Mixture of Ethyl formate + n-Hexane

Excel

Ethyl formate

Name
Ethyl formate
InChI
InChI=1S/C3H6O2/c1-2-5-3-4/h3H,2H2,1H3
InChI Key
WBJINCZRORDGAQ-UHFFFAOYSA-N
Formula
C3H6O2
SMILES
CCOC=O
Mol. Weight (g/mol)
74.08
CAS
109-94-4

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
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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 Ethyl formate (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethyl formate (1) - Liquid Mole fraction of Ethyl formate (1) - Gas
0.0000 0.0000
0.0028 0.0134
0.0431 0.1796
0.0569 0.2058
0.0747 0.2620
0.0820 0.2763
0.0849 0.2867
0.1033 0.3178
0.1260 0.3608
0.1497 0.3964
0.1799 0.4361
0.1959 0.4535
0.2022 0.4603
0.2481 0.4991
0.3113 0.5365
0.3324 0.5455
0.3595 0.5566
0.4048 0.5823
0.4694 0.6114
0.5308 0.6366
0.5895 0.6580
0.6478 0.6798
0.7054 0.7038
0.7656 0.7323
0.8236 0.7667
0.8749 0.8078
0.9134 0.8483
0.9463 0.8920
0.9657 0.9271
0.9835 0.9619
0.9938 0.9847
1.0000 1.0000

Mole fraction of Ethyl formate (1) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethyl formate (1) - Liquid Mole fraction of Ethyl formate (1) - Gas
0.0000 0.0000
0.0028 0.0134
0.0431 0.1796
0.0569 0.2058
0.0747 0.2620
0.0820 0.2763
0.0849 0.2867
0.1033 0.3178
0.1260 0.3608
0.1497 0.3964
0.1799 0.4361
0.1959 0.4535
0.2022 0.4603
0.2481 0.4991
0.3113 0.5365
0.3324 0.5455
0.3595 0.5566
0.4048 0.5823
0.4694 0.6114
0.5308 0.6366
0.5895 0.6580
0.6478 0.6798
0.7054 0.7038
0.7656 0.7323
0.8236 0.7667
0.8749 0.8078
0.9134 0.8483
0.9463 0.8920
0.9657 0.9271
0.9835 0.9619
0.9938 0.9847
1.0000 1.0000

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

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethyl formate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
291.15 0.0920 0.4488
291.15 0.2090 0.9555
291.15 0.3175 1.2742
291.15 0.4075 1.4475
291.15 0.4677 1.5229
291.15 0.5161 1.5399
291.15 0.5681 1.5253
291.15 0.6185 1.4376
291.15 0.6714 1.3358
291.15 0.7272 1.1986
291.15 0.7841 1.0159
291.15 0.8430 0.7871
291.15 0.9022 0.5311
291.15 0.9514 0.3052
318.15 0.1003 0.6223
318.15 0.1895 1.0194
318.15 0.2842 1.352
318.15 0.3713 1.5342
318.15 0.4495 1.6279
318.15 0.5137 1.647
318.15 0.5599 1.6191
318.15 0.5991 1.5658
318.15 0.6795 1.4099
318.15 0.7593 1.1752
318.15 0.8299 0.9023
318.15 0.8814 0.6468
318.15 0.9215 0.4398
318.15 0.9660 0.2132

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

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethyl formate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
291.15 0.0920 0.4488
291.15 0.2090 0.9555
291.15 0.3175 1.2742
291.15 0.4075 1.4475
291.15 0.4677 1.5229
291.15 0.5161 1.5399
291.15 0.5681 1.5253
291.15 0.6185 1.4376
291.15 0.6714 1.3358
291.15 0.7272 1.1986
291.15 0.7841 1.0159
291.15 0.8430 0.7871
291.15 0.9022 0.5311
291.15 0.9514 0.3052
318.15 0.1003 0.6223
318.15 0.1895 1.0194
318.15 0.2842 1.352
318.15 0.3713 1.5342
318.15 0.4495 1.6279
318.15 0.5137 1.647
318.15 0.5599 1.6191
318.15 0.5991 1.5658
318.15 0.6795 1.4099
318.15 0.7593 1.1752
318.15 0.8299 0.9023
318.15 0.8814 0.6468
318.15 0.9215 0.4398
318.15 0.9660 0.2132

