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

Datasets

1. Activity coefficient (2)
2. Mole fraction (4)
3. η - Viscosity, Pa*s (4)
4. ρ_l - Mass density, kg/m3 (4)
5. T_boil - Boiling temperature at pressure P, K (4)

Activity coefficient of Ethylbenzene (1) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of Ethylbenzene (1) - Liquid
333.15	4.819
343.15	4.646
353.15	4.483
363.15	4.353
373.15	4.26

Activity coefficient of Ethylbenzene (1) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of Ethylbenzene (1) - Liquid
333.15	4.819
343.15	4.646
353.15	4.483
363.15	4.353
373.15	4.26

Mole fraction of Ethylbenzene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Ethylbenzene (1) - Liquid	Mole fraction of Ethylbenzene (1) - Gas
0.0337	0.8111
0.0613	0.9120
0.0660	0.9296
0.0949	0.9531
0.1462	0.9698
0.2184	0.9823
0.3436	0.9857
0.4788	0.9899
0.5405	0.9909
0.6459	0.9914
0.7983	0.9974
0.8958	0.9982

Mole fraction of Ethylbenzene (1) [ref]

Fixed		Measured
Mole fraction of Ethylbenzene (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethylbenzene (1) - Gas
0.0880	10.00	0.9938
0.0890	5.00	0.9938
0.0920	20.00	0.9878
0.1970	20.00	0.9959
0.2010	10.00	0.9971
0.2020	5.00	0.9979
0.2570	10.00	0.9977
0.2570	20.00	0.9965
0.2580	5.00	0.9984
0.3470	20.00	0.9972
0.3480	5.00	0.9987
0.3480	10.00	0.9981
0.4290	5.00	0.9989
0.4300	20.00	0.9976
0.4310	10.00	0.9984
0.5120	10.00	0.9986
0.5150	20.00	0.9980
0.5170	5.00	0.9991
0.6500	5.00	0.9993
0.6500	20.00	0.9985
0.6510	10.00	0.9990
0.7370	5.00	0.9995
0.7400	10.00	0.9993
0.7410	20.00	0.9989
0.8290	5.00	0.9997
0.8310	10.00	0.9995
0.8330	20.00	0.9993
0.9080	5.00	0.9998
0.9120	10.00	0.9998
0.9130	20.00	0.9996

Mole fraction of Ethylbenzene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Ethylbenzene (1) - Liquid	Mole fraction of Ethylbenzene (1) - Gas
0.0337	0.8111
0.0613	0.9120
0.0660	0.9296
0.0949	0.9531
0.1462	0.9698
0.2184	0.9823
0.3436	0.9857
0.4788	0.9899
0.5405	0.9909
0.6459	0.9914
0.7983	0.9974
0.8958	0.9982

Mole fraction of Ethylbenzene (1) [ref]

Fixed		Measured
Mole fraction of Ethylbenzene (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethylbenzene (1) - Gas
0.0880	10.00	0.9938
0.0890	5.00	0.9938
0.0920	20.00	0.9878
0.1970	20.00	0.9959
0.2010	10.00	0.9971
0.2020	5.00	0.9979
0.2570	10.00	0.9977
0.2570	20.00	0.9965
0.2580	5.00	0.9984
0.3470	20.00	0.9972
0.3480	5.00	0.9987
0.3480	10.00	0.9981
0.4290	5.00	0.9989
0.4300	20.00	0.9976
0.4310	10.00	0.9984
0.5120	10.00	0.9986
0.5150	20.00	0.9980
0.5170	5.00	0.9991
0.6500	5.00	0.9993
0.6500	20.00	0.9985
0.6510	10.00	0.9990
0.7370	5.00	0.9995
0.7400	10.00	0.9993
0.7410	20.00	0.9989
0.8290	5.00	0.9997
0.8310	10.00	0.9995
0.8330	20.00	0.9993
0.9080	5.00	0.9998
0.9120	10.00	0.9998
0.9130	20.00	0.9996

