Mixture of Benzene + 1-Butanol

Excel

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

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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Datasets

  1. Excess molar enthalpy (molar enthalpy (8)
  2. Pvap - Vapor or sublimation pressure, kPa (6)
  3. ρl - Mass density, kg/m3 (2)
  4. Vapor Liquid Equilibrium at Constant Pressure
  5. Vapor Liquid Equilibrium at Constant Temperature (2)

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

Operational conditions:

Mole fraction of Benzene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0494 0.1481
0.1007 0.3037
0.1497 0.4510
0.2007 0.5981
0.2495 0.7328
0.3002 0.8622
0.3507 0.9803
0.4010 1.0859
0.4493 1.1714
0.4993 1.2431
0.5492 1.2965
0.6010 1.328
0.6506 1.337
0.7001 1.3216
0.7495 1.2794
0.8007 1.1995
0.8498 1.0836
0.9007 0.9011
0.9495 0.6055

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

Operational conditions:

Mole fraction of Benzene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0504 0.1180
0.0997 0.2370
0.1497 0.3562
0.1997 0.4745
0.2505 0.5898
0.3001 0.6967
0.3506 0.7974
0.3999 0.8865
0.4502 0.9634
0.5002 1.0283
0.5501 1.076
0.5998 1.107
0.6505 1.1182
0.7000 1.1066
0.7503 1.0725
0.7996 1.0124
0.8497 0.9190
0.8996 0.7758
0.9504 0.5377

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

Operational conditions:

Mole fraction of Benzene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1430 0.3439
0.2530 0.6116
0.3370 0.8004
0.3800 0.8932
0.4250 1.0033
0.4910 1.1132
0.5500 1.1962
0.6020 1.2436
0.6550 1.2576
0.7230 1.16
0.7610 1.0303
0.8210 0.8231

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

Fixed Measured
Mole fraction of Benzene (1) - Liquid Pressure, kPa - Liquid Temperature, K - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.5000 101.00 303.15 1.1319

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

Operational conditions:

Mole fraction of Benzene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0494 0.1481
0.1007 0.3037
0.1497 0.4510
0.2007 0.5981
0.2495 0.7328
0.3002 0.8622
0.3507 0.9803
0.4010 1.0859
0.4493 1.1714
0.4993 1.2431
0.5492 1.2965
0.6010 1.328
0.6506 1.337
0.7001 1.3216
0.7495 1.2794
0.8007 1.1995
0.8498 1.0836
0.9007 0.9011
0.9495 0.6055

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

Operational conditions:

Mole fraction of Benzene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0504 0.1180
0.0997 0.2370
0.1497 0.3562
0.1997 0.4745
0.2505 0.5898
0.3001 0.6967
0.3506 0.7974
0.3999 0.8865
0.4502 0.9634
0.5002 1.0283
0.5501 1.076
0.5998 1.107
0.6505 1.1182
0.7000 1.1066
0.7503 1.0725
0.7996 1.0124
0.8497 0.9190
0.8996 0.7758
0.9504 0.5377

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

Operational conditions:

Mole fraction of Benzene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1430 0.3439
0.2530 0.6116
0.3370 0.8004
0.3800 0.8932
0.4250 1.0033
0.4910 1.1132
0.5500 1.1962
0.6020 1.2436
0.6550 1.2576
0.7230 1.16
0.7610 1.0303
0.8210 0.8231

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

Fixed Measured
Mole fraction of Benzene (1) - Liquid Pressure, kPa - Liquid Temperature, K - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.5000 101.00 303.15 1.1319

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0802 20.17
0.1690 20.28
0.2561 20.11
0.3150 19.84
0.3896 19.35
0.4603 18.61
0.5294 17.43
0.6035 16.49
0.6755 15.09
0.7565 13.29
0.8052 12.25
0.8465 10.72
0.9238 7.41
0.9789 4.03

