Mixture of n-Hexane + Thiophene, tetrahydro-, 1,1-dioxide

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n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

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. Mole fraction (4)
  2. Vapor Liquid Equilibrium at Constant Pressure (3)

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of n-Hexane (1) - Liquid mixture 1
300.30 0.9999
307.43 0.9995
323.51 0.9987
348.72 0.9966
363.36 0.9918
372.41 0.9893
377.72 0.9849
384.43 0.9842
393.92 0.9788
403.51 0.9756
412.29 0.9706
422.92 0.9681
429.93 0.9608

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 2 Mole fraction of n-Hexane (1) - Liquid mixture 2
300.30 0.0092
307.43 0.0150
323.51 0.0203
348.72 0.0276
363.36 0.0332
372.41 0.0432
377.72 0.0469
384.43 0.0520
393.92 0.0584
403.51 0.0698
412.29 0.0794
422.92 0.0980
429.93 0.1161

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of n-Hexane (1) - Liquid mixture 1
300.30 0.9999
307.43 0.9995
323.51 0.9987
348.72 0.9966
363.36 0.9918
372.41 0.9893
377.72 0.9849
384.43 0.9842
393.92 0.9788
403.51 0.9756
412.29 0.9706
422.92 0.9681
429.93 0.9608

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 2 Mole fraction of n-Hexane (1) - Liquid mixture 2
300.30 0.0092
307.43 0.0150
323.51 0.0203
348.72 0.0276
363.36 0.0332
372.41 0.0432
377.72 0.0469
384.43 0.0520
393.92 0.0584
403.51 0.0698
412.29 0.0794
422.92 0.0980
429.93 0.1161

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 79.99 (VLE)

T [K] - VLE x1[mol/mol] of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid
334.65 0.0000
332.95 0.0010
330.95 0.0019
330.85 0.0021
329.15 0.0029
327.35 0.0039
492.65 0.9864
503.95 0.9893
516.45 0.9924
535.25 0.9972
541.45 0.9988
546.35 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 93.33 (VLE)

T [K] - VLE x1[mol/mol] of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid
339.25 0.0000
337.15 0.0010
335.15 0.0019
334.95 0.0021
332.75 0.0029
330.95 0.0039
504.85 0.9864
515.15 0.9893
525.75 0.9924
542.95 0.9972
548.25 0.9988
552.75 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 99.99 (VLE)

T [K] - VLE x1[mol/mol] of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid
341.45 0.0000
339.25 0.0010
337.15 0.0019
336.95 0.0021
334.45 0.0029
332.65 0.0039
510.75 0.9864
520.65 0.9893
530.85 0.9924
546.45 0.9972
551.65 0.9988
555.65 1.0000

Sources