Mixture of Isopropyl Alcohol + Thiophene, tetrahydro-, 1,1-dioxide

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Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

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. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)
  3. Vapor Liquid Equilibrium at Constant Temperature (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
0.0000 303.15 0.0018
0.0750 303.15 0.0016
0.1640 303.15 0.0017
0.2500 303.15 0.0019
0.3530 303.15 0.0021
0.4370 303.15 0.0024
0.5360 303.15 0.0029
0.6560 303.15 0.0037
0.7680 303.15 0.0050
0.8800 303.15 0.0069
1.0000 303.15 0.0104
0.0000 313.15 0.0013
0.0750 313.15 0.0013
0.1640 313.15 0.0013
0.2500 313.15 0.0015
0.3530 313.15 0.0017
0.4370 313.15 0.0020
0.5360 313.15 0.0024
0.6560 313.15 0.0030
0.7680 313.15 0.0040
0.8800 313.15 0.0055
1.0000 313.15 0.0081
0.0000 323.15 0.0010
0.0750 323.15 0.0010
0.1640 323.15 0.0011
0.2500 323.15 0.0012
0.3530 323.15 0.0014
0.4370 323.15 0.0016
0.5360 323.15 0.0019
0.6560 323.15 0.0025
0.7680 323.15 0.0033
0.8800 323.15 0.0044
1.0000 323.15 0.0065
0.0000 333.15 0.0008
0.0750 333.15 0.0008
0.1640 333.15 0.0009
0.2500 333.15 0.0010
0.3530 333.15 0.0012
0.4370 333.15 0.0014
0.5360 333.15 0.0016
0.6560 333.15 0.0021
0.7680 333.15 0.0027
0.8800 333.15 0.0037
1.0000 333.15 0.0052
0.0000 343.15 0.0006
0.0750 343.15 0.0007
0.1640 343.15 0.0007
0.2500 343.15 0.0008
0.3530 343.15 0.0010
0.4370 343.15 0.0011
0.5360 343.15 0.0014
0.6560 343.15 0.0018
0.7680 343.15 0.0023
0.8800 343.15 0.0031
1.0000 343.15 0.0043

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
0.0000 303.15 0.0018
0.0750 303.15 0.0016
0.1640 303.15 0.0017
0.2500 303.15 0.0019
0.3530 303.15 0.0021
0.4370 303.15 0.0024
0.5360 303.15 0.0029
0.6560 303.15 0.0037
0.7680 303.15 0.0050
0.8800 303.15 0.0069
1.0000 303.15 0.0104
0.0000 313.15 0.0013
0.0750 313.15 0.0013
0.1640 313.15 0.0013
0.2500 313.15 0.0015
0.3530 313.15 0.0017
0.4370 313.15 0.0020
0.5360 313.15 0.0024
0.6560 313.15 0.0030
0.7680 313.15 0.0040
0.8800 313.15 0.0055
1.0000 313.15 0.0081
0.0000 323.15 0.0010
0.0750 323.15 0.0010
0.1640 323.15 0.0011
0.2500 323.15 0.0012
0.3530 323.15 0.0014
0.4370 323.15 0.0016
0.5360 323.15 0.0019
0.6560 323.15 0.0025
0.7680 323.15 0.0033
0.8800 323.15 0.0044
1.0000 323.15 0.0065
0.0000 333.15 0.0008
0.0750 333.15 0.0008
0.1640 333.15 0.0009
0.2500 333.15 0.0010
0.3530 333.15 0.0012
0.4370 333.15 0.0014
0.5360 333.15 0.0016
0.6560 333.15 0.0021
0.7680 333.15 0.0027
0.8800 333.15 0.0037
1.0000 333.15 0.0052
0.0000 343.15 0.0006
0.0750 343.15 0.0007
0.1640 343.15 0.0007
0.2500 343.15 0.0008
0.3530 343.15 0.0010
0.4370 343.15 0.0011
0.5360 343.15 0.0014
0.6560 343.15 0.0018
0.7680 343.15 0.0023
0.8800 343.15 0.0031
1.0000 343.15 0.0043