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Benzene (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 2.49
0.0590 6.42
0.1080 9.18
0.1510 11.27
0.1980 13.23
0.2559 15.24
0.3023 16.58
0.3533 17.82
0.4027 18.84
0.4028 18.83
0.4501 19.66
0.4519 19.67
0.4997 20.38
0.5019 20.40
0.5497 21.00
0.5506 21.00
0.5999 21.55
0.6001 21.54
0.6497 22.03
0.7001 22.45
0.7502 22.83
0.8010 23.18
0.8591 23.52
0.9108 23.83
0.9547 24.14
1.0000 24.37

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.3006 22.45
0.6922 16.79

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0802 20.17
0.1690 20.28
0.2561 20.11
0.3150 19.84
0.3896 19.35
0.4603 18.61
0.5294 17.43
0.6035 16.49
0.6755 15.09
0.7565 13.29
0.8052 12.25
0.8465 10.72
0.9238 7.41
0.9789 4.03

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Benzene (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 2.49
0.0590 6.42
0.1080 9.18
0.1510 11.27
0.1980 13.23
0.2559 15.24
0.3023 16.58
0.3533 17.82
0.4027 18.84
0.4028 18.83
0.4501 19.66
0.4519 19.67
0.4997 20.38
0.5019 20.40
0.5497 21.00
0.5506 21.00
0.5999 21.55
0.6001 21.54
0.6497 22.03
0.7001 22.45
0.7502 22.83
0.8010 23.18
0.8591 23.52
0.9108 23.83
0.9547 24.14
1.0000 24.37

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.3006 22.45
0.6922 16.79

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 884.246
288.15 0.0193 882.483
288.15 0.0534 879.595
288.15 0.1013 875.72
288.15 0.1509 871.829
288.15 0.2016 867.984
288.15 0.2018 867.955
288.15 0.2500 864.382
288.15 0.2997 860.741
288.15 0.3532 856.936
288.15 0.4019 853.504
288.15 0.4525 850.0
288.15 0.4998 846.738
288.15 0.5532 843.129
288.15 0.6004 839.985
288.15 0.6493 836.693
288.15 0.7010 833.239
288.15 0.7502 829.979
288.15 0.7945 827.051
288.15 0.8511 823.296
288.15 0.8961 820.299
288.15 0.9510 816.663
288.15 1.0000 813.373
293.15 0.0000 878.918
293.15 0.0193 877.168
293.15 0.0534 874.309
293.15 0.1013 870.495
293.15 0.1509 866.677
293.15 0.2016 862.908
293.15 0.2018 862.874
293.15 0.2500 859.372
293.15 0.2997 855.806
293.15 0.3532 852.081
293.15 0.4019 848.721
293.15 0.4525 845.3
293.15 0.4998 842.111
293.15 0.5532 838.594
293.15 0.6004 835.529
293.15 0.6493 832.317
293.15 0.7010 828.949
293.15 0.7502 825.772
293.15 0.7945 822.92
293.15 0.8511 819.258
293.15 0.8961 816.336
293.15 0.9510 812.791
293.15 1.0000 809.573
298.15 0.0000 873.582
298.15 0.0193 871.844
298.15 0.0534 869.007
298.15 0.1013 865.255
298.15 0.1509 861.506
298.15 0.2016 857.807
298.15 0.2018 857.776
298.15 0.2500 854.344
298.15 0.2997 850.849
298.15 0.3532 847.201
298.15 0.4019 843.914
298.15 0.4525 840.574
298.15 0.4998 837.46
298.15 0.5532 834.03
298.15 0.6004 831.042
298.15 0.6493 827.91
298.15 0.7010 824.631
298.15 0.7502 821.537
298.15 0.7945 818.759
298.15 0.8511 815.196
298.15 0.8961 812.348
298.15 0.9510 808.897
298.15 1.0000 805.762
303.15 0.0000 868.233
303.15 0.0193 866.507
303.15 0.0534 863.694
303.15 0.1013 859.995
303.15 0.1509 856.309
303.15 0.2016 852.685
303.15 0.2018 852.651
303.15 0.2500 849.285
303.15 0.2997 845.866
303.15 0.3532 842.294
303.15 0.4019 839.08
303.15 0.4525 835.817
303.15 0.4998 832.778
303.15 0.5532 829.436
303.15 0.6004 826.525
303.15 0.6493 823.473
303.15 0.7010 820.282
303.15 0.7502 817.269
303.15 0.7945 814.569
303.15 0.8511 811.102
303.15 0.8961 808.331
303.15 0.9510 804.977
303.15 1.0000 801.923
308.15 0.0000 862.871
308.15 0.0193 861.158
308.15 0.0534 858.36
308.15 0.1013 854.713
308.15 0.1509 851.089
308.15 0.2016 847.536
308.15 0.2018 847.499
308.15 0.2500 844.201
308.15 0.2997 840.854
308.15 0.3532 837.357
308.15 0.4019 834.214
308.15 0.4525 831.029
308.15 0.4998 828.059
308.15 0.5532 824.804
308.15 0.6004 821.974
308.15 0.6493 819.001
308.15 0.7010 815.895
308.15 0.7502 812.965
308.15 0.7945 810.343
308.15 0.8511 806.975
308.15 0.8961 804.274
308.15 0.9510 801.025
308.15 1.0000 798.053
313.15 0.0000 857.498
313.15 0.0193 855.809
313.15 0.0534 853.019
313.15 0.1013 849.433
313.15 0.1509 845.861
313.15 0.2016 842.375
313.15 0.2018 842.342
313.15 0.2500 839.11
313.15 0.2997 835.83
313.15 0.3532 832.4
313.15 0.4019 829.324
313.15 0.4525 826.217
313.15 0.4998 823.32
313.15 0.5532 820.157
313.15 0.6004 817.402
313.15 0.6493 814.449
313.15 0.7010 811.483
313.15 0.7502 808.64
313.15 0.7945 806.094
313.15 0.8511 802.822
313.15 0.8961 800.189
313.15 0.9510 797.051
313.15 1.0000 794.147

