Mixture of Acetic acid, butyl ester + Cyclohexane

Excel

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

Cyclohexane

Name
Cyclohexane
InChI
InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key
XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula
C6H12
SMILES
C1CCCCC1
Mol. Weight (g/mol)
84.16
CAS
110-82-7
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Tboil - Boiling temperature at pressure P, K (2)
  3. Vapor Liquid Equilibrium at Constant Pressure
  4. Vapor Liquid Equilibrium at Constant Temperature (2)
  5. Excess molar volume, m3/mol (2)

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

Operational conditions:

Mole fraction of Acetic acid, butyl ester (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1409 0.8169
0.1975 1.0714
0.2672 1.2865
0.3389 1.3921
0.4035 1.3858
0.4961 1.2542
0.5517 1.1201
0.6466 0.8582
0.7965 0.4704
0.8311 0.3962
0.9061 0.2364

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

Operational conditions:

Mole fraction of Acetic acid, butyl ester (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1409 0.8169
0.1975 1.0714
0.2672 1.2865
0.3389 1.3921
0.4035 1.3858
0.4961 1.2542
0.5517 1.1201
0.6466 0.8582
0.7965 0.4704
0.8311 0.3962
0.9061 0.2364

Boiling temperature at pressure P, K [ref]

Fixed Measured
Pressure, kPa - Liquid Mole fraction of Acetic acid, butyl ester (1) - Liquid Boiling temperature at pressure P, K - Liquid
29.77 0.0000 317.95
29.77 0.0375 318.45
29.77 0.0769 319.05
29.77 0.1219 319.80
29.77 0.1664 320.60
29.77 0.2125 321.35
29.77 0.2570 322.15
29.77 0.2954 323.20
29.77 0.3539 324.25
29.77 0.4081 325.45
29.77 0.4544 326.75
29.77 0.4949 327.85
29.77 0.5512 330.20
29.77 0.6079 331.75
29.77 0.6622 334.25
29.77 0.7040 336.75
29.77 0.7590 339.40
29.77 0.8006 342.65
29.77 0.8442 346.05
29.77 0.8956 350.20
29.77 0.9425 354.85
29.77 1.0000 361.65
58.85 0.0000 336.85
58.85 0.0375 337.65
58.85 0.0769 338.35
58.85 0.1219 339.20
58.85 0.1664 340.05
58.85 0.2125 340.95
58.85 0.2570 341.85
58.85 0.2954 342.65
58.85 0.3539 344.00
58.85 0.4081 345.45
58.85 0.4544 346.90
58.85 0.4949 348.20
58.85 0.5512 350.65
58.85 0.6079 352.40
58.85 0.6622 354.85
58.85 0.7040 357.40
58.85 0.7590 360.50
58.85 0.8006 363.20
58.85 0.8442 366.90
58.85 0.8956 370.70
58.85 0.9425 375.55
58.85 1.0000 381.35
87.65 0.0000 349.15
87.65 0.0375 350.25
87.65 0.0769 351.00
87.65 0.1219 351.85
87.65 0.1664 352.75
87.65 0.2125 353.55
87.65 0.2570 354.55
87.65 0.2954 355.55
87.65 0.3539 356.85
87.65 0.4081 358.30
87.65 0.4544 359.90
87.65 0.4949 361.15
87.65 0.5512 363.65
87.65 0.6079 365.65
87.65 0.6622 367.85
87.65 0.7040 370.45
87.65 0.7590 374.75
87.65 0.8006 377.50
87.65 0.8442 380.95
87.65 0.8956 384.55
87.65 0.9425 388.55
87.65 1.0000 394.25

Boiling temperature at pressure P, K [ref]

