Mixture of Methyl formate + Decane

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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

Decane

Name
Decane
InChI
InChI=1S/C10H22/c1-3-5-7-9-10-8-6-4-2/h3-10H2,1-2H3
InChI Key
DIOQZVSQGTUSAI-UHFFFAOYSA-N
Formula
C10H22
SMILES
CCCCCCCCCC
Mol. Weight (g/mol)
142.28
CAS
124-18-5
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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
0.1828 0.9860
0.2256 0.9899
0.2810 0.9930
0.3184 0.9941
0.3740 0.9950
0.4566 0.9950
0.4813 0.9950
0.5586 0.9954
0.6443 0.9957
0.7422 0.9962
0.7513 0.9962
0.7683 0.9962
0.8156 0.9962
0.8046 0.9963
0.7573 0.9963
0.8736 0.9963
0.8497 0.9964
0.8534 0.9964
0.7951 0.9964
0.8958 0.9964
0.8788 0.9965
0.9279 0.9965
0.9507 0.9969
1.0000 1.0000
0.0000 0.0000
0.1828 0.9860
0.2256 0.9899
0.2810 0.9930
0.3184 0.9941
0.3740 0.9950
0.4566 0.9950
0.4813 0.9950
0.5586 0.9954
0.6443 0.9957
0.7422 0.9962
0.7513 0.9962
0.7683 0.9962
0.8156 0.9962
0.8046 0.9963
0.7573 0.9963
0.8736 0.9963
0.8497 0.9964
0.8534 0.9964
0.7951 0.9964
0.8958 0.9964
0.8788 0.9965
0.9279 0.9965
0.9507 0.9969
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
0.1828 0.9860
0.2256 0.9899
0.2810 0.9930
0.3184 0.9941
0.3740 0.9950
0.4566 0.9950
0.4813 0.9950
0.5586 0.9954
0.6443 0.9957
0.7422 0.9962
0.7513 0.9962
0.7683 0.9962
0.8156 0.9962
0.8046 0.9963
0.7573 0.9963
0.8736 0.9963
0.8497 0.9964
0.8534 0.9964
0.7951 0.9964
0.8958 0.9964
0.8788 0.9965
0.9279 0.9965
0.9507 0.9969
1.0000 1.0000
0.0000 0.0000
0.1828 0.9860
0.2256 0.9899
0.2810 0.9930
0.3184 0.9941
0.3740 0.9950
0.4566 0.9950
0.4813 0.9950
0.5586 0.9954
0.6443 0.9957
0.7422 0.9962
0.7513 0.9962
0.7683 0.9962
0.8156 0.9962
0.8046 0.9963
0.7573 0.9963
0.8736 0.9963
0.8497 0.9964
0.8534 0.9964
0.7951 0.9964
0.8958 0.9964
0.8788 0.9965
0.9279 0.9965
0.9507 0.9969
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
0.0913 0.8430
0.1855 1.523
0.2836 2.048
0.3550 2.314
0.4355 2.523
0.4992 2.565
0.5501 2.522
0.6223 2.384
0.6570 2.28
0.6961 2.151
0.7358 1.988
0.7753 1.818
0.8182 1.603
0.8575 1.392
0.8913 1.167
0.9242 0.9540
0.9517 0.6830
0.9780 0.3700

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
0.0913 0.8430
0.1855 1.523
0.2836 2.048
0.3550 2.314
0.4355 2.523
0.4992 2.565
0.5501 2.522
0.6223 2.384
0.6570 2.28
0.6961 2.151
0.7358 1.988
0.7753 1.818
0.8182 1.603
0.8575 1.392
0.8913 1.167
0.9242 0.9540
0.9517 0.6830
0.9780 0.3700