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 884.246
288.15 0.0193 882.483
288.15 0.0534 879.595
288.15 0.1013 875.72
288.15 0.1509 871.829
288.15 0.2016 867.984
288.15 0.2018 867.955
288.15 0.2500 864.382
288.15 0.2997 860.741
288.15 0.3532 856.936
288.15 0.4019 853.504
288.15 0.4525 850.0
288.15 0.4998 846.738
288.15 0.5532 843.129
288.15 0.6004 839.985
288.15 0.6493 836.693
288.15 0.7010 833.239
288.15 0.7502 829.979
288.15 0.7945 827.051
288.15 0.8511 823.296
288.15 0.8961 820.299
288.15 0.9510 816.663
288.15 1.0000 813.373
293.15 0.0000 878.918
293.15 0.0193 877.168
293.15 0.0534 874.309
293.15 0.1013 870.495
293.15 0.1509 866.677
293.15 0.2016 862.908
293.15 0.2018 862.874
293.15 0.2500 859.372
293.15 0.2997 855.806
293.15 0.3532 852.081
293.15 0.4019 848.721
293.15 0.4525 845.3
293.15 0.4998 842.111
293.15 0.5532 838.594
293.15 0.6004 835.529
293.15 0.6493 832.317
293.15 0.7010 828.949
293.15 0.7502 825.772
293.15 0.7945 822.92
293.15 0.8511 819.258
293.15 0.8961 816.336
293.15 0.9510 812.791
293.15 1.0000 809.573
298.15 0.0000 873.582
298.15 0.0193 871.844
298.15 0.0534 869.007
298.15 0.1013 865.255
298.15 0.1509 861.506
298.15 0.2016 857.807
298.15 0.2018 857.776
298.15 0.2500 854.344
298.15 0.2997 850.849
298.15 0.3532 847.201
298.15 0.4019 843.914
298.15 0.4525 840.574
298.15 0.4998 837.46
298.15 0.5532 834.03
298.15 0.6004 831.042
298.15 0.6493 827.91
298.15 0.7010 824.631
298.15 0.7502 821.537
298.15 0.7945 818.759
298.15 0.8511 815.196
298.15 0.8961 812.348
298.15 0.9510 808.897
298.15 1.0000 805.762
303.15 0.0000 868.233
303.15 0.0193 866.507
303.15 0.0534 863.694
303.15 0.1013 859.995
303.15 0.1509 856.309
303.15 0.2016 852.685
303.15 0.2018 852.651
303.15 0.2500 849.285
303.15 0.2997 845.866
303.15 0.3532 842.294
303.15 0.4019 839.08
303.15 0.4525 835.817
303.15 0.4998 832.778
303.15 0.5532 829.436
303.15 0.6004 826.525
303.15 0.6493 823.473
303.15 0.7010 820.282
303.15 0.7502 817.269
303.15 0.7945 814.569
303.15 0.8511 811.102
303.15 0.8961 808.331
303.15 0.9510 804.977
303.15 1.0000 801.923
308.15 0.0000 862.871
308.15 0.0193 861.158
308.15 0.0534 858.36
308.15 0.1013 854.713
308.15 0.1509 851.089
308.15 0.2016 847.536
308.15 0.2018 847.499
308.15 0.2500 844.201
308.15 0.2997 840.854
308.15 0.3532 837.357
308.15 0.4019 834.214
308.15 0.4525 831.029
308.15 0.4998 828.059
308.15 0.5532 824.804
308.15 0.6004 821.974
308.15 0.6493 819.001
308.15 0.7010 815.895
308.15 0.7502 812.965
308.15 0.7945 810.343
308.15 0.8511 806.975
308.15 0.8961 804.274
308.15 0.9510 801.025
308.15 1.0000 798.053
313.15 0.0000 857.498
313.15 0.0193 855.809
313.15 0.0534 853.019
313.15 0.1013 849.433
313.15 0.1509 845.861
313.15 0.2016 842.375
313.15 0.2018 842.342
313.15 0.2500 839.11
313.15 0.2997 835.83
313.15 0.3532 832.4
313.15 0.4019 829.324
313.15 0.4525 826.217
313.15 0.4998 823.32
313.15 0.5532 820.157
313.15 0.6004 817.402
313.15 0.6493 814.449
313.15 0.7010 811.483
313.15 0.7502 808.64
313.15 0.7945 806.094
313.15 0.8511 802.822
313.15 0.8961 800.189
313.15 0.9510 797.051
313.15 1.0000 794.147