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0101
303.15	0.1118	0.0062
303.15	0.2205	0.0042
303.15	0.3267	0.0029
303.15	0.4301	0.0022
303.15	0.5309	0.0015
303.15	0.6293	0.0013
303.15	0.7254	0.0011
303.15	0.8194	0.0009
303.15	0.9106	0.0007
303.15	1.0000	0.0006
323.15	0.0000	0.0062
323.15	0.1118	0.0040
323.15	0.2205	0.0028
323.15	0.3267	0.0020
323.15	0.4301	0.0016
323.15	0.5309	0.0011
323.15	0.6293	0.0010
323.15	0.7254	0.0008
323.15	0.8194	0.0007
323.15	0.9106	0.0006
323.15	1.0000	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0101
303.15	0.1118	0.0062
303.15	0.2205	0.0042
303.15	0.3267	0.0029
303.15	0.4301	0.0022
303.15	0.5309	0.0015
303.15	0.6293	0.0013
303.15	0.7254	0.0011
303.15	0.8194	0.0009
303.15	0.9106	0.0007
303.15	1.0000	0.0006
313.15	0.0000	0.0078
313.15	0.1118	0.0049
313.15	0.2205	0.0034
313.15	0.3267	0.0025
313.15	0.4301	0.0018
313.15	0.5309	0.0013
313.15	0.6293	0.0011
313.15	0.7254	0.0009
313.15	0.8194	0.0008
313.15	0.9106	0.0006
313.15	1.0000	0.0005
323.15	0.0000	0.0062
323.15	0.1118	0.0040
323.15	0.2205	0.0028
323.15	0.3267	0.0020
323.15	0.4301	0.0016
323.15	0.5309	0.0011
323.15	0.6293	0.0010
323.15	0.7254	0.0008
323.15	0.8194	0.0007
323.15	0.9106	0.0006
323.15	1.0000	0.0005
333.15	0.0000	0.0050
333.15	0.1118	0.0033
333.15	0.2205	0.0024
333.15	0.3267	0.0018
333.15	0.4301	0.0013
333.15	0.5309	0.0010
333.15	0.6293	0.0009
333.15	0.7254	0.0007
333.15	0.8194	0.0006
333.15	0.9106	0.0005
333.15	1.0000	0.0004
343.15	0.0000	0.0041
343.15	0.1118	0.0028
343.15	0.2205	0.0020
343.15	0.3267	0.0015
343.15	0.4301	0.0012
343.15	0.5309	0.0009
343.15	0.6293	0.0008
343.15	0.7254	0.0006
343.15	0.8194	0.0005
343.15	0.9106	0.0005
343.15	1.0000	0.0004
353.15	0.0000	0.0034
353.15	0.1118	0.0024
353.15	0.2205	0.0017
353.15	0.3267	0.0013
353.15	0.4301	0.0010
353.15	0.5309	0.0008
353.15	0.6293	0.0007
353.15	0.7254	0.0006
353.15	0.8194	0.0005
353.15	0.9106	0.0004
353.15	1.0000	0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0101
303.15	0.1118	0.0062
303.15	0.2205	0.0042
303.15	0.3267	0.0029
303.15	0.4301	0.0022
303.15	0.5309	0.0015
303.15	0.6293	0.0013
303.15	0.7254	0.0011
303.15	0.8194	0.0009
303.15	0.9106	0.0007
303.15	1.0000	0.0006
323.15	0.0000	0.0062
323.15	0.1118	0.0040
323.15	0.2205	0.0028
323.15	0.3267	0.0020
323.15	0.4301	0.0016
323.15	0.5309	0.0011
323.15	0.6293	0.0010
323.15	0.7254	0.0008
323.15	0.8194	0.0007
323.15	0.9106	0.0006
323.15	1.0000	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0101
303.15	0.1118	0.0062
303.15	0.2205	0.0042
303.15	0.3267	0.0029
303.15	0.4301	0.0022
303.15	0.5309	0.0015
303.15	0.6293	0.0013
303.15	0.7254	0.0011
303.15	0.8194	0.0009
303.15	0.9106	0.0007
303.15	1.0000	0.0006
313.15	0.0000	0.0078
313.15	0.1118	0.0049
313.15	0.2205	0.0034
313.15	0.3267	0.0025
313.15	0.4301	0.0018
313.15	0.5309	0.0013
313.15	0.6293	0.0011
313.15	0.7254	0.0009
313.15	0.8194	0.0008
313.15	0.9106	0.0006
313.15	1.0000	0.0005
323.15	0.0000	0.0062
323.15	0.1118	0.0040
323.15	0.2205	0.0028
323.15	0.3267	0.0020
323.15	0.4301	0.0016
323.15	0.5309	0.0011
323.15	0.6293	0.0010
323.15	0.7254	0.0008
323.15	0.8194	0.0007
323.15	0.9106	0.0006
323.15	1.0000	0.0005
333.15	0.0000	0.0050
333.15	0.1118	0.0033
333.15	0.2205	0.0024
333.15	0.3267	0.0018
333.15	0.4301	0.0013
333.15	0.5309	0.0010
333.15	0.6293	0.0009
333.15	0.7254	0.0007
333.15	0.8194	0.0006
333.15	0.9106	0.0005
333.15	1.0000	0.0004
343.15	0.0000	0.0041
343.15	0.1118	0.0028
343.15	0.2205	0.0020
343.15	0.3267	0.0015
343.15	0.4301	0.0012
343.15	0.5309	0.0009
343.15	0.6293	0.0008
343.15	0.7254	0.0006
343.15	0.8194	0.0005
343.15	0.9106	0.0005
343.15	1.0000	0.0004
353.15	0.0000	0.0034
353.15	0.1118	0.0024
353.15	0.2205	0.0017
353.15	0.3267	0.0013
353.15	0.4301	0.0010
353.15	0.5309	0.0008
353.15	0.6293	0.0007
353.15	0.7254	0.0006
353.15	0.8194	0.0005
353.15	0.9106	0.0004
353.15	1.0000	0.0004

