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

Excel

Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

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. Temperature, K x Mass fraction (2)
  2. Vapor Liquid Equilibrium at Constant Pressure

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mass fraction of Thiophene, tetrahydro-, 1,1-dioxide (3) - Liquid mixture 2 Mass fraction of Benzene (1) - Liquid mixture 2 Mass fraction of Thiophene, tetrahydro-, 1,1-dioxide (3) - Liquid mixture 1 Mass fraction of Benzene (1) - Liquid mixture 1
308.15 0.6923 0.2776 0.0981 0.4351
308.15 0.7192 0.2532 0.0693 0.4203
308.15 0.7626 0.2142 0.0391 0.3807
308.15 0.8194 0.1612 0.0277 0.3029
313.15 0.6477 0.3085 0.0901 0.4232
313.15 0.7209 0.2449 0.0761 0.4086
313.15 0.7503 0.2256 0.0715 0.3842
313.15 0.8059 0.1705 0.0574 0.2844
313.15 0.8398 0.1396 0.0499 0.2392
318.15 0.6696 0.2875 0.0798 0.4434
318.15 0.7247 0.2396 0.0704 0.4250
318.15 0.7819 0.1923 0.0598 0.3854
318.15 0.8335 0.1456 0.0485 0.3001

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mass fraction of Thiophene, tetrahydro-, 1,1-dioxide (3) - Liquid mixture 2 Mass fraction of Benzene (1) - Liquid mixture 2 Mass fraction of Thiophene, tetrahydro-, 1,1-dioxide (3) - Liquid mixture 1 Mass fraction of Benzene (1) - Liquid mixture 1
308.15 0.6923 0.2776 0.0981 0.4351
308.15 0.7192 0.2532 0.0693 0.4203
308.15 0.7626 0.2142 0.0391 0.3807
308.15 0.8194 0.1612 0.0277 0.3029
313.15 0.6477 0.3085 0.0901 0.4232
313.15 0.7209 0.2449 0.0761 0.4086
313.15 0.7503 0.2256 0.0715 0.3842
313.15 0.8059 0.1705 0.0574 0.2844
313.15 0.8398 0.1396 0.0499 0.2392
318.15 0.6696 0.2875 0.0798 0.4434
318.15 0.7247 0.2396 0.0704 0.4250
318.15 0.7819 0.1923 0.0598 0.3854
318.15 0.8335 0.1456 0.0485 0.3001

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of n-Hexane (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of n-Hexane (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
344.65 0.0618 0.2110 0.7511 0.2488
346.25 0.0750 0.3263 0.6303 0.3696
364.35 0.0220 0.2480 0.4660 0.5339
354.95 0.0350 0.2350 0.6170 0.3825
351.15 0.0450 0.2230 0.7060 0.2938
347.75 0.0485 0.2233 0.6853 0.3146
347.35 0.0629 0.3201 0.6232 0.3767
346.05 0.1083 0.4464 0.5670 0.4329
345.75 0.0548 0.1957 0.7373 0.2626

Sources