Mixture of Acetic acid, butyl ester + Ethyl Acetate

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Acetic acid, butyl ester

Name
Acetic acid, butyl ester
InChI
InChI=1S/C6H12O2/c1-3-4-5-8-6(2)7/h3-5H2,1-2H3
InChI Key
DKPFZGUDAPQIHT-UHFFFAOYSA-N
Formula
C6H12O2
SMILES
CCCCOC(C)=O
Mol. Weight (g/mol)
116.16
CAS
123-86-4

Ethyl Acetate

Name
Ethyl Acetate
InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Mol. Weight (g/mol)
88.11
CAS
141-78-6
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. ρl - Mass density, kg/m3 (2)
  5. Vapor Liquid Equilibrium at Constant Pressure
  6. Vapor Liquid Equilibrium at Constant Temperature

Mole fraction of Ethyl Acetate (2) [ref]

Fixed Measured
Mole fraction of Ethyl Acetate (2) - Liquid Temperature, K - Liquid Mole fraction of Ethyl Acetate (2) - Gas
0.0000 350.12 0.0000
0.0530 350.07 0.2210
0.0940 350.03 0.3460
0.1380 350.06 0.4490
0.1760 350.07 0.5180
0.2220 350.12 0.5940
0.2650 350.05 0.6480
0.3130 350.11 0.6970
0.3490 350.14 0.7300
0.3820 350.12 0.7550
0.4340 350.11 0.7950
0.4760 350.10 0.8220
0.5190 350.08 0.8500
0.5990 350.04 0.8820
0.6580 350.10 0.9050
0.7150 350.06 0.9260
0.7770 350.08 0.9450
0.8190 350.12 0.9570
0.8730 350.11 0.9710
0.9310 350.05 0.9850
0.9850 350.06 0.9970
1.0000 350.02 1.0000

Mole fraction of Ethyl Acetate (2) [ref]

Fixed Measured
Mole fraction of Ethyl Acetate (2) - Liquid Temperature, K - Liquid Mole fraction of Ethyl Acetate (2) - Gas
0.0000 350.12 0.0000
0.0530 350.07 0.2210
0.0940 350.03 0.3460
0.1380 350.06 0.4490
0.1760 350.07 0.5180
0.2220 350.12 0.5940
0.2650 350.05 0.6480
0.3130 350.11 0.6970
0.3490 350.14 0.7300
0.3820 350.12 0.7550
0.4340 350.11 0.7950
0.4760 350.10 0.8220
0.5190 350.08 0.8500
0.5990 350.04 0.8820
0.6580 350.10 0.9050
0.7150 350.06 0.9260
0.7770 350.08 0.9450
0.8190 350.12 0.9570
0.8730 350.11 0.9710
0.9310 350.05 0.9850
0.9850 350.06 0.9970
1.0000 350.02 1.0000

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

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0991 0.0232
0.1982 0.0437
0.2993 0.0594
0.3993 0.0700
0.4982 0.0760
0.5994 0.0747
0.6985 0.0670
0.7988 0.0524
0.8995 0.0300

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

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0991 0.0232
0.1982 0.0437
0.2993 0.0594
0.3993 0.0700
0.4982 0.0760
0.5994 0.0747
0.6985 0.0670
0.7988 0.0524
0.8995 0.0300

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Ethyl Acetate (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 350.12 19.17
0.0530 350.07 23.36
0.0940 350.03 26.72
0.1380 350.06 30.07
0.1760 350.07 33.11
0.2220 350.12 36.83
0.2650 350.05 40.48
0.3130 350.11 44.00
0.3490 350.14 47.33
0.3820 350.12 50.03
0.4340 350.11 54.38
0.4760 350.10 58.26
0.5190 350.08 62.19
0.5990 350.04 67.80
0.6580 350.10 72.60
0.7150 350.06 77.09
0.7770 350.08 82.25
0.8190 350.12 85.95
0.8730 350.11 90.33
0.9310 350.05 94.87
0.9850 350.06 99.46
1.0000 350.02 100.68

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Ethyl Acetate (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 350.12 19.17
0.0530 350.07 23.36
0.0940 350.03 26.72
0.1380 350.06 30.07
0.1760 350.07 33.11
0.2220 350.12 36.83
0.2650 350.05 40.48
0.3130 350.11 44.00
0.3490 350.14 47.33
0.3820 350.12 50.03
0.4340 350.11 54.38
0.4760 350.10 58.26
0.5190 350.08 62.19
0.5990 350.04 67.80
0.6580 350.10 72.60
0.7150 350.06 77.09
0.7770 350.08 82.25
0.8190 350.12 85.95
0.8730 350.11 90.33
0.9310 350.05 94.87
0.9850 350.06 99.46
1.0000 350.02 100.68

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Mass density, kg/m3 - Liquid
0.0991 876.9
0.1982 878.2
0.2993 879.7
0.3993 881.3
0.4982 882.9
0.5994 884.8
0.6985 886.7
0.7988 888.9
0.8995 891.3

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Mass density, kg/m3 - Liquid
0.0991 876.9
0.1982 878.2
0.2993 879.7
0.3993 881.3
0.4982 882.9
0.5994 884.8
0.6985 886.7
0.7988 888.9
0.8995 891.3

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl Acetate (2) - Liquid y1[mol/mol] of Ethyl Acetate (2) - Vapour
394.95 0.0390 0.1410
390.35 0.0960 0.2990
384.05 0.1720 0.4710
376.45 0.2910 0.6390
370.15 0.4060 0.7420
366.85 0.4790 0.8070
364.55 0.5520 0.8380
362.65 0.5780 0.8640
359.45 0.6890 0.9030
355.55 0.8070 0.9490
352.35 0.9040 0.9780
352.15 0.9140 0.9800
350.75 0.9560 0.9900

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 15.4 (VLE)

Fixed Measured
P [kPa] - VLE T [K] - VLE x1[mol/mol] of Ethyl Acetate (2) - Liquid y1[mol/mol] of Ethyl Acetate (2) - Vapour
19.17 350.12 0.0000 0.0000
23.36 350.07 0.0530 0.2210
26.72 350.03 0.0940 0.3460
30.07 350.06 0.1380 0.4490
33.11 350.07 0.1760 0.5180
36.83 350.12 0.2220 0.5940
40.48 350.05 0.2650 0.6480
44.0 350.11 0.3130 0.6970
47.33 350.14 0.3490 0.7300
50.03 350.12 0.3820 0.7550
54.38 350.11 0.4340 0.7950
58.26 350.1 0.4760 0.8220
62.19 350.08 0.5190 0.8500
67.8 350.04 0.5990 0.8820
72.6 350.1 0.6580 0.9050
77.09 350.06 0.7150 0.9260
82.25 350.08 0.7770 0.9450
85.95 350.12 0.8190 0.9570
90.33 350.11 0.8730 0.9710
94.87 350.05 0.9310 0.9850
99.46 350.06 0.9850 0.9970
100.68 350.02 1.0000 1.0000

Sources