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0000 303.15 777.5
0.0750 303.15 823.6
0.1640 303.15 875.9
0.2500 303.15 924.0
0.3530 303.15 978.7
0.4370 303.15 1021.3
0.5360 303.15 1069.3
0.6560 303.15 1124.3
0.7680 303.15 1172.1
0.8800 303.15 1219.3
1.0000 303.15 1262.9
0.0000 313.15 768.8
0.0750 313.15 814.6
0.1640 313.15 866.9
0.2500 313.15 914.8
0.3530 313.15 969.6
0.4370 313.15 1012.1
0.5360 313.15 1060.2
0.6560 313.15 1115.3
0.7680 313.15 1163.1
0.8800 313.15 1210.4
1.0000 313.15 1254.1
0.0000 323.15 759.7
0.0750 323.15 805.3
0.1640 323.15 857.5
0.2500 323.15 905.4
0.3530 323.15 960.4
0.4370 323.15 1002.9
0.5360 323.15 1050.9
0.6560 323.15 1106.2
0.7680 323.15 1154.1
0.8800 323.15 1201.6
1.0000 323.15 1245.2
0.0000 333.15 750.0
0.0750 333.15 795.5
0.1640 333.15 847.9
0.2500 333.15 896.0
0.3530 333.15 950.7
0.4370 333.15 993.8
0.5360 333.15 1041.6
0.6560 333.15 1097.0
0.7680 333.15 1145.1
0.8800 333.15 1192.6
1.0000 333.15 1236.6
0.0000 343.15 739.5
0.0750 343.15 785.2
0.1640 343.15 837.9
0.2500 343.15 886.0
0.3530 343.15 941.1
0.4370 343.15 984.3
0.5360 343.15 1032.1
0.6560 343.15 1087.7
0.7680 343.15 1135.9
0.8800 343.15 1183.7
1.0000 343.15 1228.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0000 303.15 777.5
0.0750 303.15 823.6
0.1640 303.15 875.9
0.2500 303.15 924.0
0.3530 303.15 978.7
0.4370 303.15 1021.3
0.5360 303.15 1069.3
0.6560 303.15 1124.3
0.7680 303.15 1172.1
0.8800 303.15 1219.3
1.0000 303.15 1262.9
0.0000 313.15 768.8
0.0750 313.15 814.6
0.1640 313.15 866.9
0.2500 313.15 914.8
0.3530 313.15 969.6
0.4370 313.15 1012.1
0.5360 313.15 1060.2
0.6560 313.15 1115.3
0.7680 313.15 1163.1
0.8800 313.15 1210.4
1.0000 313.15 1254.1
0.0000 323.15 759.7
0.0750 323.15 805.3
0.1640 323.15 857.5
0.2500 323.15 905.4
0.3530 323.15 960.4
0.4370 323.15 1002.9
0.5360 323.15 1050.9
0.6560 323.15 1106.2
0.7680 323.15 1154.1
0.8800 323.15 1201.6
1.0000 323.15 1245.2
0.0000 333.15 750.0
0.0750 333.15 795.5
0.1640 333.15 847.9
0.2500 333.15 896.0
0.3530 333.15 950.7
0.4370 333.15 993.8
0.5360 333.15 1041.6
0.6560 333.15 1097.0
0.7680 333.15 1145.1
0.8800 333.15 1192.6
1.0000 333.15 1236.6
0.0000 343.15 739.5
0.0750 343.15 785.2
0.1640 343.15 837.9
0.2500 343.15 886.0
0.3530 343.15 941.1
0.4370 343.15 984.3
0.5360 343.15 1032.1
0.6560 343.15 1087.7
0.7680 343.15 1135.9
0.8800 343.15 1183.7
1.0000 343.15 1228.1

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 303.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Isopropyl Alcohol (1) - Liquid
0.0093 0.0000
1.6865 0.0490
4.137 0.1530
5.256 0.2260
6.205 0.3040
6.435 0.3650
7.067 0.5490
7.129 0.6720
7.211 0.7790
7.397 0.9010
7.561 0.9830
7.685 0.9920
7.821 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 313.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Isopropyl Alcohol (1) - Liquid
0.0107 0.0000
2.636 0.0490
6.607 0.1530
8.305 0.2260
10.251 0.3040
10.986 0.3650
11.956 0.5490
12.326 0.6720
12.542 0.7790
13.003 0.9010
13.55 0.9830
13.683 0.9920
13.78 1.0000

Sources