Mixture of Tridecane + Benzene, 1,4-diethyl- + Thiophene, tetrahydro-, 1,1-dioxide

Excel

Tridecane

Name
Tridecane
InChI
InChI=1S/C13H28/c1-3-5-7-9-11-13-12-10-8-6-4-2/h3-13H2,1-2H3
InChI Key
IIYFAKIEWZDVMP-UHFFFAOYSA-N
Formula
C13H28
SMILES
CCCCCCCCCCCCC
Mol. Weight (g/mol)
184.36
CAS
629-50-5

Benzene, 1,4-diethyl-

Name
Benzene, 1,4-diethyl-
InChI
InChI=1S/C10H14/c1-3-9-5-7-10(4-2)8-6-9/h5-8H,3-4H2,1-2H3
InChI Key
DSNHSQKRULAAEI-UHFFFAOYSA-N
Formula
C10H14
SMILES
CCc1ccc(CC)cc1
Mol. Weight (g/mol)
134.22
CAS
105-05-5

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. Temperature, K x Mole fraction (2)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Benzene, 1,4-diethyl- (2) - Liquid mixture 1 Mole fraction of Tridecane (1) - Liquid mixture 1 Mole fraction of Tridecane (1) - Liquid mixture 2 Mole fraction of Benzene, 1,4-diethyl- (2) - Liquid mixture 2
323.15 0.0000 0.9939 0.0015 0.0000
323.15 0.1262 0.8671 0.0016 0.0122
323.15 0.2356 0.7549 0.0017 0.0237
323.15 0.3641 0.6216 0.0019 0.0430
323.15 0.4673 0.5108 0.0020 0.0579
323.15 0.5614 0.4057 0.0023 0.0825
323.15 0.6572 0.2904 0.0026 0.1126
323.15 0.7286 0.1622 0.0028 0.1686
348.15 0.0000 0.9888 0.0026 0.0000
348.15 0.1276 0.8633 0.0028 0.0158
348.15 0.2538 0.7322 0.0030 0.0338
348.15 0.3721 0.6041 0.0035 0.0570
348.15 0.4676 0.4962 0.0038 0.0728
348.15 0.5662 0.3750 0.0045 0.1045
348.15 0.6469 0.2574 0.0056 0.1436
348.15 0.6866 0.1632 0.0067 0.1908
373.15 0.0000 0.9790 0.0045 0.0000
373.15 0.1545 0.8236 0.0055 0.0247
373.15 0.2495 0.7246 0.0065 0.0402
373.15 0.3378 0.6212 0.0067 0.0598
373.15 0.4308 0.5083 0.0072 0.0821
373.15 0.5343 0.3588 0.0081 0.1246
373.15 0.5923 0.2427 0.0083 0.1670
373.15 0.5998 0.1475 0.0114 0.2299

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Benzene, 1,4-diethyl- (2) - Liquid mixture 1 Mole fraction of Tridecane (1) - Liquid mixture 1 Mole fraction of Tridecane (1) - Liquid mixture 2 Mole fraction of Benzene, 1,4-diethyl- (2) - Liquid mixture 2
323.15 0.0000 0.9939 0.0015 0.0000
323.15 0.1262 0.8671 0.0016 0.0122
323.15 0.2356 0.7549 0.0017 0.0237
323.15 0.3641 0.6216 0.0019 0.0430
323.15 0.4673 0.5108 0.0020 0.0579
323.15 0.5614 0.4057 0.0023 0.0825
323.15 0.6572 0.2904 0.0026 0.1126
323.15 0.7286 0.1622 0.0028 0.1686
348.15 0.0000 0.9888 0.0026 0.0000
348.15 0.1276 0.8633 0.0028 0.0158
348.15 0.2538 0.7322 0.0030 0.0338
348.15 0.3721 0.6041 0.0035 0.0570
348.15 0.4676 0.4962 0.0038 0.0728
348.15 0.5662 0.3750 0.0045 0.1045
348.15 0.6469 0.2574 0.0056 0.1436
348.15 0.6866 0.1632 0.0067 0.1908
373.15 0.0000 0.9790 0.0045 0.0000
373.15 0.1545 0.8236 0.0055 0.0247
373.15 0.2495 0.7246 0.0065 0.0402
373.15 0.3378 0.6212 0.0067 0.0598
373.15 0.4308 0.5083 0.0072 0.0821
373.15 0.5343 0.3588 0.0081 0.1246
373.15 0.5923 0.2427 0.0083 0.1670
373.15 0.5998 0.1475 0.0114 0.2299

Sources