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
390.85 0.0000 0.0000
390.05 0.0040 0.0250
385.15 0.0400 0.2170
380.25 0.0850 0.3800
375.37 0.1340 0.5100
373.37 0.1610 0.5600
371.85 0.1800 0.5900
368.75 0.2340 0.6600
365.4 0.3080 0.7240
362.84 0.3690 0.7790
361.43 0.3970 0.7870
359.54 0.4750 0.8190
357.69 0.5600 0.8470
356.34 0.6310 0.8670
355.13 0.7140 0.8850
354.51 0.7900 0.9040
354.02 0.8480 0.9200
353.82 0.8970 0.9470
353.54 0.9280 0.9520
353.43 0.9420 0.9600
353.36 0.9480 0.9630
353.31 0.9540 0.9660
353.24 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 298.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Benzene (1) - Vapour
0.8533 0.0000 0.0000
6.879 0.2020 0.8870
8.986 0.3500 0.9190
10.386 0.5000 0.9300
11.439 0.6870 0.9410
11.906 0.8030 0.9550
12.586 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Benzene (1) - Vapour
15.204 0.1794 0.8107
19.844 0.2928 0.8689
22.837 0.3997 0.8946
25.014 0.5085 0.9115
26.309 0.5996 0.9221
27.422 0.6993 0.9316
28.371 0.8014 0.9421
29.184 0.9026 0.9568
29.503 0.9462 0.9677

Sources