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl formate (1) - Liquid Mass density, kg/m3 - Liquid
291.15 0.0000 731.24
291.15 0.0586 734.13
291.15 0.1175 737.52
291.15 0.1207 737.49
291.15 0.1852 741.83
291.15 0.2211 744.6
291.15 0.3017 751.85
291.15 0.4028 763.44
291.15 0.5045 778.54
291.15 0.6061 798.22
291.15 0.6969 820.96
291.15 0.7505 837.89
291.15 0.8031 857.11
291.15 0.8422 873.82
291.15 0.9005 902.87
291.15 0.9514 936.01
291.15 1.0000 976.9
298.15 0.0000 726.26
298.15 0.0066 726.63
298.15 0.0509 728.85
298.15 0.1250 732.64
298.15 0.1570 734.47
298.15 0.2245 739.31
298.15 0.2785 744.09
298.15 0.3728 753.68
298.15 0.4849 768.98
298.15 0.5941 789.08
298.15 0.6968 813.83
298.15 0.7424 827.18
298.15 0.7939 845.3
298.15 0.8450 866.07
298.15 0.8953 890.78
298.15 0.9458 922.09
298.15 1.0000 966.54

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl formate (1) - Liquid Mass density, kg/m3 - Liquid
291.15 0.0000 731.24
291.15 0.0586 734.13
291.15 0.1175 737.52
291.15 0.1207 737.49
291.15 0.1852 741.83
291.15 0.2211 744.6
291.15 0.3017 751.85
291.15 0.4028 763.44
291.15 0.5045 778.54
291.15 0.6061 798.22
291.15 0.6969 820.96
291.15 0.7505 837.89
291.15 0.8031 857.11
291.15 0.8422 873.82
291.15 0.9005 902.87
291.15 0.9514 936.01
291.15 1.0000 976.9
298.15 0.0000 726.26
298.15 0.0066 726.63
298.15 0.0509 728.85
298.15 0.1250 732.64
298.15 0.1570 734.47
298.15 0.2245 739.31
298.15 0.2785 744.09
298.15 0.3728 753.68
298.15 0.4849 768.98
298.15 0.5941 789.08
298.15 0.6968 813.83
298.15 0.7424 827.18
298.15 0.7939 845.3
298.15 0.8450 866.07
298.15 0.8953 890.78
298.15 0.9458 922.09
298.15 1.0000 966.54

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 446.93
0.1828 323.96
0.2256 318.08
0.2810 312.32
0.3184 309.71
0.3740 307.51
0.4566 307.28
0.4813 307.24
0.5586 306.23
0.6443 306.06
0.7422 306.07
0.7513 306.13
0.7573 306.05
0.7683 306.04
0.7951 305.88
0.8046 306.01
0.8156 306.04
0.8497 306.02
0.8534 305.97
0.8736 305.95
0.8788 305.85
0.8958 305.78
0.9279 305.64
0.9507 305.45
1.0000 304.70
0.0000 446.93
0.1828 323.96
0.2256 318.08
0.2810 312.32
0.3184 309.71
0.3740 307.51
0.4566 307.28
0.4813 307.24
0.5586 306.23
0.6443 306.06
0.7422 306.07
0.7513 306.13
0.7573 306.05
0.7683 306.04
0.7951 305.88
0.8046 306.01
0.8156 306.04
0.8497 306.02
0.8534 305.97
0.8736 305.95
0.8788 305.85
0.8958 305.78
0.9279 305.64
0.9507 305.45
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 446.93
0.1828 323.96
0.2256 318.08
0.2810 312.32
0.3184 309.71
0.3740 307.51
0.4566 307.28
0.4813 307.24
0.5586 306.23
0.6443 306.06
0.7422 306.07
0.7513 306.13
0.7573 306.05
0.7683 306.04
0.7951 305.88
0.8046 306.01
0.8156 306.04
0.8497 306.02
0.8534 305.97
0.8736 305.95
0.8788 305.85
0.8958 305.78
0.9279 305.64
0.9507 305.45
1.0000 304.70
0.0000 446.93
0.1828 323.96
0.2256 318.08
0.2810 312.32
0.3184 309.71
0.3740 307.51
0.4566 307.28
0.4813 307.24
0.5586 306.23
0.6443 306.06
0.7422 306.07
0.7513 306.13
0.7573 306.05
0.7683 306.04
0.7951 305.88
0.8046 306.01
0.8156 306.04
0.8497 306.02
0.8534 305.97
0.8736 305.95
0.8788 305.85
0.8958 305.78
0.9279 305.64
0.9507 305.45
1.0000 304.70

Sources