Mixture of 1-Propanol + 1,2-Ethanediol

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

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
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (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
0.0200 0.6220
0.0710 0.8650
0.1200 0.9120
0.1720 0.9310
0.2330 0.9450
0.3110 0.9560
0.3790 0.9640
0.4320 0.9680
0.5120 0.9750
0.5710 0.9790
0.6190 0.9820
0.6720 0.9850
0.7320 0.9880
0.7890 0.9910
0.8620 0.9940
0.8930 0.9960
0.9310 0.9970
0.9620 0.9990
0.9910 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
0.0200 0.6220
0.0710 0.8650
0.1200 0.9120
0.1720 0.9310
0.2330 0.9450
0.3110 0.9560
0.3790 0.9640
0.4320 0.9680
0.5120 0.9750
0.5710 0.9790
0.6190 0.9820
0.6720 0.9850
0.7320 0.9880
0.7890 0.9910
0.8620 0.9940
0.8930 0.9960
0.9310 0.9970
0.9620 0.9990
0.9910 1.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,2-Ethanediol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0664 0.2084
298.15 0.1300 0.3553
298.15 0.1915 0.4559
298.15 0.2511 0.5281
298.15 0.3089 0.5728
298.15 0.3648 0.6024
298.15 0.4191 0.6140
298.15 0.4718 0.6134
298.15 0.5229 0.6042
298.15 0.5725 0.5770
298.15 0.6207 0.5535
298.15 0.6676 0.5172
298.15 0.7131 0.4771
298.15 0.7574 0.4262
298.15 0.8005 0.3753
298.15 0.8425 0.3101
298.15 0.8834 0.2433
298.15 0.9232 0.1675
298.15 0.9619 0.0874
308.15 0.0664 0.2237
308.15 0.1300 0.3816
308.15 0.1915 0.4893
308.15 0.2511 0.5649
308.15 0.3089 0.6131
308.15 0.3648 0.6365
308.15 0.4191 0.6485
308.15 0.4718 0.6543
308.15 0.5229 0.6414
308.15 0.5725 0.6195
308.15 0.6207 0.5887
308.15 0.6676 0.5511
308.15 0.7131 0.5067
308.15 0.7574 0.4540
308.15 0.8005 0.3942
308.15 0.8425 0.3281
308.15 0.8834 0.2557
308.15 0.9232 0.1780
308.15 0.9619 0.0912
323.15 0.0644 0.2367
323.15 0.1300 0.4043
323.15 0.1915 0.5247
323.15 0.2511 0.6010
323.15 0.3089 0.6530
323.15 0.3648 0.6840
323.15 0.4192 0.6990
323.15 0.4718 0.6977
323.15 0.5229 0.6823
323.15 0.5725 0.6605
323.15 0.6207 0.6293
323.15 0.6676 0.5892
323.15 0.7131 0.5409
323.15 0.7574 0.4869
323.15 0.8005 0.4212
323.15 0.8425 0.3507
323.15 0.8833 0.2724
323.15 0.9231 0.1875
323.15 0.9619 0.0960

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,2-Ethanediol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0664 0.2084
298.15 0.1300 0.3553
298.15 0.1915 0.4559
298.15 0.2511 0.5281
298.15 0.3089 0.5728
298.15 0.3648 0.6024
298.15 0.4191 0.6140
298.15 0.4718 0.6134
298.15 0.5229 0.6042
298.15 0.5725 0.5770
298.15 0.6207 0.5535
298.15 0.6676 0.5172
298.15 0.7131 0.4771
298.15 0.7574 0.4262
298.15 0.8005 0.3753
298.15 0.8425 0.3101
298.15 0.8834 0.2433
298.15 0.9232 0.1675
298.15 0.9619 0.0874
308.15 0.0664 0.2237
308.15 0.1300 0.3816
308.15 0.1915 0.4893
308.15 0.2511 0.5649
308.15 0.3089 0.6131
308.15 0.3648 0.6365
308.15 0.4191 0.6485
308.15 0.4718 0.6543
308.15 0.5229 0.6414
308.15 0.5725 0.6195
308.15 0.6207 0.5887
308.15 0.6676 0.5511
308.15 0.7131 0.5067
308.15 0.7574 0.4540
308.15 0.8005 0.3942
308.15 0.8425 0.3281
308.15 0.8834 0.2557
308.15 0.9232 0.1780
308.15 0.9619 0.0912
323.15 0.0644 0.2367
323.15 0.1300 0.4043
323.15 0.1915 0.5247
323.15 0.2511 0.6010
323.15 0.3089 0.6530
323.15 0.3648 0.6840
323.15 0.4192 0.6990
323.15 0.4718 0.6977
323.15 0.5229 0.6823
323.15 0.5725 0.6605
323.15 0.6207 0.6293
323.15 0.6676 0.5892
323.15 0.7131 0.5409
323.15 0.7574 0.4869
323.15 0.8005 0.4212
323.15 0.8425 0.3507
323.15 0.8833 0.2724
323.15 0.9231 0.1875
323.15 0.9619 0.0960

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
0.0200 440.82
0.0710 414.58
0.1200 405.31
0.1720 400.23
0.2330 396.14
0.3110 392.09
0.3790 389.17
0.4320 387.29
0.5120 384.49
0.5710 382.53
0.6190 380.96
0.6720 379.45
0.7320 377.69
0.7890 375.98
0.8620 374.06
0.8930 373.25
0.9310 372.19
0.9620 371.41
0.9910 370.64

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
0.0200 440.82
0.0710 414.58
0.1200 405.31
0.1720 400.23
0.2330 396.14
0.3110 392.09
0.3790 389.17
0.4320 387.29
0.5120 384.49
0.5710 382.53
0.6190 380.96
0.6720 379.45
0.7320 377.69
0.7890 375.98
0.8620 374.06
0.8930 373.25
0.9310 372.19
0.9620 371.41
0.9910 370.64

Sources