Mixture of Isopropyl Alcohol + Ethanol, 2-methoxy-

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

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 Isopropyl Alcohol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid Mole fraction of Isopropyl Alcohol (1) - Gas
0.0000 0.0000
0.0500 0.1860
0.0990 0.3280
0.1550 0.4460
0.2070 0.5400
0.2610 0.6220
0.3140 0.6860
0.3710 0.7380
0.4250 0.7750
0.4850 0.8120
0.5410 0.8420
0.6000 0.8750
0.6580 0.9000
0.7150 0.9210
0.7670 0.9370
0.8150 0.9500
0.8590 0.9630
0.9020 0.9750
0.9420 0.9850
1.0000 1.0000

Mole fraction of Isopropyl Alcohol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid Mole fraction of Isopropyl Alcohol (1) - Gas
0.0000 0.0000
0.0500 0.1860
0.0990 0.3280
0.1550 0.4460
0.2070 0.5400
0.2610 0.6220
0.3140 0.6860
0.3710 0.7380
0.4250 0.7750
0.4850 0.8120
0.5410 0.8420
0.6000 0.8750
0.6580 0.9000
0.7150 0.9210
0.7670 0.9370
0.8150 0.9500
0.8590 0.9630
0.9020 0.9750
0.9420 0.9850
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 0.0823 800.06
293.15 0.1565 813.56
293.15 0.2367 828.13
293.15 0.3166 842.63
293.15 0.4015 858.01
293.15 0.4766 871.62
293.15 0.5605 886.76
293.15 0.6403 901.1
293.15 0.7179 914.98
293.15 0.7925 928.26
293.15 0.8593 940.12
293.15 0.9585 957.65
303.15 0.0823 791.49
303.15 0.1565 804.91
303.15 0.2367 819.4
303.15 0.3166 833.83
303.15 0.4015 849.14
303.15 0.4766 862.69
303.15 0.5605 877.79
303.15 0.6403 892.08
303.15 0.7179 905.92
303.15 0.7925 919.16
303.15 0.8593 931.0
303.15 0.9585 948.49
313.15 0.0823 782.64
313.15 0.1565 796.0
313.15 0.2367 810.43
313.15 0.3166 824.81
313.15 0.4015 840.08
313.15 0.4766 853.59
313.15 0.5605 868.64
313.15 0.6403 882.9
313.15 0.7179 896.72
313.15 0.7925 909.94
313.15 0.8593 921.74
313.15 0.9585 939.2
323.15 0.0823 773.45
323.15 0.1565 786.79
323.15 0.2367 801.18
323.15 0.3166 815.54
323.15 0.4015 830.78
323.15 0.4766 844.26
323.15 0.5605 859.3
323.15 0.6403 873.54
323.15 0.7179 887.34
323.15 0.7925 900.55
323.15 0.8593 912.34
323.15 0.9585 929.78
333.15 0.0823 763.86
333.15 0.1565 777.21
333.15 0.2367 791.6
333.15 0.3166 805.96
333.15 0.4015 821.21
333.15 0.4766 834.69
333.15 0.5605 849.72
333.15 0.6403 863.96
333.15 0.7179 877.76
333.15 0.7925 890.96
333.15 0.8593 902.77
333.15 0.9585 920.21
343.15 0.0823 753.79
343.15 0.1565 767.2
343.15 0.2367 781.64
343.15 0.3166 796.02
343.15 0.4015 811.31
343.15 0.4766 824.82
343.15 0.5605 839.87
343.15 0.6403 854.14
343.15 0.7179 867.96
343.15 0.7925 881.18
343.15 0.8593 892.99
343.15 0.9585 910.45

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 0.0823 800.06
293.15 0.1565 813.56
293.15 0.2367 828.13
293.15 0.3166 842.63
293.15 0.4015 858.01
293.15 0.4766 871.62
293.15 0.5605 886.76
293.15 0.6403 901.1
293.15 0.7179 914.98
293.15 0.7925 928.26
293.15 0.8593 940.12
293.15 0.9585 957.65
303.15 0.0823 791.49
303.15 0.1565 804.91
303.15 0.2367 819.4
303.15 0.3166 833.83
303.15 0.4015 849.14
303.15 0.4766 862.69
303.15 0.5605 877.79
303.15 0.6403 892.08
303.15 0.7179 905.92
303.15 0.7925 919.16
303.15 0.8593 931.0
303.15 0.9585 948.49
313.15 0.0823 782.64
313.15 0.1565 796.0
313.15 0.2367 810.43
313.15 0.3166 824.81
313.15 0.4015 840.08
313.15 0.4766 853.59
313.15 0.5605 868.64
313.15 0.6403 882.9
313.15 0.7179 896.72
313.15 0.7925 909.94
313.15 0.8593 921.74
313.15 0.9585 939.2
323.15 0.0823 773.45
323.15 0.1565 786.79
323.15 0.2367 801.18
323.15 0.3166 815.54
323.15 0.4015 830.78
323.15 0.4766 844.26
323.15 0.5605 859.3
323.15 0.6403 873.54
323.15 0.7179 887.34
323.15 0.7925 900.55
323.15 0.8593 912.34
323.15 0.9585 929.78
333.15 0.0823 763.86
333.15 0.1565 777.21
333.15 0.2367 791.6
333.15 0.3166 805.96
333.15 0.4015 821.21
333.15 0.4766 834.69
333.15 0.5605 849.72
333.15 0.6403 863.96
333.15 0.7179 877.76
333.15 0.7925 890.96
333.15 0.8593 902.77
333.15 0.9585 920.21
343.15 0.0823 753.79
343.15 0.1565 767.2
343.15 0.2367 781.64
343.15 0.3166 796.02
343.15 0.4015 811.31
343.15 0.4766 824.82
343.15 0.5605 839.87
343.15 0.6403 854.14
343.15 0.7179 867.96
343.15 0.7925 881.18
343.15 0.8593 892.99
343.15 0.9585 910.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 397.44
0.0500 392.64
0.0990 388.36
0.1550 384.14
0.2070 380.64
0.2610 377.42
0.3140 374.67
0.3710 372.03
0.4250 369.77
0.4850 367.62
0.5410 365.79
0.6000 363.99
0.6580 362.33
0.7150 360.84
0.7670 359.48
0.8150 358.64
0.8590 357.96
0.9020 357.33
0.9420 356.59
1.0000 355.35

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 397.44
0.0500 392.64
0.0990 388.36
0.1550 384.14
0.2070 380.64
0.2610 377.42
0.3140 374.67
0.3710 372.03
0.4250 369.77
0.4850 367.62
0.5410 365.79
0.6000 363.99
0.6580 362.33
0.7150 360.84
0.7670 359.48
0.8150 358.64
0.8590 357.96
0.9020 357.33
0.9420 356.59
1.0000 355.35

Sources