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethyl formate (1) - Liquid Mass density, kg/m3 - Liquid
291.15 0.0000 661.2
291.15 0.0495 667.8
291.15 0.1025 675.4
291.15 0.1497 682.8
291.15 0.2049 692.1
291.15 0.2531 700.4
291.15 0.3068 710.6
291.15 0.3937 728.2
291.15 0.5016 753.0
291.15 0.6039 780.0
291.15 0.6996 808.2
291.15 0.7504 824.6
291.15 0.8029 842.4
291.15 0.8259 860.9
291.15 0.9016 880.3
291.15 0.9065 882.4
291.15 0.9522 901.9
291.15 0.9580 905.0
291.15 1.0000 924.7
298.15 0.0000 654.89
298.15 0.0777 665.63
298.15 0.1291 673.25
298.15 0.1715 679.95
298.15 0.2501 693.44
298.15 0.3270 707.73
298.15 0.4765 739.84
298.15 0.5354 754.13
298.15 0.5955 769.95
298.15 0.6441 783.83
298.15 0.6993 800.39
298.15 0.7956 832.38
298.15 0.8840 865.42
298.15 0.9643 898.98
298.15 1.0000 915.16
308.15 0.0000 646.07
308.15 0.0485 651.9
308.15 0.1103 660.5
308.15 0.1539 667.2
308.15 0.2548 683.8
308.15 0.3998 711.6
308.15 0.4915 731.9
308.15 0.5935 757.8
308.15 0.6998 788.0
308.15 0.7971 819.9
308.15 0.9063 860.7
308.15 0.9488 878.7
308.15 1.0000 902.07
318.15 0.0000 636.43
318.15 0.0476 642.18
318.15 0.0875 647.84
318.15 0.1044 649.54
318.15 0.1471 655.88
318.15 0.2199 667.46
318.15 0.3041 681.93
318.15 0.4061 701.97
318.15 0.5293 729.7
318.15 0.5869 744.1
318.15 0.6984 775.52
318.15 0.7476 790.78
318.15 0.7932 805.56
318.15 0.8873 840.19
318.15 0.9692 874.21
318.15 1.0000 888.42

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethyl formate (1) - Liquid Mass density, kg/m3 - Liquid
291.15 0.0000 661.2
291.15 0.0495 667.8
291.15 0.1025 675.4
291.15 0.1497 682.8
291.15 0.2049 692.1
291.15 0.2531 700.4
291.15 0.3068 710.6
291.15 0.3937 728.2
291.15 0.5016 753.0
291.15 0.6039 780.0
291.15 0.6996 808.2
291.15 0.7504 824.6
291.15 0.8029 842.4
291.15 0.8259 860.9
291.15 0.9016 880.3
291.15 0.9065 882.4
291.15 0.9522 901.9
291.15 0.9580 905.0
291.15 1.0000 924.7
298.15 0.0000 654.89
298.15 0.0777 665.63
298.15 0.1291 673.25
298.15 0.1715 679.95
298.15 0.2501 693.44
298.15 0.3270 707.73
298.15 0.4765 739.84
298.15 0.5354 754.13
298.15 0.5955 769.95
298.15 0.6441 783.83
298.15 0.6993 800.39
298.15 0.7956 832.38
298.15 0.8840 865.42
298.15 0.9643 898.98
298.15 1.0000 915.16
308.15 0.0000 646.07
308.15 0.0485 651.9
308.15 0.1103 660.5
308.15 0.1539 667.2
308.15 0.2548 683.8
308.15 0.3998 711.6
308.15 0.4915 731.9
308.15 0.5935 757.8
308.15 0.6998 788.0
308.15 0.7971 819.9
308.15 0.9063 860.7
308.15 0.9488 878.7
308.15 1.0000 902.07
318.15 0.0000 636.43
318.15 0.0476 642.18
318.15 0.0875 647.84
318.15 0.1044 649.54
318.15 0.1471 655.88
318.15 0.2199 667.46
318.15 0.3041 681.93
318.15 0.4061 701.97
318.15 0.5293 729.7
318.15 0.5869 744.1
318.15 0.6984 775.52
318.15 0.7476 790.78
318.15 0.7932 805.56
318.15 0.8873 840.19
318.15 0.9692 874.21
318.15 1.0000 888.42

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethyl formate (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 341.76
0.0028 341.41
0.0431 337.13
0.0569 335.90
0.0747 334.85
0.0820 334.37
0.0849 334.12
0.1033 332.97
0.1260 331.63
0.1497 330.46
0.1799 329.30
0.1959 328.72
0.2022 328.48
0.2481 327.17
0.3113 326.06
0.3324 325.85
0.3595 325.60
0.4048 324.84
0.4694 324.22
0.5308 323.81
0.5895 323.53
0.6478 323.38
0.7054 323.31
0.7656 323.39
0.8236 323.66
0.8749 324.11
0.9134 324.67
0.9463 325.38
0.9657 325.93
0.9835 326.56
0.9938 326.94
1.0000 327.33

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Ethyl formate (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 341.76
0.0028 341.41
0.0431 337.13
0.0569 335.90
0.0747 334.85
0.0820 334.37
0.0849 334.12
0.1033 332.97
0.1260 331.63
0.1497 330.46
0.1799 329.30
0.1959 328.72
0.2022 328.48
0.2481 327.17
0.3113 326.06
0.3324 325.85
0.3595 325.60
0.4048 324.84
0.4694 324.22
0.5308 323.81
0.5895 323.53
0.6478 323.38
0.7054 323.31
0.7656 323.39
0.8236 323.66
0.8749 324.11
0.9134 324.67
0.9463 325.38
0.9657 325.93
0.9835 326.56
0.9938 326.94
1.0000 327.33

Sources