Mixture of 1-Propanol + Ethanol, 2-methoxy-

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

Ethanol, 2-methoxy-

Name
Ethanol, 2-methoxy-
InChI
InChI=1S/C3H8O2/c1-5-3-2-4/h4H,2-3H2,1H3
InChI Key
XNWFRZJHXBZDAG-UHFFFAOYSA-N
Formula
C3H8O2
SMILES
COCCO
Mol. Weight (g/mol)
76.09
CAS
109-86-4
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Datasets

  1. Mole fraction (2)
  2. ρl - Mass density, kg/m3 (2)
  3. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of 1-Propanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid Mole fraction of 1-Propanol (1) - Gas
0.0000 0.0000
0.1060 0.2450
0.1660 0.3510
0.1990 0.4030
0.2330 0.4510
0.2690 0.4970
0.3060 0.5420
0.3470 0.5860
0.3850 0.6230
0.4610 0.6900
0.5000 0.7210
0.5390 0.7500
0.5760 0.7750
0.6120 0.7990
0.6710 0.8350
0.7320 0.8690
0.7860 0.8970
0.8320 0.9210
0.8910 0.9490
0.9460 0.9750
1.0000 1.0000

Mole fraction of 1-Propanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid Mole fraction of 1-Propanol (1) - Gas
0.0000 0.0000
0.1060 0.2450
0.1660 0.3510
0.1990 0.4030
0.2330 0.4510
0.2690 0.4970
0.3060 0.5420
0.3470 0.5860
0.3850 0.6230
0.4610 0.6900
0.5000 0.7210
0.5390 0.7500
0.5760 0.7750
0.6120 0.7990
0.6710 0.8350
0.7320 0.8690
0.7860 0.8970
0.8320 0.9210
0.8910 0.9490
0.9460 0.9750
1.0000 1.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 81.5 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-methoxy- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0845 817.73
293.15 0.1559 829.58
293.15 0.2391 843.36
293.15 0.3146 855.77
293.15 0.4015 869.91
293.15 0.4790 882.45
293.15 0.5597 895.42
293.15 0.6365 907.69
293.15 0.7183 920.73
293.15 0.7939 932.73
293.15 0.8775 945.88
293.15 0.9553 957.99
303.15 0.0845 809.55
303.15 0.1559 821.29
303.15 0.2391 834.94
303.15 0.3146 847.26
303.15 0.4015 861.29
303.15 0.4790 873.74
303.15 0.5597 886.62
303.15 0.6365 898.82
303.15 0.7183 911.78
303.15 0.7939 923.71
303.15 0.8775 936.8
303.15 0.9553 948.84
313.15 0.0845 801.23
313.15 0.1559 812.86
313.15 0.2391 826.39
313.15 0.3146 838.61
313.15 0.4015 852.53
313.15 0.4790 864.89
313.15 0.5597 877.69
313.15 0.6365 889.81
313.15 0.7183 902.7
313.15 0.7939 914.56
313.15 0.8775 927.59
313.15 0.9553 939.57
323.15 0.0845 792.73
323.15 0.1559 804.25
323.15 0.2391 817.66
323.15 0.3146 829.78
323.15 0.4015 843.61
323.15 0.4790 855.88
323.15 0.5597 868.6
323.15 0.6365 880.65
323.15 0.7183 893.47
323.15 0.7939 905.28
323.15 0.8775 918.24
323.15 0.9553 930.18
333.15 0.0845 783.99
333.15 0.1559 795.42
333.15 0.2391 808.72
333.15 0.3146 820.75
333.15 0.4015 834.47
333.15 0.4790 846.68
333.15 0.5597 859.32
333.15 0.6365 871.31
333.15 0.7183 884.08
333.15 0.7939 895.83
333.15 0.8775 908.74
333.15 0.9553 920.63
343.15 0.0845 774.97
343.15 0.1559 786.31
343.15 0.2391 799.51
343.15 0.3146 811.47
343.15 0.4015 825.11
343.15 0.4790 837.25
343.15 0.5597 849.83
343.15 0.6365 861.76
343.15 0.7183 874.48
343.15 0.7939 886.17
343.15 0.8775 899.05
343.15 0.9553 910.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 81.5 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-methoxy- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0845 817.73
293.15 0.1559 829.58
293.15 0.2391 843.36
293.15 0.3146 855.77
293.15 0.4015 869.91
293.15 0.4790 882.45
293.15 0.5597 895.42
293.15 0.6365 907.69
293.15 0.7183 920.73
293.15 0.7939 932.73
293.15 0.8775 945.88
293.15 0.9553 957.99
303.15 0.0845 809.55
303.15 0.1559 821.29
303.15 0.2391 834.94
303.15 0.3146 847.26
303.15 0.4015 861.29
303.15 0.4790 873.74
303.15 0.5597 886.62
303.15 0.6365 898.82
303.15 0.7183 911.78
303.15 0.7939 923.71
303.15 0.8775 936.8
303.15 0.9553 948.84
313.15 0.0845 801.23
313.15 0.1559 812.86
313.15 0.2391 826.39
313.15 0.3146 838.61
313.15 0.4015 852.53
313.15 0.4790 864.89
313.15 0.5597 877.69
313.15 0.6365 889.81
313.15 0.7183 902.7
313.15 0.7939 914.56
313.15 0.8775 927.59
313.15 0.9553 939.57
323.15 0.0845 792.73
323.15 0.1559 804.25
323.15 0.2391 817.66
323.15 0.3146 829.78
323.15 0.4015 843.61
323.15 0.4790 855.88
323.15 0.5597 868.6
323.15 0.6365 880.65
323.15 0.7183 893.47
323.15 0.7939 905.28
323.15 0.8775 918.24
323.15 0.9553 930.18
333.15 0.0845 783.99
333.15 0.1559 795.42
333.15 0.2391 808.72
333.15 0.3146 820.75
333.15 0.4015 834.47
333.15 0.4790 846.68
333.15 0.5597 859.32
333.15 0.6365 871.31
333.15 0.7183 884.08
333.15 0.7939 895.83
333.15 0.8775 908.74
333.15 0.9553 920.63
343.15 0.0845 774.97
343.15 0.1559 786.31
343.15 0.2391 799.51
343.15 0.3146 811.47
343.15 0.4015 825.11
343.15 0.4790 837.25
343.15 0.5597 849.83
343.15 0.6365 861.76
343.15 0.7183 874.48
343.15 0.7939 886.17
343.15 0.8775 899.05
343.15 0.9553 910.9

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 397.58
0.1060 392.30
0.1660 389.75
0.1990 388.45
0.2330 387.18
0.2690 385.95
0.3060 384.73
0.3470 383.46
0.3850 382.35
0.4610 380.34
0.5000 379.37
0.5390 378.46
0.5760 377.64
0.6120 376.87
0.6710 375.72
0.7320 374.58
0.7860 373.65
0.8320 372.87
0.8910 371.93
0.9460 371.12
1.0000 370.40

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 397.58
0.1060 392.30
0.1660 389.75
0.1990 388.45
0.2330 387.18
0.2690 385.95
0.3060 384.73
0.3470 383.46
0.3850 382.35
0.4610 380.34
0.5000 379.37
0.5390 378.46
0.5760 377.64
0.6120 376.87
0.6710 375.72
0.7320 374.58
0.7860 373.65
0.8320 372.87
0.8910 371.93
0.9460 371.12
1.0000 370.40

Sources