Mixture of n-Hexane + Methyl formate

Excel

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

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
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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 (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl formate (2) - Liquid Mole fraction of Methyl formate (2) - Gas
0.0000 0.0000
0.0220 0.2663
0.0325 0.3347
0.0634 0.4771
0.1218 0.6286
0.1809 0.6971
0.2420 0.7380
0.2890 0.7615
0.3342 0.7711
0.4008 0.7910
0.4699 0.8020
0.5404 0.8095
0.5945 0.8146
0.6592 0.8204
0.7253 0.8257
0.7969 0.8369
0.8429 0.8473
0.8811 0.8597
0.9160 0.8763
0.9367 0.8903
0.9585 0.9172
0.9781 0.9501
0.9872 0.9657
0.9979 0.9921
1.0000 1.0000

Mole fraction of Methyl formate (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl formate (2) - Liquid Mole fraction of Methyl formate (2) - Gas
0.0000 0.0000
0.0220 0.2663
0.0325 0.3347
0.0634 0.4771
0.1218 0.6286
0.1809 0.6971
0.2420 0.7380
0.2890 0.7615
0.3342 0.7711
0.4008 0.7910
0.4699 0.8020
0.5404 0.8095
0.5945 0.8146
0.6592 0.8204
0.7253 0.8257
0.7969 0.8369
0.8429 0.8473
0.8811 0.8597
0.9160 0.8763
0.9367 0.8903
0.9585 0.9172
0.9781 0.9501
0.9872 0.9657
0.9979 0.9921
1.0000 1.0000

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

Operational conditions:

Mole fraction of Methyl formate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1408 1.0599
0.2520 1.6259
0.3379 1.9346
0.4008 2.0582
0.4618 2.1105
0.5094 2.0986
0.5501 2.0632
0.5862 2.0134
0.6157 1.9318
0.6568 1.8364
0.7033 1.7134
0.7517 1.5467
0.7971 1.382
0.8450 1.1754
0.8923 0.9169
0.9292 0.6401
0.9665 0.3748

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

Operational conditions:

Mole fraction of Methyl formate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1408 1.0599
0.2520 1.6259
0.3379 1.9346
0.4008 2.0582
0.4618 2.1105
0.5094 2.0986
0.5501 2.0632
0.5862 2.0134
0.6157 1.9318
0.6568 1.8364
0.7033 1.7134
0.7517 1.5467
0.7971 1.382
0.8450 1.1754
0.8923 0.9169
0.9292 0.6401
0.9665 0.3748

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl formate (2) - Liquid Mass density, kg/m3 - Liquid
291.15 0.0000 661.2
291.15 0.0190 663.0
291.15 0.0499 666.3
291.15 0.0863 670.6
291.15 0.1013 672.6
291.15 0.1209 675.3
291.15 0.2033 687.1
291.15 0.2986 702.6
291.15 0.3828 718.9
291.15 0.4841 742.3
291.15 0.5462 759.1
291.15 0.6061 777.4
291.15 0.6987 810.1
291.15 0.7445 829.1
291.15 0.7956 851.5
291.15 0.8392 872.6
291.15 0.9030 908.4
291.15 0.9539 939.9
291.15 1.0000 976.9
298.15 0.0000 654.89
298.15 0.0376 659.63
298.15 0.0816 664.26
298.15 0.1327 670.55
298.15 0.1642 674.8
298.15 0.2352 685.32
298.15 0.2936 695.29
298.15 0.3903 714.41
298.15 0.4987 740.05
298.15 0.5979 768.9
298.15 0.7062 806.5
298.15 0.7433 821.74
298.15 0.7972 845.31
298.15 0.8497 871.94
298.15 0.9050 902.05
298.15 0.9582 936.28
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 (2) - Liquid Mass density, kg/m3 - Liquid
291.15 0.0000 661.2
291.15 0.0190 663.0
291.15 0.0499 666.3
291.15 0.0863 670.6
291.15 0.1013 672.6
291.15 0.1209 675.3
291.15 0.2033 687.1
291.15 0.2986 702.6
291.15 0.3828 718.9
291.15 0.4841 742.3
291.15 0.5462 759.1
291.15 0.6061 777.4
291.15 0.6987 810.1
291.15 0.7445 829.1
291.15 0.7956 851.5
291.15 0.8392 872.6
291.15 0.9030 908.4
291.15 0.9539 939.9
291.15 1.0000 976.9
298.15 0.0000 654.89
298.15 0.0376 659.63
298.15 0.0816 664.26
298.15 0.1327 670.55
298.15 0.1642 674.8
298.15 0.2352 685.32
298.15 0.2936 695.29
298.15 0.3903 714.41
298.15 0.4987 740.05
298.15 0.5979 768.9
298.15 0.7062 806.5
298.15 0.7433 821.74
298.15 0.7972 845.31
298.15 0.8497 871.94
298.15 0.9050 902.05
298.15 0.9582 936.28
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 (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 341.76
0.0220 333.45
0.0325 331.00
0.0634 325.36
0.1218 315.65
0.1809 311.55
0.2420 308.20
0.2890 306.72
0.3342 305.93
0.4008 304.76
0.4699 303.99
0.5404 303.53
0.5945 303.30
0.6592 303.08
0.7253 302.91
0.7969 302.77
0.8429 302.73
0.8811 302.75
0.9160 302.88
0.9367 303.07
0.9585 303.36
0.9781 303.85
0.9872 304.11
0.9979 304.55
1.0000 304.70

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl formate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 341.76
0.0220 333.45
0.0325 331.00
0.0634 325.36
0.1218 315.65
0.1809 311.55
0.2420 308.20
0.2890 306.72
0.3342 305.93
0.4008 304.76
0.4699 303.99
0.5404 303.53
0.5945 303.30
0.6592 303.08
0.7253 302.91
0.7969 302.77
0.8429 302.73
0.8811 302.75
0.9160 302.88
0.9367 303.07
0.9585 303.36
0.9781 303.85
0.9872 304.11
0.9979 304.55
1.0000 304.70

Sources