Mixture of Benzene + Acetonitrile

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

Acetonitrile

Name
Acetonitrile
InChI
InChI=1S/C2H3N/c1-2-3/h1H3
InChI Key
WEVYAHXRMPXWCK-UHFFFAOYSA-N
Formula
C2H3N
SMILES
CC#N
Mol. Weight (g/mol)
41.05
CAS
75-05-8
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. n0 - Refractive index (Na D-line) (2)
  3. ρl - Mass density, kg/m3 (2)
  4. Vapor Liquid Equilibrium at Constant Temperature (3)

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

Operational conditions:

Mole fraction of Acetonitrile (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2196 0.2399
0.2968 0.3190
0.3876 0.3768
0.4577 0.4289
0.5295 0.4415
0.6280 0.4522
0.7169 0.4239
0.7715 0.3988
0.8351 0.3188
0.8710 0.2692
0.9101 0.2021

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

Operational conditions:

Mole fraction of Acetonitrile (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2196 0.2399
0.2968 0.3190
0.3876 0.3768
0.4577 0.4289
0.5295 0.4415
0.6280 0.4522
0.7169 0.4239
0.7715 0.3988
0.8351 0.3188
0.8710 0.2692
0.9101 0.2021

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Benzene (1) - Liquid Refractive index (Na D-line) - Liquid
0.0500 1.3523
0.1000 1.3638
0.2000 1.3823
0.2998 1.402
0.4001 1.4217
0.4999 1.4378
0.6002 1.4531
0.7004 1.466
0.7997 1.4789
0.9002 1.4892
0.9506 1.4929

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Benzene (1) - Liquid Refractive index (Na D-line) - Liquid
0.0500 1.3523
0.1000 1.3638
0.2000 1.3823
0.2998 1.402
0.4001 1.4217
0.4999 1.4378
0.6002 1.4531
0.7004 1.466
0.7997 1.4789
0.9002 1.4892
0.9506 1.4929

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Benzene (1) - Liquid Mass density, kg/m3 - Liquid
0.0500 784.35
0.1000 791.68
0.2000 805.24
0.2998 817.45
0.4001 828.54
0.4999 838.46
0.6002 847.41
0.7004 855.36
0.7997 862.34
0.9002 868.48
0.9506 871.14

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Benzene (1) - Liquid Mass density, kg/m3 - Liquid
0.0500 784.35
0.1000 791.68
0.2000 805.24
0.2998 817.45
0.4001 828.54
0.4999 838.46
0.6002 847.41
0.7004 855.36
0.7997 862.34
0.9002 868.48
0.9506 871.14

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
27.778 0.0000 0.0000
30.038 0.0427 0.1084
32.331 0.1028 0.2131
34.372 0.1855 0.3087
35.792 0.2794 0.3843
36.778 0.4054 0.4625
36.978 0.4542 0.4902
37.068 0.4931 0.5115
36.996 0.6020 0.5726
36.457 0.7091 0.6393
35.285 0.8171 0.7217
33.553 0.9060 0.8182
31.957 0.9545 0.8944
29.819 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 293.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Benzene (1) - Vapour
9.799 0.0180 0.0540
10.106 0.0330 0.0960
10.599 0.0630 0.1610
10.639 0.0640 0.1620
11.106 0.0980 0.2210
11.386 0.1280 0.2560
11.719 0.1680 0.3000
11.852 0.1870 0.3210
11.932 0.1980 0.3300
12.186 0.2430 0.3700
12.226 0.2560 0.3760
12.359 0.2840 0.3950
12.439 0.3100 0.4120
12.466 0.3200 0.4170
12.612 0.3680 0.4420
12.666 0.4240 0.4730
12.679 0.4350 0.4790
12.679 0.4460 0.4840
12.692 0.4460 0.4860
12.719 0.4700 0.4980
12.692 0.4810 0.5010
12.746 0.5110 0.5180
12.732 0.5120 0.5190
12.746 0.5350 0.5320
12.719 0.5720 0.5510
12.719 0.6070 0.5710
12.666 0.6480 0.5930
12.639 0.6570 0.5970
12.612 0.6790 0.6120
12.519 0.7100 0.6320
12.359 0.7530 0.6620
12.186 0.7930 0.6950
12.119 0.8150 0.7090
12.012 0.8410 0.7340
11.866 0.8570 0.7570
11.706 0.8740 0.7670
11.386 0.9060 0.8080
11.252 0.9200 0.8290
11.106 0.9330 0.8490
11.026 0.9390 0.8600
10.879 0.9530 0.8830
10.692 0.9660 0.9060
10.506 0.9750 0.9300
10.319 0.9830 0.9500
10.186 0.9910 0.9720

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
28.851 0.0167 0.0484
32.651 0.1088 0.2251
34.784 0.2047 0.3241
36.157 0.3142 0.4013
37.01 0.4320 0.4854
37.157 0.4734 0.5038
37.117 0.5855 0.5639
36.664 0.6909 0.6330
35.81 0.7779 0.6982
33.131 0.9256 0.8469
31.251 0.9753 0.9318

Sources