaporating40.0 psig (276 kPa)
High side at 86 °F condensing193 psig (1333 kPa)
Old cylinder colournone assigned
OilPOE
Used forBlend component of R-404A and R-507A. Not charged alone.

Pressures are saturation values from reference equations of state. Real pressures change with load and airflow. GWP is the IPCC AR4 100-year value (blends calculated from their ingredients). Cylinder colours were an old AHRI code; since 2020 new cylinders are all one colour with the name on the label, so always read the label, never go by colour.

R-143a pressure / temperature chart

°F°CpsigkPa
-60-51.1V 5.1-17
-59-50.6V 4.4-15
-58-50.0V 3.7-13
-57-49.4V 3.0-10
-56-48.9V 2.3-8
-55-48.3V 1.5-5
-54-47.8V 0.8-3
-53-47.20.00
-52-46.70.43
-51-46.10.86
-50-45.61.28
-49-45.01.611
-48-44.42.014
-47-43.92.517
-46-43.32.920
-45-42.83.423
-44-42.23.826
-43-41.74.330
-42-41.14.833
-41-40.65.336
-40-40.05.840
-39-39.46.343
-38-38.96.847
-37-38.37.350
-36-37.87.854
-35-37.28.458
-34-36.78.962
-33-36.19.566
-32-35.610.170
-31-35.010.774
-30-34.411.378
-29-33.911.982
-28-33.312.586
-27-32.813.191
-26-32.213.895
-25-31.714.4100
-24-31.115.1104
-23-30.615.8109
-22-30.016.5114
-21-29.417.2118
-20-28.917.9123
-19-28.318.6128
-18-27.819.4133
-17-27.220.1139
-16-26.720.9144
-15-26.121.6149
-14-25.622.4155
-13-25.023.2160
-12-24.424.0166
-11-23.924.9171
-10-23.325.7177
-9-22.826.6183
-8-22.227.4189
-7-21.728.3195
-6-21.129.2201
-5-20.630.1208
-4-20.031.0214
-3-19.432.0220
-2-18.932.9227
-1-18.333.9234
0-17.834.9241
1-17.235.9247
2-16.736.9254
3-16.137.9262
4-15.639.0269
5-15.040.0276
6-14.441.1283
7-13.942.2291
8-13.343.3299
9-12.844.4306
10-12.245.6314
11-11.746.7322
12-11.147.9330
13-10.649.1339
14-10.050.3347
15-9.451.5355
16-8.952.8364
17-8.354.0373
18-7.855.3381
19-7.256.6390
20-6.757.9399
21-6.159.3409
22-5.660.6418
23-5.062.0427
24-4.463.4437
25-3.964.8447
26-3.366.2457
27-2.867.7466
28-2.269.1477
29-1.770.6487
30-1.172.1497
31-0.673.6508
320.075.2518
330.676.7529
341.178.3540
351.779.9551
362.281.6562
372.883.2574
383.384.9585
393.986.6597
404.488.3609
415.090.0621
425.691.8633
436.193.5645
446.795.3657
457.297.2670
467.899.0683
478.3101695
488.9103708
499.4105722
5010.0107735
5110.6109748
5211.1111762
5311.7113776
5412.2115790
5512.8117804
5613.3119818
5713.9121833
5814.4123848
5915.0125862
6015.6127877
6116.1129893
6216.7132908
6317.2134923
6417.8136939
6518.3139955
6618.9141971
6719.4143987
6820.01461004
6920.61481020
7021.11501037
7121.71531054
7222.21551071
7322.81581089
7423.31601106
7523.91631124
7624.41661142
7725.01681160
7825.61711179
7926.11741197
8026.71761216
8127.21791235
8227.81821254
8328.31851273
8428.91881293
8529.41901313
8630.01931333
8730.61961353
8831.11991373
8931.72021394
9032.22051415
9132.82081436
9233.32111457
9333.92141479
9434.42181500
9535.02211522
9635.62241544
9736.12271567
9836.72311589
9937.22341612
10037.82371635
10138.32411659
10238.92441682
10339.42471706
10440.02511730
10540.62541754
10641.12581779
10741.72621804
10842.22651829
10942.82691854
11043.32731879
11143.92761905
11244.42801931
11345.02841958
11445.62881984
11546.12922011
11646.72962038
11747.23002065
11847.83042093
11948.33082121
12048.93122149
12149.43162177
12250.03202206
12350.63242235
12451.13282264
12551.73332294
12652.23372324
12752.83412354
12853.33462384
12953.93502415
13054.43552446

V = vacuum in inches of mercury. Saturation pressure in psig at sea level, calculated from reference equations of state. The chart gives the boiling temperature at that pressure, not the pipe temperature. Air in the system adds pressure and throws it off.

R-143a pressure in psig, psia, kPa and bar

°F°CpsigpsiakPa gaugekPa absolutebar absolute
-60-51.1V 5.112.2-17840.84
-55-48.3V 1.513.9-5960.96
-50-45.61.215.981101.10
-45-42.83.418.1231251.25
-40-40.05.820.5401411.41
-35-37.28.423.1581591.59
-30-34.411.326.0781791.79
-25-31.714.429.11002012.01
-20-28.917.932.61232252.25
-15-26.121.636.31492502.50
-10-23.325.740.41772792.79
-5-20.630.144.82083093.09
0-17.834.949.62413423.42
5-15.040.054.72763773.77
10-12.245.660.33144164.16
15-9.451.566.23554574.57
20-6.757.972.63995015.01
25-3.964.879.54475485.48
30-1.172.186.84975995.99
351.779.994.65516526.52
404.488.3103.06097107.10
457.297.2111.86707717.71
5010.0107121.37358368.36
5512.8117131.38049059.05
6015.6127142.08779799.79
6518.3139153.2955105610.56
7021.1150165.11037113911.39
7523.9163177.71124122512.25
8026.7176191.01216131713.17
8529.4190205.11313141414.14
9032.2205219.91415151615.16
9535.0221235.51522162416.24
10037.8237251.91635173717.37
10540.6254269.11754185618.56
11043.3273287.31879198119.81
11546.1292306.32011211221.12
12048.9312326.42149225022.50
12551.7333347.42294239523.95
13054.4355369.42446254725.47

V = vacuum in inches of mercury. Absolute pressure = gauge + 14.7 psi at sea level; use absolute pressure for gas-law work. For blends the dew column is the vapour (suction) side and the bubble column the liquid side.

Other refrigerants

R-11 R-12 R-22 R-23 R-32 R-123 R-125 R-134a R-152a R-170 R-245fa R-290 R-401A R-401B R-404A R-407A R-407C R-407F R-408A R-409A R-410A R-417A R-422A R-422D R-427A R-448A R-449A R-450A R-452A R-452B R-454A R-454B R-454C R-455A R-500 R-502 R-507A R-508B R-513A R-600 R-600a R-717 R-744 R-1233zd(E) R-1234yf R-1234ze(E) R-1270

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Calculation aids and reference figures for licensed technicians. Always follow the manufacturer’s data plate and manual for the exact model, and local codes. Gas, electrical and refrigerant work must be done by a qualified, licensed person. Pressures are typical saturation values and change with load and airflow.