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	1260.8
303.15	0.1118	1209.27
303.15	0.2205	1160.4
303.15	0.3267	1114.66
303.15	0.4301	1071.65
303.15	0.5309	1031.19
303.15	0.6293	993.33
303.15	0.7254	957.17
303.15	0.8194	923.09
303.15	0.9106	890.45
303.15	1.0000	859.95
323.15	0.0000	1243.36
323.15	0.1118	1191.64
323.15	0.2205	1142.7
323.15	0.3267	1096.92
323.15	0.4301	1053.9
323.15	0.5309	1013.47
323.15	0.6293	975.58
323.15	0.7254	939.43
323.15	0.8194	905.36
323.15	0.9106	872.72
323.15	1.0000	842.27

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	1260.8
303.15	0.1118	1209.27
303.15	0.2205	1160.4
303.15	0.3267	1114.66
303.15	0.4301	1071.65
303.15	0.5309	1031.19
303.15	0.6293	993.33
303.15	0.7254	957.17
303.15	0.8194	923.09
303.15	0.9106	890.45
303.15	1.0000	859.95
313.15	0.0000	1251.9
313.15	0.1118	1200.44
313.15	0.2205	1151.53
313.15	0.3267	1105.77
313.15	0.4301	1062.77
313.15	0.5309	1022.32
313.15	0.6293	984.45
313.15	0.7254	948.31
313.15	0.8194	914.23
313.15	0.9106	881.6
313.15	1.0000	851.14
323.15	0.0000	1243.36
323.15	0.1118	1191.64
323.15	0.2205	1142.7
323.15	0.3267	1096.92
323.15	0.4301	1053.9
323.15	0.5309	1013.47
323.15	0.6293	975.58
323.15	0.7254	939.43
323.15	0.8194	905.36
323.15	0.9106	872.72
323.15	1.0000	842.27
333.15	0.0000	1234.62
333.15	0.1118	1182.85
333.15	0.2205	1133.86
333.15	0.3267	1088.06
333.15	0.4301	1045.02
333.15	0.5309	1004.57
333.15	0.6293	966.66
333.15	0.7254	930.5
333.15	0.8194	896.41
333.15	0.9106	863.76
333.15	1.0000	833.34
343.15	0.0000	1225.92
343.15	0.1118	1173.93
343.15	0.2205	1124.89
343.15	0.3267	1079.06
343.15	0.4301	1036.02
343.15	0.5309	995.54
343.15	0.6293	957.62
343.15	0.7254	921.43
343.15	0.8194	887.32
343.15	0.9106	854.67
343.15	1.0000	824.26
353.15	0.0000	1216.8
353.15	0.1118	1165.14
353.15	0.2205	1116.08
353.15	0.3267	1070.18
353.15	0.4301	1027.1
353.15	0.5309	986.58
353.15	0.6293	948.63
353.15	0.7254	912.4
353.15	0.8194	878.28
353.15	0.9106	845.58
353.15	1.0000	815.18

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	1260.8
303.15	0.1118	1209.27
303.15	0.2205	1160.4
303.15	0.3267	1114.66
303.15	0.4301	1071.65
303.15	0.5309	1031.19
303.15	0.6293	993.33
303.15	0.7254	957.17
303.15	0.8194	923.09
303.15	0.9106	890.45
303.15	1.0000	859.95
323.15	0.0000	1243.36
323.15	0.1118	1191.64
323.15	0.2205	1142.7
323.15	0.3267	1096.92
323.15	0.4301	1053.9
323.15	0.5309	1013.47
323.15	0.6293	975.58
323.15	0.7254	939.43
323.15	0.8194	905.36
323.15	0.9106	872.72
323.15	1.0000	842.27

