Mixture of 2-Propen-1-ol + Ethanol

Excel

2-Propen-1-ol

Name
2-Propen-1-ol
InChI
InChI=1S/C3H6O/c1-2-3-4/h2,4H,1,3H2
InChI Key
XXROGKLTLUQVRX-UHFFFAOYSA-N
Formula
C3H6O
SMILES
C=CCO
Mol. Weight (g/mol)
58.08
CAS
107-18-6

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of 2-Propen-1-ol (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Gas)

Temperature, K - Gas Mole fraction of 2-Propen-1-ol (1) - Gas
370.11 0.9870
369.50 0.9530
367.14 0.7990
366.08 0.7350
364.45 0.6420
363.53 0.5880
362.01 0.5000
361.55 0.4730
360.94 0.4430
359.58 0.3750
358.54 0.3250
357.71 0.2800
356.86 0.2410
356.01 0.1950
354.50 0.1300
352.92 0.0630

Mole fraction of 2-Propen-1-ol (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Gas)

Temperature, K - Gas Mole fraction of 2-Propen-1-ol (1) - Gas
370.11 0.9870
369.50 0.9530
367.14 0.7990
366.08 0.7350
364.45 0.6420
363.53 0.5880
362.01 0.5000
361.55 0.4730
360.94 0.4430
359.58 0.3750
358.54 0.3250
357.71 0.2800
356.86 0.2410
356.01 0.1950
354.50 0.1300
352.92 0.0630

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 2-Propen-1-ol (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.9930 370.11
0.9730 369.50
0.8860 367.14
0.8430 366.08
0.7760 364.45
0.7380 363.53
0.6640 362.01
0.6400 361.55
0.6090 360.94
0.5450 359.58
0.4880 358.54
0.4360 357.71
0.3830 356.86
0.3330 356.01
0.2400 354.50
0.1290 352.92

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 2-Propen-1-ol (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.9930 370.11
0.9730 369.50
0.8860 367.14
0.8430 366.08
0.7760 364.45
0.7380 363.53
0.6640 362.01
0.6400 361.55
0.6090 360.94
0.5450 359.58
0.4880 358.54
0.4360 357.71
0.3830 356.86
0.3330 356.01
0.2400 354.50
0.1290 352.92

Sources