Mixture of p-Xylene + Thiophene, tetrahydro-, 1,1-dioxide

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p-Xylene

Name
p-Xylene
InChI
InChI=1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3
InChI Key
URLKBWYHVLBVBO-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccc(C)cc1
Mol. Weight (g/mol)
106.17
CAS
106-42-3

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
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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 p-Xylene (1) [ref]

Operational conditions:

Temperature, K - Liquid Activity coefficient of p-Xylene (1) - Liquid
333.15 5.508
343.15 5.249
353.15 5.105
363.15 4.877
373.15 4.761

Activity coefficient of p-Xylene (1) [ref]

Operational conditions:

Temperature, K - Liquid Activity coefficient of p-Xylene (1) - Liquid
333.15 5.508
343.15 5.249
353.15 5.105
363.15 4.877
373.15 4.761

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0101
303.15 0.1118 0.0062
303.15 0.2206 0.0041
303.15 0.3266 0.0029
303.15 0.4301 0.0021
303.15 0.5310 0.0016
303.15 0.6293 0.0013
303.15 0.7252 0.0010
303.15 0.8191 0.0008
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 0.2206 0.0027
323.15 0.3266 0.0020
323.15 0.4301 0.0015
323.15 0.5310 0.0012
323.15 0.6293 0.0009
323.15 0.7252 0.0007
323.15 0.8191 0.0006
323.15 0.9106 0.0005
323.15 1.0000 0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0101
303.15 0.1118 0.0062
303.15 0.2206 0.0041
303.15 0.3266 0.0029
303.15 0.4301 0.0021
303.15 0.5310 0.0016
303.15 0.6293 0.0013
303.15 0.7252 0.0010
303.15 0.8191 0.0008
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 0.2206 0.0027
323.15 0.3266 0.0020
323.15 0.4301 0.0015
323.15 0.5310 0.0012
323.15 0.6293 0.0009
323.15 0.7252 0.0007
323.15 0.8191 0.0006
323.15 0.9106 0.0005
323.15 1.0000 0.0005

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 1260.8
303.15 0.1118 1207.85
303.15 0.2206 1158.09
303.15 0.3266 1110.7
303.15 0.4301 1066.73
303.15 0.5310 1025.22
303.15 0.6293 986.5
303.15 0.7252 950.04
303.15 0.8191 915.82
303.15 0.9106 883.35
303.15 1.0000 852.35
323.15 0.0000 1243.36
323.15 0.1118 1190.21
323.15 0.2206 1140.37
323.15 0.3266 1092.99
323.15 0.4301 1049.03
323.15 0.5310 1007.58
323.15 0.6293 968.88
323.15 0.7252 932.4
323.15 0.8191 898.26
323.15 0.9106 865.85
323.15 1.0000 834.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 1260.8
303.15 0.1118 1207.85
303.15 0.2206 1158.09
303.15 0.3266 1110.7
303.15 0.4301 1066.73
303.15 0.5310 1025.22
303.15 0.6293 986.5
303.15 0.7252 950.04
303.15 0.8191 915.82
303.15 0.9106 883.35
303.15 1.0000 852.35
323.15 0.0000 1243.36
323.15 0.1118 1190.21
323.15 0.2206 1140.37
323.15 0.3266 1092.99
323.15 0.4301 1049.03
323.15 0.5310 1007.58
323.15 0.6293 968.88
323.15 0.7252 932.4
323.15 0.8191 898.26
323.15 0.9106 865.85
323.15 1.0000 834.9

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

T [K] - VLE x1[mol/mol] of p-Xylene (1) - Liquid
560.47 0.0000
452.45 0.0979
445.76 0.1294
443.03 0.1450
437.38 0.1678
434.24 0.1979
431.73 0.2146
429.13 0.2434
427.0 0.2539
424.43 0.2932
422.96 0.3201
421.59 0.3879
420.3 0.4381
418.45 0.5382
415.12 0.8042
412.97 0.9459
411.6 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 348.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of p-Xylene (1) - Liquid y1[mol/mol] of p-Xylene (1) - Vapour
3.541 0.0820 0.9951
7.602 0.2210 0.9980
7.797 0.2300 0.9981
10.066 0.3780 0.9986
10.951 0.4990 0.9986
11.299 0.6060 0.9986
11.482 0.7290 0.9989
11.74 0.8460 0.9987

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 348.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of p-Xylene (1) - Liquid y1[mol/mol] of p-Xylene (1) - Vapour
3.541 0.0820 0.9951
7.602 0.2210 0.9980
7.795 0.2300 0.9981
10.066 0.3780 0.9986
10.951 0.4990 0.9986
11.299 0.6060 0.9986
11.482 0.7290 0.9986
11.74 0.8460 0.9987

Sources