Mixture of Benzene + Acetic acid, butyl ester

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Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

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
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. ρl - Mass density, kg/m3 (2)
  4. γ - Surface tension liquid-gas, N/m (2)
  5. Tboil - Boiling temperature at pressure P, K (2)
  6. Vapor Liquid Equilibrium at Constant Pressure (3)
  7. Excess molar volume, m3/mol (2)

Mole fraction of Benzene (1) [ref]

Operational condition: Pressure, kPa = 101.31 (Liquid)

Mole fraction of Benzene (1) - Liquid Mole fraction of Benzene (1) - Gas
0.0189 0.0617
0.0437 0.1361
0.0884 0.2533
0.1168 0.3181
0.1979 0.4765
0.2712 0.5846
0.3600 0.6814
0.4351 0.7410
0.4894 0.7830
0.5565 0.8238
0.6005 0.8495
0.6821 0.8914
0.7651 0.9276
0.7999 0.9410
0.8599 0.9608
0.9077 0.9751
0.9501 0.9875

Mole fraction of Benzene (1) [ref]

Operational condition: Pressure, kPa = 101.31 (Liquid)

Mole fraction of Benzene (1) - Liquid Mole fraction of Benzene (1) - Gas
0.0189 0.0617
0.0437 0.1361
0.0884 0.2533
0.1168 0.3181
0.1979 0.4765
0.2712 0.5846
0.3600 0.6814
0.4351 0.7410
0.4894 0.7830
0.5565 0.8238
0.6005 0.8495
0.6821 0.8914
0.7651 0.9276
0.7999 0.9410
0.8599 0.9608
0.9077 0.9751
0.9501 0.9875

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

Operational conditions:

Mole fraction of Acetic acid, butyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1269 -0.0075
0.2523 -0.0140
0.4029 -0.0209
0.4575 -0.0227
0.4958 -0.0245
0.5619 -0.0264
0.6599 -0.0274
0.7279 -0.0260
0.7714 -0.0245
0.8714 -0.0204

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

Operational conditions:

Mole fraction of Acetic acid, butyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1269 -0.0075
0.2523 -0.0140
0.4029 -0.0209
0.4575 -0.0227
0.4958 -0.0245
0.5619 -0.0264
0.6599 -0.0274
0.7279 -0.0260
0.7714 -0.0245
0.8714 -0.0204

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Benzene (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 876.12
0.1024 875.81
0.1831 875.49
0.2895 875.15
0.4054 874.78
0.4956 874.43
0.5951 874.03
0.7066 873.66
0.7940 873.49
0.9113 873.38

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Benzene (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 876.12
0.1024 875.81
0.1831 875.49
0.2895 875.15
0.4054 874.78
0.4956 874.43
0.5951 874.03
0.7066 873.66
0.7940 873.49
0.9113 873.38

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Benzene (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0561 0.0251
0.1063 0.0252
0.1514 0.0253
0.2049 0.0254
0.2521 0.0255
0.3085 0.0257
0.3529 0.0258
0.4027 0.0259
0.4573 0.0261
0.5028 0.0262
0.5534 0.0264
0.6058 0.0266
0.6532 0.0268
0.7041 0.0271
0.7521 0.0273
0.8006 0.0276
0.8561 0.0279
0.8992 0.0281
0.9500 0.0285

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Benzene (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0561 0.0251
0.1063 0.0252
0.1514 0.0253
0.2049 0.0254
0.2521 0.0255
0.3085 0.0257
0.3529 0.0258
0.4027 0.0259
0.4573 0.0261
0.5028 0.0262
0.5534 0.0264
0.6058 0.0266
0.6532 0.0268
0.7041 0.0271
0.7521 0.0273
0.8006 0.0276
0.8561 0.0279
0.8992 0.0281
0.9500 0.0285

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.31 (Liquid)

Mole fraction of Benzene (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0189 397.19
0.0437 395.18
0.0884 391.75
0.1168 389.71
0.1979 384.15
0.2712 379.77
0.3600 375.27
0.4351 372.14
0.4894 369.75
0.5565 367.22
0.6005 365.52
0.6821 362.54
0.7651 359.71
0.7999 358.58
0.8599 356.81
0.9077 355.47
0.9501 354.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.31 (Liquid)

Mole fraction of Benzene (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0189 397.19
0.0437 395.18
0.0884 391.75
0.1168 389.71
0.1979 384.15
0.2712 379.77
0.3600 375.27
0.4351 372.14
0.4894 369.75
0.5565 367.22
0.6005 365.52
0.6821 362.54
0.7651 359.71
0.7999 358.58
0.8599 356.81
0.9077 355.47
0.9501 354.25

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Benzene (1) - Vapour
395.75 0.0440 0.1380
393.55 0.0780 0.2250
391.55 0.1140 0.2980
388.85 0.1590 0.3840
385.95 0.2060 0.4730
383.85 0.2380 0.5220
378.85 0.3310 0.6530
377.55 0.3610 0.6820
373.45 0.4410 0.7660
369.05 0.5360 0.8330
366.45 0.5980 0.8700
364.15 0.6550 0.8920
362.25 0.7040 0.9150
360.35 0.7570 0.9340
357.75 0.8350 0.9590
356.65 0.8800 0.9710
355.75 0.9110 0.9800

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

x1[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Benzene (1) - Vapour
0.0657 0.1775
0.1385 0.3157
0.1735 0.3730
0.2235 0.4284
0.3195 0.5725
0.4470 0.7030
0.5215 0.7695
0.6475 0.8575
0.7607 0.9146
0.8345 0.9527
0.8930 0.9710
0.9340 0.9840
0.9560 0.9880

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Benzene (1) - Vapour
399.25 0.0000 0.0000
395.15 0.0500 0.1650
391.75 0.1000 0.3000
385.95 0.2000 0.5030
380.65 0.3000 0.6430
375.75 0.4000 0.7430
370.95 0.5000 0.8170
366.65 0.6000 0.8770
362.95 0.7000 0.9230
359.35 0.8000 0.9580
356.15 0.9000 0.9820
354.65 0.9500 0.9900
353.25 1.0000 1.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, butyl ester (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0901 4.2000e-08
0.2214 7.0000e-08
0.3662 7.6000e-08
0.4623 6.9000e-08
0.5430 6.0000e-08
0.6504 4.4000e-08
0.7052 3.6000e-08
0.7601 2.8000e-08
0.8505 1.7000e-08
0.9370 0.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, butyl ester (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0901 4.2000e-08
0.2214 7.0000e-08
0.3662 7.6000e-08
0.4623 6.9000e-08
0.5430 6.0000e-08
0.6504 4.4000e-08
0.7052 3.6000e-08
0.7601 2.8000e-08
0.8505 1.7000e-08
0.9370 0.0000

Sources