Mixture of 1-Propanol + 1-Propanol, 2-methyl-

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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-Propanol, 2-methyl-

Name
1-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2)3-5/h4-5H,3H2,1-2H3
InChI Key
ZXEKIIBDNHEJCQ-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)CO
Mol. Weight (g/mol)
74.12
CAS
78-83-1
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.1038 0.0021
293.15 0.1962 0.0023
293.15 0.2944 0.0024
293.15 0.4058 0.0026
293.15 0.5040 0.0028
293.15 0.6041 0.0030
293.15 0.7019 0.0032
293.15 0.8072 0.0035
303.15 0.1038 0.0016
303.15 0.1962 0.0017
303.15 0.2944 0.0017
303.15 0.4058 0.0019
303.15 0.5040 0.0020
303.15 0.6041 0.0021
303.15 0.7019 0.0023
303.15 0.8072 0.0024
303.15 0.8996 0.0026
313.15 0.1038 0.0011
313.15 0.1962 0.0011
313.15 0.2944 0.0012
313.15 0.4058 0.0013
313.15 0.5040 0.0014
313.15 0.6041 0.0015
313.15 0.7019 0.0016
313.15 0.8072 0.0018
313.15 0.8996 0.0019
323.15 0.1038 0.0008
323.15 0.1962 0.0009
323.15 0.2944 0.0009
323.15 0.4058 0.0010
323.15 0.5040 0.0011
323.15 0.6041 0.0011
323.15 0.7019 0.0012
323.15 0.8072 0.0013
323.15 0.8996 0.0014
333.15 0.1038 0.0005
333.15 0.1962 0.0005
333.15 0.2944 0.0006
333.15 0.4058 0.0006
333.15 0.5040 0.0007
333.15 0.6041 0.0008
333.15 0.7019 0.0008
333.15 0.8072 0.0009
333.15 0.8996 0.0010

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.1038 0.0021
293.15 0.1962 0.0023
293.15 0.2944 0.0024
293.15 0.4058 0.0026
293.15 0.5040 0.0028
293.15 0.6041 0.0030
293.15 0.7019 0.0032
293.15 0.8072 0.0035
303.15 0.1038 0.0016
303.15 0.1962 0.0017
303.15 0.2944 0.0017
303.15 0.4058 0.0019
303.15 0.5040 0.0020
303.15 0.6041 0.0021
303.15 0.7019 0.0023
303.15 0.8072 0.0024
303.15 0.8996 0.0026
313.15 0.1038 0.0011
313.15 0.1962 0.0011
313.15 0.2944 0.0012
313.15 0.4058 0.0013
313.15 0.5040 0.0014
313.15 0.6041 0.0015
313.15 0.7019 0.0016
313.15 0.8072 0.0018
313.15 0.8996 0.0019
323.15 0.1038 0.0008
323.15 0.1962 0.0009
323.15 0.2944 0.0009
323.15 0.4058 0.0010
323.15 0.5040 0.0011
323.15 0.6041 0.0011
323.15 0.7019 0.0012
323.15 0.8072 0.0013
323.15 0.8996 0.0014
333.15 0.1038 0.0005
333.15 0.1962 0.0005
333.15 0.2944 0.0006
333.15 0.4058 0.0006
333.15 0.5040 0.0007
333.15 0.6041 0.0008
333.15 0.7019 0.0008
333.15 0.8072 0.0009
333.15 0.8996 0.0010

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.1038 803.39
293.15 0.1962 803.24
293.15 0.2944 803.09
293.15 0.4058 802.91
293.15 0.5040 802.75
293.15 0.6041 802.58
293.15 0.7019 802.41
293.15 0.8072 802.21
303.15 0.1038 795.39
303.15 0.1962 795.27
303.15 0.2944 795.15
303.15 0.4058 795.01
303.15 0.5040 794.88
303.15 0.6041 794.74
303.15 0.7019 794.59
303.15 0.8072 794.41
303.15 0.8996 794.24
313.15 0.1038 787.25
313.15 0.1962 787.16
313.15 0.2944 787.07
313.15 0.4058 786.96
313.15 0.5040 786.86
313.15 0.6041 786.74
313.15 0.7019 786.61
313.15 0.8072 786.45
313.15 0.8996 786.29
323.15 0.1038 778.91
323.15 0.1962 778.85
323.15 0.2944 778.79
323.15 0.4058 778.71
323.15 0.5040 778.62
323.15 0.6041 778.52
323.15 0.7019 778.41
323.15 0.8072 778.26
323.15 0.8996 778.11
333.15 0.1038 770.34
333.15 0.1962 770.31
333.15 0.2944 770.27
333.15 0.4058 770.2
333.15 0.5040 770.13
333.15 0.6041 770.04
333.15 0.7019 769.94
333.15 0.8072 769.8
333.15 0.8996 769.64

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.1038 803.39
293.15 0.1962 803.24
293.15 0.2944 803.09
293.15 0.4058 802.91
293.15 0.5040 802.75
293.15 0.6041 802.58
293.15 0.7019 802.41
293.15 0.8072 802.21
303.15 0.1038 795.39
303.15 0.1962 795.27
303.15 0.2944 795.15
303.15 0.4058 795.01
303.15 0.5040 794.88
303.15 0.6041 794.74
303.15 0.7019 794.59
303.15 0.8072 794.41
303.15 0.8996 794.24
313.15 0.1038 787.25
313.15 0.1962 787.16
313.15 0.2944 787.07
313.15 0.4058 786.96
313.15 0.5040 786.86
313.15 0.6041 786.74
313.15 0.7019 786.61
313.15 0.8072 786.45
313.15 0.8996 786.29
323.15 0.1038 778.91
323.15 0.1962 778.85
323.15 0.2944 778.79
323.15 0.4058 778.71
323.15 0.5040 778.62
323.15 0.6041 778.52
323.15 0.7019 778.41
323.15 0.8072 778.26
323.15 0.8996 778.11
333.15 0.1038 770.34
333.15 0.1962 770.31
333.15 0.2944 770.27
333.15 0.4058 770.2
333.15 0.5040 770.13
333.15 0.6041 770.04
333.15 0.7019 769.94
333.15 0.8072 769.8
333.15 0.8996 769.64

Sources