Mixture of Pentane + Cyclohexane
Datasets
-
η - Viscosity, Pa*s (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Cyclohexane (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0437 |
0.0002 |
0.2145 |
0.0003 |
0.2955 |
0.0003 |
0.3753 |
0.0003 |
0.4595 |
0.0004 |
0.6125 |
0.0004 |
0.7048 |
0.0005 |
0.7791 |
0.0006 |
0.8514 |
0.0007 |
0.9254 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Cyclohexane (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0437 |
0.0002 |
0.2145 |
0.0003 |
0.2955 |
0.0003 |
0.3753 |
0.0003 |
0.4595 |
0.0004 |
0.6125 |
0.0004 |
0.7048 |
0.0005 |
0.7791 |
0.0006 |
0.8514 |
0.0007 |
0.9254 |
0.0008 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Pentane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.21 |
0.0000 |
10.60 |
293.20 |
0.0508 |
13.50 |
293.20 |
0.1411 |
18.30 |
293.20 |
0.1891 |
20.70 |
293.20 |
0.2466 |
23.40 |
293.20 |
0.2963 |
25.80 |
293.20 |
0.3544 |
28.50 |
293.20 |
0.4007 |
30.60 |
293.20 |
0.4505 |
32.90 |
293.20 |
0.5033 |
35.20 |
293.20 |
0.5512 |
37.10 |
293.20 |
0.6002 |
39.20 |
293.20 |
0.6460 |
41.10 |
293.20 |
0.7000 |
43.40 |
293.20 |
0.7483 |
45.50 |
293.20 |
0.8024 |
47.90 |
293.19 |
0.8466 |
49.80 |
293.20 |
0.9041 |
52.30 |
293.20 |
0.9512 |
54.40 |
293.20 |
1.0000 |
56.60 |
298.18 |
0.0000 |
13.40 |
298.17 |
0.0462 |
16.60 |
298.17 |
0.1018 |
20.20 |
298.17 |
0.1529 |
23.30 |
298.17 |
0.2029 |
26.30 |
298.16 |
0.2541 |
29.20 |
298.17 |
0.3047 |
32.10 |
298.17 |
0.3579 |
35.10 |
298.17 |
0.4017 |
37.50 |
298.18 |
0.4464 |
40.30 |
298.17 |
0.5013 |
42.90 |
298.18 |
0.5509 |
45.40 |
298.18 |
0.5990 |
47.70 |
298.18 |
0.6498 |
50.30 |
298.18 |
0.6996 |
52.80 |
298.18 |
0.7483 |
55.30 |
298.18 |
0.8013 |
58.00 |
298.18 |
0.8523 |
60.70 |
298.19 |
0.9019 |
63.30 |
298.18 |
0.9527 |
66.00 |
298.18 |
1.0000 |
68.50 |
303.18 |
0.0000 |
16.40 |
303.18 |
0.0517 |
20.60 |
303.18 |
0.0986 |
24.10 |
303.18 |
0.1515 |
27.90 |
303.18 |
0.2049 |
31.70 |
303.18 |
0.2549 |
35.20 |
303.18 |
0.2982 |
38.10 |
303.18 |
0.3514 |
41.70 |
303.18 |
0.4007 |
44.90 |
303.18 |
0.4443 |
47.80 |
303.18 |
0.4924 |
50.80 |
303.18 |
0.5491 |
54.10 |
303.18 |
0.6010 |
57.30 |
303.18 |
0.6541 |
60.60 |
303.18 |
0.7053 |
63.70 |
303.18 |
0.7504 |
66.50 |
303.18 |
0.8103 |
70.20 |
303.18 |
0.8529 |
72.90 |
303.18 |
0.9033 |
76.10 |
303.18 |
0.9485 |
78.90 |
303.18 |
1.0000 |
82.20 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Pentane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.21 |
0.0000 |
10.60 |
293.20 |
0.0508 |
13.50 |
293.20 |
0.1411 |
18.30 |
293.20 |
0.1891 |
20.70 |
293.20 |
0.2466 |
23.40 |
293.20 |
0.2963 |
25.80 |
293.20 |
0.3544 |
28.50 |
293.20 |
0.4007 |
30.60 |
293.20 |
0.4505 |
32.90 |
293.20 |
0.5033 |
35.20 |
293.20 |
0.5512 |
37.10 |
293.20 |
0.6002 |
39.20 |
293.20 |
0.6460 |
41.10 |
293.20 |
0.7000 |
43.40 |
293.20 |
0.7483 |
45.50 |
293.20 |
0.8024 |
47.90 |
293.19 |
0.8466 |
49.80 |
293.20 |
0.9041 |
52.30 |
293.20 |
0.9512 |
54.40 |
293.20 |
1.0000 |
56.60 |
298.18 |
0.0000 |
13.40 |
298.17 |
0.0462 |
16.60 |
298.17 |
0.1018 |
20.20 |
298.17 |
0.1529 |
23.30 |
298.17 |
0.2029 |
26.30 |
298.16 |
0.2541 |
29.20 |
298.17 |
0.3047 |
32.10 |
298.17 |
0.3579 |
35.10 |
298.17 |
0.4017 |
37.50 |
298.18 |
0.4464 |
40.30 |
298.17 |
0.5013 |
42.90 |
298.18 |
0.5509 |
45.40 |
298.18 |
0.5990 |
47.70 |
298.18 |
0.6498 |
50.30 |
298.18 |
0.6996 |
52.80 |
298.18 |
0.7483 |
55.30 |
298.18 |
0.8013 |
58.00 |
298.18 |
0.8523 |
60.70 |
298.19 |
0.9019 |
63.30 |
298.18 |
0.9527 |
66.00 |
298.18 |
1.0000 |
68.50 |
303.18 |
0.0000 |
16.40 |
303.18 |
0.0517 |
20.60 |
303.18 |
0.0986 |
24.10 |
303.18 |
0.1515 |
27.90 |
303.18 |
0.2049 |
31.70 |
303.18 |
0.2549 |
35.20 |
303.18 |
0.2982 |
38.10 |
303.18 |
0.3514 |
41.70 |
303.18 |
0.4007 |
44.90 |
303.18 |
0.4443 |
47.80 |
303.18 |
0.4924 |
50.80 |
303.18 |
0.5491 |
54.10 |
303.18 |
0.6010 |
57.30 |
303.18 |
0.6541 |
60.60 |
303.18 |
0.7053 |
63.70 |
303.18 |
0.7504 |
66.50 |
303.18 |
0.8103 |
70.20 |
303.18 |
0.8529 |
72.90 |
303.18 |
0.9033 |
76.10 |
303.18 |
0.9485 |
78.90 |
303.18 |
1.0000 |
82.20 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Cyclohexane (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0437 |
627.56 |
0.2145 |
653.09 |
0.2955 |
665.44 |
0.3753 |
677.59 |
0.4595 |
690.43 |
0.6125 |
713.75 |
0.7048 |
727.81 |
0.7791 |
739.14 |
0.8514 |
750.15 |
0.9254 |
761.85 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Cyclohexane (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0437 |
627.56 |
0.2145 |
653.09 |
0.2955 |
665.44 |
0.3753 |
677.59 |
0.4595 |
690.43 |
0.6125 |
713.75 |
0.7048 |
727.81 |
0.7791 |
739.14 |
0.8514 |
750.15 |
0.9254 |
761.85 |
Sources