Mixture of Benzene + Thiophene, tetrahydro-, 1,1-dioxide

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

Thiophene, tetrahydro-, 1,1-dioxide

Name
Thiophene, tetrahydro-, 1,1-dioxide
InChI
InChI=1S/C4H8O2S/c5-7(6)3-1-2-4-7/h1-4H2
InChI Key
HXJUTPCZVOIRIF-UHFFFAOYSA-N
Formula
C4H8O2S
SMILES
O=S1(=O)CCCC1
Mol. Weight (g/mol)
120.17
CAS
126-33-0
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. Activity coefficient (2)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (2)
  4. Vapor Liquid Equilibrium at Constant Pressure
  5. Vapor Liquid Equilibrium at Constant Temperature (2)

Activity coefficient of Benzene (1) [ref]

Operational conditions:

Temperature, K - Liquid Activity coefficient of Benzene (1) - Liquid
333.15 2.316
343.15 2.297
353.15 2.281
363.15 2.26
373.15 2.249

Activity coefficient of Benzene (1) [ref]

Operational conditions:

Temperature, K - Liquid Activity coefficient of Benzene (1) - Liquid
333.15 2.316
343.15 2.297
353.15 2.281
363.15 2.26
373.15 2.249

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene (1) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0101
303.15 0.1417 0.0061
303.15 0.2777 0.0040
303.15 0.3972 0.0028
303.15 0.5062 0.0021
303.15 0.6063 0.0016
303.15 0.6976 0.0012
303.15 0.7823 0.0010
303.15 0.8602 0.0008
303.15 0.9327 0.0007
303.15 1.0000 0.0006
323.15 0.0000 0.0062
323.15 0.1417 0.0039
323.15 0.2777 0.0027
323.15 0.3972 0.0019
323.15 0.5062 0.0015
323.15 0.6063 0.0011
323.15 0.6976 0.0009
323.15 0.7823 0.0007
323.15 0.8602 0.0006
323.15 0.9327 0.0005
323.15 1.0000 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene (1) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0101
303.15 0.1417 0.0061
303.15 0.2777 0.0040
303.15 0.3972 0.0028
303.15 0.5062 0.0021
303.15 0.6063 0.0016
303.15 0.6976 0.0012
303.15 0.7823 0.0010
303.15 0.8602 0.0008
303.15 0.9327 0.0007
303.15 1.0000 0.0006
323.15 0.0000 0.0062
323.15 0.1417 0.0039
323.15 0.2777 0.0027
323.15 0.3972 0.0019
323.15 0.5062 0.0015
323.15 0.6063 0.0011
323.15 0.6976 0.0009
323.15 0.7823 0.0007
323.15 0.8602 0.0006
323.15 0.9327 0.0005
323.15 1.0000 0.0004

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene (1) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 1260.8
303.15 0.1417 1211.21
303.15 0.2777 1164.97
303.15 0.3972 1120.9
303.15 0.5062 1079.14
303.15 0.6063 1039.2
303.15 0.6976 1001.76
303.15 0.7823 965.81
303.15 0.8602 931.48
303.15 0.9327 897.62
303.15 1.0000 868.21
323.15 0.0000 1243.36
323.15 0.1417 1193.23
323.15 0.2777 1146.6
323.15 0.3972 1102.13
323.15 0.5062 1059.91
323.15 0.6063 1019.54
323.15 0.6976 981.64
323.15 0.7823 945.38
323.15 0.8602 910.67
323.15 0.9327 876.47
323.15 1.0000 846.65

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene (1) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 1260.8
303.15 0.1417 1211.21
303.15 0.2777 1164.97
303.15 0.3972 1120.9
303.15 0.5062 1079.14
303.15 0.6063 1039.2
303.15 0.6976 1001.76
303.15 0.7823 965.81
303.15 0.8602 931.48
303.15 0.9327 897.62
303.15 1.0000 868.21
323.15 0.0000 1243.36
323.15 0.1417 1193.23
323.15 0.2777 1146.6
323.15 0.3972 1102.13
323.15 0.5062 1059.91
323.15 0.6063 1019.54
323.15 0.6976 981.64
323.15 0.7823 945.38
323.15 0.8602 910.67
323.15 0.9327 876.47
323.15 1.0000 846.65

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
412.65 0.1315 0.9905
390.75 0.2027 0.9946
380.35 0.2822 0.9964
372.15 0.3609 0.9976
368.05 0.4386 0.9980
364.15 0.5356 0.9986
360.95 0.6364 0.9990
359.25 0.7495 0.9992
356.75 0.8425 0.9994

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 303.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid
1.44 0.0410
4.44 0.1350
5.733 0.1830
7.039 0.2400
7.866 0.2830
8.706 0.3320
9.666 0.3810
9.853 0.4040
10.839 0.4710
11.266 0.5080
12.226 0.5930
12.532 0.6230
12.759 0.6520
13.132 0.6960
13.439 0.7280
13.826 0.7760
14.212 0.8180
14.599 0.8770
14.932 0.9140
15.145 0.9450
15.439 0.9660
15.799 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 303.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid
0.0093 0.0000
3.42 0.1002
6.21 0.1998
7.739 0.2968
9.761 0.4029
11.44 0.5137
12.39 0.6047
13.27 0.6990
14.12 0.8028
14.769 0.9039
15.911 1.0000

Sources