Mixture of Ethanol + Tetrahydrofuran

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Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5

Tetrahydrofuran

Name
Tetrahydrofuran
InChI
InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
InChI Key
WYURNTSHIVDZCO-UHFFFAOYSA-N
Formula
C4H8O
SMILES
C1CCOC1
Mol. Weight (g/mol)
72.11
CAS
109-99-9
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)
  3. Vapor Liquid Equilibrium at Constant Pressure (3)

Mole fraction of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid Mole fraction of Tetrahydrofuran (2) - Gas
0.0980 0.2020
0.1890 0.3400
0.2980 0.4670
0.3850 0.5500
0.4880 0.6350
0.6200 0.7200
0.7010 0.7710
0.7980 0.8250
0.8980 0.9010
0.9540 0.9510

Mole fraction of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid Mole fraction of Tetrahydrofuran (2) - Gas
0.0980 0.2020
0.1890 0.3400
0.2980 0.4670
0.3850 0.5500
0.4880 0.6350
0.6200 0.7200
0.7010 0.7710
0.7980 0.8250
0.8980 0.9010
0.9540 0.9510

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0980 348.50
0.1890 346.30
0.2980 344.30
0.3850 342.70
0.4880 341.50
0.6200 340.20
0.7010 339.70
0.7980 339.00
0.8980 338.80
0.9540 338.90

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0980 348.50
0.1890 346.30
0.2980 344.30
0.3850 342.70
0.4880 341.50
0.6200 340.20
0.7010 339.70
0.7980 339.00
0.8980 338.80
0.9540 338.90

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

T [K] - VLE x1[mol/mol] of Tetrahydrofuran (2) - Liquid
351.15 0.0000
349.75 0.0500
348.35 0.1000
345.95 0.2000
344.05 0.3000
342.45 0.4000
341.15 0.5000
340.25 0.6000
339.45 0.7000
339.05 0.8000
338.95 0.9000
338.95 0.9500
338.95 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Tetrahydrofuran (2) - Liquid y1[mol/mol] of Tetrahydrofuran (2) - Vapour
351.55 0.0001 0.0002
351.55 0.0010 0.0019
350.85 0.0200 0.0383
349.85 0.0500 0.1017
348.35 0.1000 0.2070
347.05 0.1500 0.2931
345.85 0.2000 0.3631
344.85 0.2500 0.4231
343.95 0.3000 0.4665
343.25 0.3500 0.5057
342.45 0.4000 0.5455
341.25 0.5000 0.6124
340.85 0.5500 0.6501
340.35 0.6000 0.6805
339.55 0.7000 0.7521
339.25 0.7500 0.7895
338.95 0.8000 0.8276
338.85 0.8500 0.8670
338.75 0.9000 0.9090
338.7 0.9500 0.9527
338.67 0.9800 0.9810
338.65 0.9990 0.9990
338.65 0.9999 0.9999

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 25 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Tetrahydrofuran (2) - Liquid y1[mol/mol] of Tetrahydrofuran (2) - Vapour
319.65 0.0000 0.0000
318.85 0.0146 0.0610
317.45 0.0438 0.1470
314.75 0.1030 0.3020
310.65 0.2290 0.5060
304.35 0.5690 0.7610
302.85 0.7760 0.8560
302.05 0.8790 0.9125
301.75 0.9395 0.9516
301.55 1.0000 1.0000

Sources