Mixture of 1-Propanol + 1-Propanamine, N-propyl-

Excel

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

1-Propanamine, N-propyl-

Name
1-Propanamine, N-propyl-
InChI
InChI=1S/C6H15N/c1-3-5-7-6-4-2/h7H,3-6H2,1-2H3
InChI Key
WEHWNAOGRSTTBQ-UHFFFAOYSA-N
Formula
C6H15N
SMILES
CCCNCCC
Mol. Weight (g/mol)
101.19
CAS
142-84-7
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Azeotropic composition: mole fraction (2)
  2. Azeotropic pressure, kPa (4)

Azeotropic composition: mole fraction of 1-Propanol (1) [ref]

Temperature, K - Liquid Azeotropic composition: mole fraction of 1-Propanol (1) - Liquid
293.15 0.7646
298.15 0.7620
303.15 0.7504
308.15 0.7342
313.15 0.7194
318.15 0.6995

Azeotropic composition: mole fraction of 1-Propanol (1) [ref]

Temperature, K - Liquid Azeotropic composition: mole fraction of 1-Propanol (1) - Liquid
293.15 0.7646
298.15 0.7620
303.15 0.7504
308.15 0.7342
313.15 0.7194
318.15 0.6995

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid Azeotropic pressure, kPa - Liquid
293.15 1.88
298.15 2.62
303.15 3.61
308.15 4.90
313.15 6.55
318.15 8.67

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Gas Mole fraction of 1-Propanol (1) - Gas Vapor or sublimation pressure, kPa - Gas
293.15 0.0000 2.72
293.15 0.0500 2.66
293.15 0.1566 2.50
293.15 0.2332 2.43
293.15 0.3517 2.29
293.15 0.4317 2.19
293.15 0.5191 2.07
293.15 0.5816 1.97
293.15 0.6292 1.94
293.15 0.7172 1.88
293.15 0.7512 1.88
293.15 0.7725 1.89
293.15 0.8619 1.92
293.15 0.9530 1.98
293.15 1.0000 2.03
298.15 0.0000 3.60
298.15 0.0500 3.53
298.15 0.1566 3.36
298.15 0.2332 3.26
298.15 0.3517 3.10
298.15 0.4317 2.98
298.15 0.5191 2.83
298.15 0.5816 2.74
298.15 0.6292 2.69
298.15 0.7172 2.62
298.15 0.7512 2.61
298.15 0.7725 2.63
298.15 0.8619 2.67
298.15 0.9530 2.76
298.15 1.0000 2.81
303.15 0.0000 4.71
303.15 0.0500 4.61
303.15 0.1566 4.48
303.15 0.2332 4.34
303.15 0.3517 4.14
303.15 0.4317 4.01
303.15 0.5191 3.84
303.15 0.5816 3.73
303.15 0.6292 3.67
303.15 0.7172 3.61
303.15 0.7512 3.60
303.15 0.7725 3.61
303.15 0.8619 3.69
303.15 0.9530 3.81
303.15 1.0000 3.88
308.15 0.0000 6.12
308.15 0.0500 5.97
308.15 0.1566 5.79
308.15 0.2332 5.68
308.15 0.3517 5.47
308.15 0.4317 5.31
308.15 0.5191 5.16
308.15 0.5816 5.01
308.15 0.6292 4.94
308.15 0.7172 4.88
308.15 0.7512 4.88
308.15 0.7725 4.89
308.15 0.8619 5.01
308.15 0.9530 5.16
308.15 1.0000 5.25
313.15 0.0000 7.80
313.15 0.0500 7.67
313.15 0.1566 7.46
313.15 0.2332 7.36
313.15 0.3517 7.16
313.15 0.4317 7.01
313.15 0.5191 6.79
313.15 0.5816 6.66
313.15 0.6292 6.57
313.15 0.7172 6.54
313.15 0.7512 6.54
313.15 0.7725 6.56
313.15 0.8619 6.71
313.15 0.9530 6.92
313.15 1.0000 7.03
318.15 0.0000 9.89
318.15 0.0500 9.73
318.15 0.1566 9.54
318.15 0.2332 9.48
318.15 0.3517 9.29
318.15 0.4317 9.08
318.15 0.5191 8.87
318.15 0.5816 8.75
318.15 0.6292 8.67
318.15 0.7172 8.66
318.15 0.7512 8.67
318.15 0.7725 8.70
318.15 0.8619 8.88
318.15 0.9530 9.15
318.15 1.0000 9.31

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid Azeotropic pressure, kPa - Liquid
293.15 1.88
298.15 2.62
303.15 3.61
308.15 4.90
313.15 6.55
318.15 8.67

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Gas Mole fraction of 1-Propanol (1) - Gas Vapor or sublimation pressure, kPa - Gas
293.15 0.0000 2.72
293.15 0.0500 2.66
293.15 0.1566 2.50
293.15 0.2332 2.43
293.15 0.3517 2.29
293.15 0.4317 2.19
293.15 0.5191 2.07
293.15 0.5816 1.97
293.15 0.6292 1.94
293.15 0.7172 1.88
293.15 0.7512 1.88
293.15 0.7725 1.89
293.15 0.8619 1.92
293.15 0.9530 1.98
293.15 1.0000 2.03
298.15 0.0000 3.60
298.15 0.0500 3.53
298.15 0.1566 3.36
298.15 0.2332 3.26
298.15 0.3517 3.10
298.15 0.4317 2.98
298.15 0.5191 2.83
298.15 0.5816 2.74
298.15 0.6292 2.69
298.15 0.7172 2.62
298.15 0.7512 2.61
298.15 0.7725 2.63
298.15 0.8619 2.67
298.15 0.9530 2.76
298.15 1.0000 2.81
303.15 0.0000 4.71
303.15 0.0500 4.61
303.15 0.1566 4.48
303.15 0.2332 4.34
303.15 0.3517 4.14
303.15 0.4317 4.01
303.15 0.5191 3.84
303.15 0.5816 3.73
303.15 0.6292 3.67
303.15 0.7172 3.61
303.15 0.7512 3.60
303.15 0.7725 3.61
303.15 0.8619 3.69
303.15 0.9530 3.81
303.15 1.0000 3.88
308.15 0.0000 6.12
308.15 0.0500 5.97
308.15 0.1566 5.79
308.15 0.2332 5.68
308.15 0.3517 5.47
308.15 0.4317 5.31
308.15 0.5191 5.16
308.15 0.5816 5.01
308.15 0.6292 4.94
308.15 0.7172 4.88
308.15 0.7512 4.88
308.15 0.7725 4.89
308.15 0.8619 5.01
308.15 0.9530 5.16
308.15 1.0000 5.25
313.15 0.0000 7.80
313.15 0.0500 7.67
313.15 0.1566 7.46
313.15 0.2332 7.36
313.15 0.3517 7.16
313.15 0.4317 7.01
313.15 0.5191 6.79
313.15 0.5816 6.66
313.15 0.6292 6.57
313.15 0.7172 6.54
313.15 0.7512 6.54
313.15 0.7725 6.56
313.15 0.8619 6.71
313.15 0.9530 6.92
313.15 1.0000 7.03
318.15 0.0000 9.89
318.15 0.0500 9.73
318.15 0.1566 9.54
318.15 0.2332 9.48
318.15 0.3517 9.29
318.15 0.4317 9.08
318.15 0.5191 8.87
318.15 0.5816 8.75
318.15 0.6292 8.67
318.15 0.7172 8.66
318.15 0.7512 8.67
318.15 0.7725 8.70
318.15 0.8619 8.88
318.15 0.9530 9.15
318.15 1.0000 9.31

Sources