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	1260.8
303.15	0.1118	1209.27
303.15	0.2205	1160.4
303.15	0.3267	1114.66
303.15	0.4301	1071.65
303.15	0.5309	1031.19
303.15	0.6293	993.33
303.15	0.7254	957.17
303.15	0.8194	923.09
303.15	0.9106	890.45
303.15	1.0000	859.95
313.15	0.0000	1251.9
313.15	0.1118	1200.44
313.15	0.2205	1151.53
313.15	0.3267	1105.77
313.15	0.4301	1062.77
313.15	0.5309	1022.32
313.15	0.6293	984.45
313.15	0.7254	948.31
313.15	0.8194	914.23
313.15	0.9106	881.6
313.15	1.0000	851.14
323.15	0.0000	1243.36
323.15	0.1118	1191.64
323.15	0.2205	1142.7
323.15	0.3267	1096.92
323.15	0.4301	1053.9
323.15	0.5309	1013.47
323.15	0.6293	975.58
323.15	0.7254	939.43
323.15	0.8194	905.36
323.15	0.9106	872.72
323.15	1.0000	842.27
333.15	0.0000	1234.62
333.15	0.1118	1182.85
333.15	0.2205	1133.86
333.15	0.3267	1088.06
333.15	0.4301	1045.02
333.15	0.5309	1004.57
333.15	0.6293	966.66
333.15	0.7254	930.5
333.15	0.8194	896.41
333.15	0.9106	863.76
333.15	1.0000	833.34
343.15	0.0000	1225.92
343.15	0.1118	1173.93
343.15	0.2205	1124.89
343.15	0.3267	1079.06
343.15	0.4301	1036.02
343.15	0.5309	995.54
343.15	0.6293	957.62
343.15	0.7254	921.43
343.15	0.8194	887.32
343.15	0.9106	854.67
343.15	1.0000	824.26
353.15	0.0000	1216.8
353.15	0.1118	1165.14
353.15	0.2205	1116.08
353.15	0.3267	1070.18
353.15	0.4301	1027.1
353.15	0.5309	986.58
353.15	0.6293	948.63
353.15	0.7254	912.4
353.15	0.8194	878.28
353.15	0.9106	845.58
353.15	1.0000	815.18

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Ethylbenzene (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0337	492.15
0.0613	473.00
0.0660	463.60
0.0949	456.60
0.1462	446.35
0.2184	432.07
0.3436	425.50
0.4788	419.05
0.5405	417.75
0.6459	415.95
0.7983	413.39
0.8958	411.69

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethylbenzene (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0880	10.00	361.50
0.0890	5.00	343.60
0.0920	20.00	379.40
0.1970	20.00	361.40
0.2010	10.00	344.80
0.2020	5.00	329.60
0.2570	10.00	342.20
0.2570	20.00	360.30
0.2580	5.00	326.90
0.3470	20.00	358.40
0.3480	5.00	325.90
0.3480	10.00	341.10
0.4290	5.00	325.90
0.4300	20.00	358.40
0.4310	10.00	341.00
0.5120	10.00	340.80
0.5150	20.00	358.30
0.5170	5.00	325.90
0.6500	5.00	325.80
0.6500	20.00	358.40
0.6510	10.00	340.70
0.7370	5.00	325.50
0.7400	10.00	340.60
0.7410	20.00	358.20
0.8290	5.00	325.30
0.8310	10.00	340.50
0.8330	20.00	357.90
0.9080	5.00	325.00
0.9120	10.00	340.40
0.9130	20.00	357.80

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Ethylbenzene (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0337	492.15
0.0613	473.00
0.0660	463.60
0.0949	456.60
0.1462	446.35
0.2184	432.07
0.3436	425.50
0.4788	419.05
0.5405	417.75
0.6459	415.95
0.7983	413.39
0.8958	411.69

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethylbenzene (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0880	10.00	361.50
0.0890	5.00	343.60
0.0920	20.00	379.40
0.1970	20.00	361.40
0.2010	10.00	344.80
0.2020	5.00	329.60
0.2570	10.00	342.20
0.2570	20.00	360.30
0.2580	5.00	326.90
0.3470	20.00	358.40
0.3480	5.00	325.90
0.3480	10.00	341.10
0.4290	5.00	325.90
0.4300	20.00	358.40
0.4310	10.00	341.00
0.5120	10.00	340.80
0.5150	20.00	358.30
0.5170	5.00	325.90
0.6500	5.00	325.80
0.6500	20.00	358.40
0.6510	10.00	340.70
0.7370	5.00	325.50
0.7400	10.00	340.60
0.7410	20.00	358.20
0.8290	5.00	325.30
0.8310	10.00	340.50
0.8330	20.00	357.90
0.9080	5.00	325.00
0.9120	10.00	340.40
0.9130	20.00	357.80

Sources

• Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
• Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
• Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
• Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
• Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography