Mixture of 1,2-Ethanediol + Ethyl Acetate

Excel

1,2-Ethanediol

Name
1,2-Ethanediol
InChI
InChI=1S/C2H6O2/c3-1-2-4/h3-4H,1-2H2
InChI Key
LYCAIKOWRPUZTN-UHFFFAOYSA-N
Formula
C2H6O2
SMILES
OCCO
Mol. Weight (g/mol)
62.07
CAS
107-21-1

Ethyl Acetate

Name
Ethyl Acetate
InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Mol. Weight (g/mol)
88.11
CAS
141-78-6
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. Mole fraction (8)
  2. Vapor Liquid Equilibrium at Constant Pressure

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of Ethyl Acetate (2) - Liquid mixture 1
288.15 0.1228
293.15 0.1321
298.15 0.1427
303.15 0.1562
313.15 0.1911
323.15 0.2543

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mole fraction of Ethyl Acetate (2) - Liquid mixture 2
288.15 0.8953
293.15 0.8819
298.15 0.8648
303.15 0.8444
313.15 0.7905
323.15 0.6954

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of Ethyl Acetate (2) - Liquid mixture 1
293.99 0.1338
299.07 0.1456
317.40 0.2136
327.35 0.3268
327.68 0.3236
328.19 0.3432
329.04 0.4288

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mole fraction of Ethyl Acetate (2) - Liquid mixture 2
296.67 0.8741
299.21 0.8648
323.63 0.6936
328.05 0.5665
328.98 0.5086
329.06 0.4606

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of Ethyl Acetate (2) - Liquid mixture 1
288.15 0.1228
293.15 0.1321
298.15 0.1427
303.15 0.1562
313.15 0.1911
323.15 0.2543

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mole fraction of Ethyl Acetate (2) - Liquid mixture 2
288.15 0.8953
293.15 0.8819
298.15 0.8648
303.15 0.8444
313.15 0.7905
323.15 0.6954

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of Ethyl Acetate (2) - Liquid mixture 1
293.99 0.1338
299.07 0.1456
317.40 0.2136
327.35 0.3268
327.68 0.3236
328.19 0.3432
329.04 0.4288

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mole fraction of Ethyl Acetate (2) - Liquid mixture 2
296.67 0.8741
299.21 0.8648
323.63 0.6936
328.05 0.5665
328.98 0.5086
329.06 0.4606

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl Acetate (2) - Liquid y1[mol/mol] of Ethyl Acetate (2) - Vapour
470.35 0.0000 0.0000
456.45 0.0050 0.3640
447.85 0.0060 0.5460
434.75 0.0080 0.7400
421.85 0.0100 0.8800
413.15 0.0140 0.9360
391.15 0.0260 0.9700
363.65 0.0800 0.9790
357.15 0.1200 0.9850
354.65 0.1440 0.9840
354.55 0.2060 0.9840
354.35 0.2220 0.9840
354.25 0.2830 0.9840
354.15 0.3210 0.9840
353.85 0.4060 0.9840
353.35 0.4570 0.9840
352.85 0.5830 0.9840
351.75 0.7800 0.9900
350.95 0.8850 0.9940
350.55 0.9880 0.9990
350.25 1.0000 1.0000

Sources