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Mixture of Isopropyl Alcohol + 1,2-Ethanediol + Water

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

1,2-Ethanediol

Name
1,2-Ethanediol
InChI
InChI=1S/C2H6O2/c3-1-2-4/h3-4H,1-2H2
InChI Key
LYCAIKOWRPUZTN-UHFFFAOYSA-N
Formula
C2H6O2
SMILES
OCCO
Mol. Weight (g/mol)
62.07
CAS
107-21-1

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Mole fraction (4)
  2. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed Measured
Solvent: Mole fraction of Isopropyl Alcohol (1) - Liquid Mass fraction of 1,2-Ethanediol (2) - Liquid Mole fraction of Water (3) - Gas
0.1982 0.8003 0.4514
0.2007 0.7016 0.4492
0.2001 0.6039 0.4492
0.1999 0.5021 0.4541
0.1999 0.4056 0.4551
0.2000 0.3040 0.4570
0.2001 0.2033 0.4542
0.2001 0.1048 0.4561
0.9461 0.8137 0.0179
0.9503 0.6992 0.0207
0.9508 0.6015 0.0255
0.9503 0.5015 0.0309
0.9503 0.4041 0.0367
0.9503 0.3015 0.0431
0.9501 0.2012 0.0515
0.9503 0.1005 0.0600

Mole fraction of Isopropyl Alcohol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed Measured
Solvent: Mole fraction of Isopropyl Alcohol (1) - Liquid Mass fraction of 1,2-Ethanediol (2) - Liquid Mole fraction of Isopropyl Alcohol (1) - Gas
0.1982 0.8003 0.5268
0.2007 0.7016 0.5409
0.2001 0.6039 0.5452
0.1999 0.5021 0.5426
0.1999 0.4056 0.5428
0.2000 0.3040 0.5417
0.2001 0.2033 0.5451
0.2001 0.1048 0.5436
0.9461 0.8137 0.9497
0.9503 0.6992 0.9613
0.9508 0.6015 0.9624
0.9503 0.5015 0.9599
0.9503 0.4041 0.9568
0.9503 0.3015 0.9524
0.9501 0.2012 0.9455
0.9503 0.1005 0.9384

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed Measured
Solvent: Mole fraction of Isopropyl Alcohol (1) - Liquid Mass fraction of 1,2-Ethanediol (2) - Liquid Mole fraction of Water (3) - Gas
0.1982 0.8003 0.4514
0.2007 0.7016 0.4492
0.2001 0.6039 0.4492
0.1999 0.5021 0.4541
0.1999 0.4056 0.4551
0.2000 0.3040 0.4570
0.2001 0.2033 0.4542
0.2001 0.1048 0.4561
0.9461 0.8137 0.0179
0.9503 0.6992 0.0207
0.9508 0.6015 0.0255
0.9503 0.5015 0.0309
0.9503 0.4041 0.0367
0.9503 0.3015 0.0431
0.9501 0.2012 0.0515
0.9503 0.1005 0.0600

Mole fraction of Isopropyl Alcohol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed Measured
Solvent: Mole fraction of Isopropyl Alcohol (1) - Liquid Mass fraction of 1,2-Ethanediol (2) - Liquid Mole fraction of Isopropyl Alcohol (1) - Gas
0.1982 0.8003 0.5268
0.2007 0.7016 0.5409
0.2001 0.6039 0.5452
0.1999 0.5021 0.5426
0.1999 0.4056 0.5428
0.2000 0.3040 0.5417
0.2001 0.2033 0.5451
0.2001 0.1048 0.5436
0.9461 0.8137 0.9497
0.9503 0.6992 0.9613
0.9508 0.6015 0.9624
0.9503 0.5015 0.9599
0.9503 0.4041 0.9568
0.9503 0.3015 0.9524
0.9501 0.2012 0.9455
0.9503 0.1005 0.9384

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Solvent: Mole fraction of Isopropyl Alcohol (1) - Liquid Mass fraction of 1,2-Ethanediol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.1982 0.8003 384.14
0.2007 0.7016 374.58
0.2001 0.6039 368.72
0.1999 0.5021 364.57
0.1999 0.4056 361.72
0.2000 0.3040 359.43
0.2001 0.2033 357.74
0.2001 0.1048 356.37
0.9461 0.8137 386.39
0.9503 0.6992 377.06
0.9508 0.6015 372.18
0.9503 0.5015 368.43
0.9503 0.4041 365.35
0.9503 0.3015 362.52
0.9501 0.2012 359.84
0.9503 0.1005 357.41

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Solvent: Mole fraction of Isopropyl Alcohol (1) - Liquid Mass fraction of 1,2-Ethanediol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.1982 0.8003 384.14
0.2007 0.7016 374.58
0.2001 0.6039 368.72
0.1999 0.5021 364.57
0.1999 0.4056 361.72
0.2000 0.3040 359.43
0.2001 0.2033 357.74
0.2001 0.1048 356.37
0.9461 0.8137 386.39
0.9503 0.6992 377.06
0.9508 0.6015 372.18
0.9503 0.5015 368.43
0.9503 0.4041 365.35
0.9503 0.3015 362.52
0.9501 0.2012 359.84
0.9503 0.1005 357.41

Sources