Saturation tables by temperature and by pressure, superheated vapor table, p–h and T–s diagrams and constants of R507A, computed with CoolProp. Any other state of R507A, from any two properties, in the State Explorer or the Worksheet.
R507A is a mixture: at a temperature, it starts boiling (bubble) and ends (dew) at different pressures.
Saturated R507A, 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
28.367
28.358
0.00072072
0.58994
110.58
211.23
321.8
0.62495
1.6648
-60
51.054
51.05
0.00073664
0.34045
122.72
205.17
327.88
0.68322
1.6458
-50
86.378
86.373
0.00075361
0.20796
135
198.94
333.94
0.73941
1.631
-40
138.68
138.66
0.00077185
0.13316
147.47
192.47
339.94
0.7939
1.6195
-30
212.89
212.83
0.00079167
0.088656
160.17
185.65
345.81
0.84696
1.6105
-20
314.52
314.38
0.00081342
0.060955
173.12
178.38
351.5
0.89885
1.6036
-10
449.54
449.28
0.00083759
0.043025
186.38
170.57
356.95
0.94979
1.598
0
624.39
623.97
0.00086486
0.031014
200
162.06
362.06
1
1.5933
10
846.01
845.36
0.00089619
0.02272
214.04
152.69
366.73
1.0498
1.5891
20
1121.8
1120.9
0.00093308
0.01683
228.61
142.21
370.82
1.0995
1.5846
30
1460
1458.7
0.00097796
0.012537
243.83
130.28
374.11
1.1495
1.5792
40
1869.5
1867.9
0.0010352
0.0093214
259.95
116.29
376.24
1.2004
1.5718
50
2361.2
2359.2
0.001114
0.0068323
277.4
99.13
376.53
1.2536
1.5604
60
2948.9
2946.9
0.0012405
0.0047931
297.26
75.947
373.2
1.312
1.54
Saturation table by pressure
At a pressure, R507A starts boiling (bubble) and ends (dew) at different temperatures.
Saturated R507A, 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
-69.096
-69.091
0.00072212
0.5597
111.67
210.69
322.35
0.63032
1.6629
50
-60.375
-60.374
0.00073602
0.34714
122.26
205.4
327.66
0.68108
1.6465
100
-47.015
-47.013
0.0007589
0.18121
138.7
197.04
335.74
0.75585
1.6272
200
-31.518
-31.512
0.00078854
0.09407
158.22
186.71
344.93
0.83899
1.6117
300
-21.26
-21.249
0.00081056
0.063776
171.47
179.33
350.81
0.89237
1.6043
500
-6.85
-6.832
0.00084581
0.038707
190.63
167.98
358.61
0.96568
1.5965
1000
15.84
15.869
0.00091693
0.019032
222.48
146.74
369.21
1.0788
1.5865
2000
42.834
42.871
0.0010547
0.0085451
264.73
111.82
376.56
1.2152
1.5691
3000
60.791
60.82
0.0012546
0.0046363
299.01
73.624
372.64
1.3171
1.5375
Diagrams
p–h diagram of R507A, with isothermsT–s diagram of R507A, with isobars
Superheated vapor table
At each pressure, from its saturated vapor (Sat.) to higher temperatures.
Superheated R507A at 50 kPa (Tsat -60.374 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.34714
310.3
327.66
1.6465
-50
0.3661
317.03
335.34
1.6817
-25
0.41069
333.88
354.42
1.7627
0
0.45432
351.74
374.46
1.8396
25
0.49743
370.67
395.55
1.9135
50
0.54024
390.69
417.7
1.9848
75
0.58287
411.77
440.91
2.054
100
0.62536
433.87
465.14
2.1212
125
0.66777
456.96
490.35
2.1865
150
0.71012
480.99
516.5
2.2502
175
0.75241
505.91
543.53
2.3123
200
0.79467
531.67
571.4
2.3728
225
0.8369
558.22
600.07
2.4318
Superheated R507A at 100 kPa (Tsat -47.013 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.18121
317.62
335.74
1.6272
-25
0.20191
332.91
353.1
1.7005
0
0.22455
351.04
373.5
1.7788
25
0.24665
370.14
394.81
1.8534
50
0.26845
390.27
417.11
1.9252
75
0.29005
411.42
440.42
1.9947
100
0.31152
433.58
464.73
2.0621
125
0.33291
456.71
490
2.1276
150
0.35423
480.77
516.19
2.1914
175
0.3755
505.71
543.26
2.2535
200
0.39673
531.49
571.16
2.3141
225
0.41794
558.06
599.85
2.3732
Superheated R507A at 200 kPa (Tsat -31.512 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.09407
326.12
344.93
1.6117
-25
0.097393
330.91
350.38
1.634
0
0.1096
349.61
371.53
1.7152
25
0.12123
369.06
393.31
1.7914
50
0.13253
389.41
415.92
1.8642
75
0.14363
410.71
439.44
1.9343
100
0.1546
432.98
463.9
2.0022
125
0.16547
456.19
489.28
2.068
150
0.17628
480.31
515.57
2.132
175
0.18704
505.3
542.71
2.1943
200
0.19777
531.12
570.68
2.255
225
0.20846
557.72
599.42
2.3142
Superheated R507A at 500 kPa (Tsat -6.832 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.038707
339.25
358.61
1.5965
0
0.040334
344.92
365.09
1.6205
25
0.045834
365.62
388.54
1.7026
50
0.050907
386.73
412.18
1.7788
75
0.055739
408.53
436.4
1.851
100
0.060421
431.15
461.36
1.9202
125
0.065001
454.61
487.11
1.987
150
0.069511
478.93
513.68
2.0517
175
0.073968
504.07
541.06
2.1145
200
0.078385
530.02
569.21
2.1756
225
0.082771
556.72
598.11
2.2352
Superheated R507A at 1 MPa (Tsat 15.869 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.019032
350.18
369.21
1.5865
25
0.02037
358.86
379.23
1.6206
50
0.023552
381.79
405.34
1.7048
75
0.026369
404.64
431.01
1.7813
100
0.028991
427.94
456.93
1.8532
125
0.031492
451.89
483.38
1.9218
150
0.033912
476.56
510.48
1.9878
175
0.036274
501.99
538.26
2.0516
200
0.038593
528.15
566.74
2.1134
225
0.04088
555.03
595.91
2.1735
Superheated R507A at 2 MPa (Tsat 42.871 °C)
T °C
v m³/kg
u kJ/kg
h kJ/kg
s kJ/(kg·K)
Sat.
0.0085451
359.47
376.56
1.5691
50
0.0093623
368.4
387.12
1.6021
75
0.011494
395.46
418.45
1.6956
100
0.013192
420.81
447.19
1.7753
125
0.0147
446.03
475.43
1.8486
150
0.016099
471.58
503.78
1.9176
175
0.017426
497.65
532.5
1.9836
200
0.018704
524.31
561.71
2.047
225
0.019944
551.59
591.47
2.1083
Enthalpy and entropy are measured from R507A's own reference state (CoolProp's default). The textbooks' refrigerant tables use ASHRAE's: in the Worksheet, write reference ASHRAE.