Saturation tables by temperature and by pressure, superheated vapor table, p–h and T–s diagrams and constants of R410A, computed with CoolProp. Any other state of R410A, from any two properties, in the State Explorer or the Worksheet.
R410A is a mixture: at a temperature, it starts boiling (bubble) and ends (dew) at different pressures.
Saturated R410A, by temperature
T °C
P bubble kPa
P dew kPa
vf m³/kg
vg m³/kg
hf kJ/kg
hfg kJ/kg
hg kJ/kg
sf kJ/(kg·K)
sg kJ/(kg·K)
-70
35.621
35.446
0.0007109
0.64169
101.24
288.02
389.25
0.58587
2.0038
-60
64.238
63.963
0.00072663
0.36904
114.79
279.97
394.76
0.6509
1.9646
-50
108.98
108.55
0.00074348
0.22448
128.45
271.61
400.05
0.71335
1.9306
-40
175.5
174.85
0.00076166
0.14307
142.25
262.84
405.08
0.77362
1.9011
-30
270.31
269.35
0.00078145
0.094796
156.24
253.56
409.8
0.83208
1.875
-20
400.69
399.31
0.0008032
0.064866
170.48
243.66
414.14
0.88907
1.8517
-10
574.6
572.68
0.0008274
0.045574
185.04
233
418.04
0.94492
1.8304
0
800.71
798.08
0.00085474
0.032707
200
221.39
421.39
1
1.8106
10
1088.3
1084.8
0.00088616
0.02386
215.45
208.6
424.05
1.0546
1.7914
20
1447.5
1442.9
0.00092314
0.017606
231.52
194.32
425.84
1.1093
1.7722
30
1889.2
1883.4
0.00096799
0.013068
248.38
178.08
426.46
1.1644
1.7519
40
2425.6
2418.6
0.0010249
0.0096865
266.32
159.12
425.45
1.2209
1.7291
50
3071.1
3063
0.0011026
0.0070848
285.88
136.04
421.92
1.2802
1.7013
60
3842.7
3834.8
0.0012264
0.0049763
308.48
105.21
413.7
1.3464
1.6622
70
4763.9
4761.7
0.0016158
0.0028811
344.34
44.046
388.39
1.4484
1.5768
Saturation table by pressure
At a pressure, R410A starts boiling (bubble) and ends (dew) at different temperatures.
Saturated R410A, by pressure
P kPa
T bubble °C
T dew °C
vf m³/kg
vg m³/kg
hf kJ/kg
hfg kJ/kg
hg kJ/kg
sf kJ/(kg·K)
sg kJ/(kg·K)
30
-72.71
-72.63
0.00070681
0.75018
97.576
290.2
387.77
0.56775
2.0152
50
-64.387
-64.31
0.0007196
0.46491
108.84
283.58
392.41
0.62272
1.9808
100
-51.7
-51.622
0.00074053
0.24251
126.12
273.09
399.21
0.7029
1.9358
200
-37.074
-36.991
0.00076727
0.12593
146.32
260.22
406.54
0.79089
1.8929
300
-27.439
-27.352
0.00078681
0.085487
159.86
251.13
410.99
0.84679
1.8686
500
-13.959
-13.864
0.00081749
0.052088
179.24
237.36
416.59
0.92292
1.8384
1000
7.167
7.273
0.00087678
0.025968
211.02
212.39
423.4
1.0392
1.7966
2000
32.228
32.347
0.00097942
0.012187
252.27
174.12
426.39
1.1769
1.7469
3000
48.983
49.099
0.0010933
0.007295
283.79
138.59
422.38
1.274
1.7041
Diagrams
p–h diagram of R410A, with isothermsT–s diagram of R410A, with isobars
Superheated vapor table
At each pressure, from its saturated vapor (Sat.) to higher temperatures.
Superheated R410A at 50 kPa (Tsat -64.31 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.46491
369.17
392.41
1.9808
-50
0.50071
378.01
403.05
2.03
-25
0.56106
393.58
421.63
2.1089
0
0.62016
409.77
440.77
2.1824
25
0.67864
426.77
460.7
2.2522
50
0.73677
444.66
481.5
2.3192
75
0.79467
463.48
503.22
2.3839
100
0.85243
483.23
525.86
2.4467
125
0.91009
503.91
549.41
2.5078
150
0.96768
525.48
573.87
2.5673
175
1.0252
547.93
599.19
2.6255
200
1.0827
571.22
625.36
2.6823
225
1.1402
595.32
652.33
2.7378
Superheated R410A at 100 kPa (Tsat -51.622 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.24251
374.96
399.21
1.9358
-25
0.2767
392.42
420.09
2.0249
0
0.30723
408.96
439.69
2.1001
25
0.3371
426.17
459.88
2.1708
50
0.3666
444.19
480.85
2.2383
75
0.39587
463.1
502.69
2.3034
100
0.42499
482.91
525.41
2.3664
125
0.45402
503.63
549.04
2.4277
150
0.48297
525.24
573.54
2.4874
175
0.51187
547.72
598.91
2.5456
200
0.54072
571.03
625.11
2.6025
225
0.56954
595.15
652.1
2.6581
Superheated R410A at 200 kPa (Tsat -36.991 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.12593
381.35
406.54
1.8929
-25
0.13434
389.93
416.8
1.9353
0
0.1507
407.31
437.45
2.0146
25
0.1663
424.95
458.21
2.0873
50
0.1815
443.24
479.54
2.156
75
0.19646
462.33
501.62
2.2218
100
0.21127
482.27
524.52
2.2853
125
0.22598
503.08
548.28
2.3469
150
0.24061
524.76
572.89
2.4068
175
0.25519
547.3
598.33
2.4653
200
0.26973
570.65
624.6
2.5223
225
0.28423
594.8
651.65
2.578
Superheated R410A at 500 kPa (Tsat -13.864 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.052088
390.55
416.59
1.8384
0
0.056512
401.83
430.09
1.8891
25
0.063698
421.09
452.94
1.9692
50
0.070378
440.29
475.48
2.0418
75
0.076785
459.96
498.35
2.11
100
0.083024
480.3
521.81
2.175
125
0.08915
501.4
545.98
2.2377
150
0.095198
523.31
570.9
2.2984
175
0.10119
546.01
596.61
2.3574
200
0.10714
569.51
623.07
2.4149
225
0.11305
593.77
650.29
2.4709
Superheated R410A at 1 MPa (Tsat 7.273 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.025968
397.43
423.4
1.7966
25
0.029251
413.77
443.02
1.8645
50
0.033228
434.96
468.19
1.9456
75
0.036839
455.79
492.63
2.0185
100
0.040248
476.89
517.14
2.0864
125
0.043528
498.53
542.06
2.1511
150
0.046722
520.83
567.55
2.2132
175
0.049855
543.84
593.69
2.2732
200
0.052943
567.57
620.52
2.3314
225
0.055995
592.03
648.03
2.3881
Superheated R410A at 2 MPa (Tsat 32.347 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.012187
402.02
426.39
1.7469
50
0.014348
422.12
450.81
1.8247
75
0.016739
446.46
479.94
1.9116
100
0.018802
469.55
507.15
1.9871
125
0.020692
492.48
533.87
2.0564
150
0.022476
515.7
560.65
2.1216
175
0.024189
539.38
587.76
2.1839
200
0.025851
563.64
615.34
2.2437
225
0.027475
588.52
643.47
2.3017
Enthalpy and entropy are measured from R410A's own reference state (CoolProp's default). The textbooks' refrigerant tables use ASHRAE's: in the Worksheet, write reference ASHRAE.