Fixed Measured
Pressure, kPa - Liquid Mole fraction of Acetic acid, butyl ester (1) - Liquid Boiling temperature at pressure P, K - Liquid
29.77 0.0000 317.95
29.77 0.0375 318.45
29.77 0.0769 319.05
29.77 0.1219 319.80
29.77 0.1664 320.60
29.77 0.2125 321.35
29.77 0.2570 322.15
29.77 0.2954 323.20
29.77 0.3539 324.25
29.77 0.4081 325.45
29.77 0.4544 326.75
29.77 0.4949 327.85
29.77 0.5512 330.20
29.77 0.6079 331.75
29.77 0.6622 334.25
29.77 0.7040 336.75
29.77 0.7590 339.40
29.77 0.8006 342.65
29.77 0.8442 346.05
29.77 0.8956 350.20
29.77 0.9425 354.85
29.77 1.0000 361.65
58.85 0.0000 336.85
58.85 0.0375 337.65
58.85 0.0769 338.35
58.85 0.1219 339.20
58.85 0.1664 340.05
58.85 0.2125 340.95
58.85 0.2570 341.85
58.85 0.2954 342.65
58.85 0.3539 344.00
58.85 0.4081 345.45
58.85 0.4544 346.90
58.85 0.4949 348.20
58.85 0.5512 350.65
58.85 0.6079 352.40
58.85 0.6622 354.85
58.85 0.7040 357.40
58.85 0.7590 360.50
58.85 0.8006 363.20
58.85 0.8442 366.90
58.85 0.8956 370.70
58.85 0.9425 375.55
58.85 1.0000 381.35
87.65 0.0000 349.15
87.65 0.0375 350.25
87.65 0.0769 351.00
87.65 0.1219 351.85
87.65 0.1664 352.75
87.65 0.2125 353.55
87.65 0.2570 354.55
87.65 0.2954 355.55
87.65 0.3539 356.85
87.65 0.4081 358.30
87.65 0.4544 359.90
87.65 0.4949 361.15
87.65 0.5512 363.65
87.65 0.6079 365.65
87.65 0.6622 367.85
87.65 0.7040 370.45
87.65 0.7590 374.75
87.65 0.8006 377.50
87.65 0.8442 380.95
87.65 0.8956 384.55
87.65 0.9425 388.55
87.65 1.0000 394.25

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Cyclohexane (2) - Liquid y1[mol/mol] of Cyclohexane (2) - Vapour
396.65 0.0230 0.1020
390.05 0.0850 0.3090
384.25 0.1520 0.4640
378.45 0.2370 0.6020
373.75 0.3230 0.6880
370.35 0.3830 0.7450
368.15 0.4410 0.7770
363.55 0.5780 0.8420
360.75 0.6870 0.8860
357.85 0.8100 0.9280
357.75 0.8260 0.9340
355.25 0.9430 0.9750

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 335 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Cyclohexane (2) - Liquid y1[mol/mol] of Cyclohexane (2) - Vapour
9.895 0.0000 0.0000
16.136 0.0768 0.4149
21.793 0.1608 0.6052
22.12 0.1656 0.6137
27.694 0.2575 0.7211
30.656 0.3154 0.7652
35.834 0.4265 0.8235
40.423 0.5389 0.8640
44.454 0.6553 0.8979
48.055 0.7693 0.9276
51.316 0.8737 0.9565
53.644 0.9518 0.9810
54.727 0.9850 0.9930
55.195 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 350 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Cyclohexane (2) - Liquid y1[mol/mol] of Cyclohexane (2) - Vapour
18.94 0.0000 0.0000
29.071 0.0816 0.3890
38.358 0.1728 0.5825
47.283 0.2700 0.6988
50.968 0.3187 0.7333
59.336 0.4342 0.8036
66.892 0.5478 0.8488
73.289 0.6627 0.8866
78.923 0.7787 0.9207
83.81 0.8771 0.9516
87.662 0.9532 0.9795
89.33 0.9852 0.9923
89.99 1.0000 1.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, butyl ester (1) - Liquid Excess molar volume, m3/mol - Liquid
0.1062 3.4700e-07
0.1575 4.3500e-07
0.2230 5.2100e-07
0.3004 6.0400e-07
0.4851 6.7400e-07
0.4863 6.8500e-07
0.5412 6.5400e-07
0.6489 6.0700e-07
0.7350 4.9800e-07
0.7661 4.0600e-07
0.8854 1.9500e-07

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, butyl ester (1) - Liquid Excess molar volume, m3/mol - Liquid
0.1062 3.4700e-07
0.1575 4.3500e-07
0.2230 5.2100e-07
0.3004 6.0400e-07
0.4851 6.7400e-07
0.4863 6.8500e-07
0.5412 6.5400e-07
0.6489 6.0700e-07
0.7350 4.9800e-07
0.7661 4.0600e-07
0.8854 1.9500e-07

Sources