| Substance and % by volume in mixture |
Minimal working temperature
[oC] |
Temperature
[oC] |
Density
[kg/m3] |
Specific heat [kJ/kg.K] |
Thermal conductivity
[W/m.K] |
Dynamic viscosity
X10-3 [N.s/m2] |
Cinematic viscosity
X10-6 [m2/s] |
Monoethylenglycol
C2H4(OH)2
20 |
-10 |
-10
0
20
40
60
80
100
|
1038
1036
1030
1022
1014
1006
997
|
3.85
3.87
3.90
3.93
3.96
3.99
4.02
|
0.498
0.50
0.512
0.521
0.531
0.540
0.550
|
5.19
3.11
1.65
1.02
0.71
0.523
0.409
|
5
3
1.6
1.0
0.7
0.52
0.41
|
| 34 |
-20 |
-20
0
20
40
60
80
100
|
1069
1063
1055
1044
1033
1022
1010
|
3.51
3.56
3.62
3.68
3.73
3.78
3.84
|
0.462
0.466
0.470
0.473
0.475
0.478
0.480
|
11.76
4.89
2.32
1.57
1.01
0.695
0.515
|
11
4.6
2.2
1.5
0.98
0.68
0.51
|
| 52 |
-40 |
-40
-20
0
20
40
60
80
100
|
1108
1100
1092
1082
1069
1057
1045
1032
|
3.04
3.11
3.19
3.26
3.34
3.41
3.49
3.56
|
0.416
0.409
0.405
0.402
0.398
0.394
0.390
0.385
|
110.80
27.50
10.37
4.87
2.57
1.59
1.05
0.722
|
100
25
9.5
4.5
2.4
1.5
1.0
0.7
|
| 1,2-Propylenglycol
C3H6(OH)2
25 |
-10 |
-10
0
20
40
60
80
100
|
1032
1030
1024
1016
1003
986
979
|
3.93
3.95
3.98
4.00
4.03
4.05
4.08
|
0.466
0.470
0.478
0.491
0.505
0.519
0.533
|
10.22
6.18
2.86
1.42
0.903
0.671
0.509
|
9.9
6.0
2.8
1.4
0.90
0.68
0.52
|
| 38 |
-20 |
-20
0
20
40
60
80
100
|
1050
1045
1036
1025
1012
997
982
|
3.68
3.72
3.77
3.82
3.88
3.94
4.00
|
0.420
0.425
0.429
0.433
0.437
0.441
0.445
|
47.25
12.54
4.56
2.26
1.32
0.897
0.687
|
45
12
4.4
2.2
1.3
0.9
0.7
|
| 47 |
-30 |
-30
-20
-10
0
20
40
60
80
100
|
1066
1062
1058
1054
1044
1030
1015
999
984
|
3.45
3.49
3.52
3.56
3.62
3.69
3.76
3.82
3.89
|
0.397
0.396
0.395
0.395
0.394
0.393
0.392
0.391
0.390
|
160
74.3
31.74
18.97
6.264
2.987
1.624
1.10
0.807
|
150
70
30
18
6
2.9
1.6
1.1
0.82
|
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