Mixture of Methyl formate + Nonane

Excel

Methyl formate

Name
Methyl formate
InChI
InChI=1S/C2H4O2/c1-4-2-3/h2H,1H3
InChI Key
TZIHFWKZFHZASV-UHFFFAOYSA-N
Formula
C2H4O2
SMILES
COC=O
Mol. Weight (g/mol)
60.05
CAS
107-31-3

Nonane

Name
Nonane
InChI
InChI=1S/C9H20/c1-3-5-7-9-8-6-4-2/h3-9H2,1-2H3
InChI Key
BKIMMITUMNQMOS-UHFFFAOYSA-N
Formula
C9H20
SMILES
CCCCCCCCC
Mol. Weight (g/mol)
128.26
CAS
111-84-2
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Datasets

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

Mole fraction of Methyl formate (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Gas)

Mole fraction of Methyl formate (1) - Liquid Mole fraction of Methyl formate (1) - Gas
0.0000 0.0000
0.0080 0.2330
0.0140 0.3850
0.0200 0.5090
0.0260 0.6040
0.0410 0.7390
0.0670 0.8560
0.1100 0.9350
0.1370 0.9540
0.2080 0.9780
0.2540 0.9840
0.3280 0.9880
0.3900 0.9900
0.4460 0.9900
0.4920 0.9910
0.5490 0.9920
0.5890 0.9920
0.6490 0.9930
0.7320 0.9930
0.7920 0.9930
0.8560 0.9930
0.9060 0.9940
0.9370 0.9950
0.9650 0.9960
0.9870 0.9980
1.0000 1.0000

Mole fraction of Methyl formate (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Gas)

Mole fraction of Methyl formate (1) - Liquid Mole fraction of Methyl formate (1) - Gas
0.0000 0.0000
0.0080 0.2330
0.0140 0.3850
0.0200 0.5090
0.0260 0.6040
0.0410 0.7390
0.0670 0.8560
0.1100 0.9350
0.1370 0.9540
0.2080 0.9780
0.2540 0.9840
0.3280 0.9880
0.3900 0.9900
0.4460 0.9900
0.4920 0.9910
0.5490 0.9920
0.5890 0.9920
0.6490 0.9930
0.7320 0.9930
0.7920 0.9930
0.8560 0.9930
0.9060 0.9940
0.9370 0.9950
0.9650 0.9960
0.9870 0.9980
1.0000 1.0000

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

Operational conditions:

Mole fraction of Methyl formate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1280 1.158
0.2410 1.904
0.3250 2.294
0.3900 2.486
0.4510 2.579
0.5050 2.59
0.5540 2.554
0.5970 2.484
0.6360 2.407
0.6770 2.289
0.7130 2.178
0.7500 2.052
0.7880 1.888
0.8250 1.715
0.8590 1.511
0.8930 1.267
0.9250 0.9970
0.9460 0.7620
0.9650 0.5270
0.9820 0.2880

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

Operational conditions:

Mole fraction of Methyl formate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1280 1.158
0.2410 1.904
0.3250 2.294
0.3900 2.486
0.4510 2.579
0.5050 2.59
0.5540 2.554
0.5970 2.484
0.6360 2.407
0.6770 2.289
0.7130 2.178
0.7500 2.052
0.7880 1.888
0.8250 1.715
0.8590 1.511
0.8930 1.267
0.9250 0.9970
0.9460 0.7620
0.9650 0.5270
0.9820 0.2880

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl formate (1) - Liquid Mass density, kg/m3 - Liquid
291.15 0.0000 719.27
291.15 0.0514 722.55
291.15 0.0978 725.22
291.15 0.1530 729.4
291.15 0.1992 733.01
291.15 0.2597 738.77
291.15 0.3040 743.49
291.15 0.3580 750.14
291.15 0.4029 756.42
291.15 0.4475 763.17
291.15 0.5016 772.34
291.15 0.5475 781.14
291.15 0.6005 792.83
291.15 0.6470 804.44
291.15 0.7024 820.19
291.15 0.7486 835.41
291.15 0.8015 855.65
291.15 0.8481 875.83
291.15 0.9011 903.59
291.15 0.9483 933.41
291.15 1.0000 976.46
298.15 0.0000 713.85
298.15 0.0553 716.79
298.15 0.0965 719.34
298.15 0.1264 721.26
298.15 0.1991 726.75
298.15 0.2405 730.69
298.15 0.2879 735.48
298.15 0.3473 741.96
298.15 0.3968 748.54
298.15 0.4554 757.03
298.15 0.5023 764.92
298.15 0.5484 773.43
298.15 0.5940 783.31
298.15 0.6374 793.43
298.15 0.7010 811.22
298.15 0.7541 827.74
298.15 0.8019 846.55
298.15 0.8504 867.8
298.15 0.9014 894.05
298.15 0.9508 924.99
298.15 1.0000 966.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl formate (1) - Liquid Mass density, kg/m3 - Liquid
291.15 0.0000 719.27
291.15 0.0514 722.55
291.15 0.0978 725.22
291.15 0.1530 729.4
291.15 0.1992 733.01
291.15 0.2597 738.77
291.15 0.3040 743.49
291.15 0.3580 750.14
291.15 0.4029 756.42
291.15 0.4475 763.17
291.15 0.5016 772.34
291.15 0.5475 781.14
291.15 0.6005 792.83
291.15 0.6470 804.44
291.15 0.7024 820.19
291.15 0.7486 835.41
291.15 0.8015 855.65
291.15 0.8481 875.83
291.15 0.9011 903.59
291.15 0.9483 933.41
291.15 1.0000 976.46
298.15 0.0000 713.85
298.15 0.0553 716.79
298.15 0.0965 719.34
298.15 0.1264 721.26
298.15 0.1991 726.75
298.15 0.2405 730.69
298.15 0.2879 735.48
298.15 0.3473 741.96
298.15 0.3968 748.54
298.15 0.4554 757.03
298.15 0.5023 764.92
298.15 0.5484 773.43
298.15 0.5940 783.31
298.15 0.6374 793.43
298.15 0.7010 811.22
298.15 0.7541 827.74
298.15 0.8019 846.55
298.15 0.8504 867.8
298.15 0.9014 894.05
298.15 0.9508 924.99
298.15 1.0000 966.1

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl formate (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 423.94
0.0080 413.55
0.0140 405.82
0.0200 398.05
0.0260 391.05
0.0410 378.85
0.0670 363.02
0.1100 345.24
0.1370 337.80
0.2080 323.99
0.2540 318.40
0.3280 313.31
0.3900 310.58
0.4460 310.14
0.4920 308.71
0.5490 308.30
0.5890 307.75
0.6490 307.44
0.7320 307.08
0.7920 306.72
0.8560 306.49
0.9060 306.42
0.9370 306.16
0.9650 305.66
0.9870 305.12
1.0000 304.70

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl formate (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 423.94
0.0080 413.55
0.0140 405.82
0.0200 398.05
0.0260 391.05
0.0410 378.85
0.0670 363.02
0.1100 345.24
0.1370 337.80
0.2080 323.99
0.2540 318.40
0.3280 313.31
0.3900 310.58
0.4460 310.14
0.4920 308.71
0.5490 308.30
0.5890 307.75
0.6490 307.44
0.7320 307.08
0.7920 306.72
0.8560 306.49
0.9060 306.42
0.9370 306.16
0.9650 305.66
0.9870 305.12
1.0000 304.70

Sources