Mixture of Ethanol + Butanedioic acid, diethyl ester + Water

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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

Butanedioic acid, diethyl ester

Name
Butanedioic acid, diethyl ester
InChI
InChI=1S/C8H14O4/c1-3-11-7(9)5-6-8(10)12-4-2/h3-6H2,1-2H3
InChI Key
DKMROQRQHGEIOW-UHFFFAOYSA-N
Formula
C8H14O4
SMILES
CCOC(=O)CCC(=O)OCC
Mol. Weight (g/mol)
174.19
CAS
123-25-1

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Temperature, K x Mass fraction (2)
  2. Liquid-liquid equilibrium temperature, K (2)

Temperature, K x Mass fraction [ref]

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

Fixed Measured
Temperature, K - Liquid mixture 1 Mass fraction of Ethanol (1) - Liquid mixture 2 Mass fraction of Water (3) - Liquid mixture 2 Mass fraction of Water (3) - Liquid mixture 1 Mass fraction of Ethanol (1) - Liquid mixture 1
303.15 0.0509 0.0438 0.8224 0.1448
303.15 0.0891 0.0710 0.7490 0.2023
303.15 0.1440 0.0981 0.6925 0.2361
303.15 0.1607 0.1339 0.6412 0.2603
303.15 0.1966 0.1569 0.5870 0.2805
303.15 0.2123 0.1713 0.5803 0.2796
313.15 0.0208 0.0319 0.9504 0.0306
313.15 0.0513 0.0493 0.8944 0.0600
313.15 0.0961 0.0762 0.8372 0.1276
313.15 0.1193 0.1041 0.7574 0.1843

Temperature, K x Mass fraction [ref]

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

Fixed Measured
Temperature, K - Liquid mixture 1 Mass fraction of Ethanol (1) - Liquid mixture 2 Mass fraction of Water (3) - Liquid mixture 2 Mass fraction of Water (3) - Liquid mixture 1 Mass fraction of Ethanol (1) - Liquid mixture 1
303.15 0.0509 0.0438 0.8224 0.1448
303.15 0.0891 0.0710 0.7490 0.2023
303.15 0.1440 0.0981 0.6925 0.2361
303.15 0.1607 0.1339 0.6412 0.2603
303.15 0.1966 0.1569 0.5870 0.2805
303.15 0.2123 0.1713 0.5803 0.2796
313.15 0.0208 0.0319 0.9504 0.0306
313.15 0.0513 0.0493 0.8944 0.0600
313.15 0.0961 0.0762 0.8372 0.1276
313.15 0.1193 0.1041 0.7574 0.1843

Liquid-liquid equilibrium temperature, K [ref]

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

Fixed Measured
Mass fraction of Ethanol (1) - Liquid mixture 1 Mass fraction of Water (3) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.0000 0.9789 313.15
0.0445 0.9341 303.15
0.0467 0.9305 313.15
0.0513 0.9259 303.15
0.0805 0.0494 303.15
0.1401 0.8333 303.15
0.1454 0.0895 313.15
0.1560 0.0958 303.15
0.1676 0.7916 313.15
0.1936 0.1347 313.15
0.2033 0.7580 303.15
0.2037 0.1454 303.15
0.2104 0.1586 313.15
0.2179 0.7391 303.15
0.2203 0.7399 303.15
0.2226 0.7067 313.15
0.2280 0.7180 303.15
0.2342 0.1963 303.15
0.2373 0.7118 303.15
0.2415 0.2292 313.15
0.2563 0.6388 313.15
0.2571 0.2448 303.15
0.2612 0.2943 313.15
0.2724 0.6430 303.15
0.2743 0.3635 313.15
0.2781 0.5704 313.15
0.2888 0.5787 303.15
0.2946 0.4353 303.15

Liquid-liquid equilibrium temperature, K [ref]

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

Fixed Measured
Mass fraction of Ethanol (1) - Liquid mixture 1 Mass fraction of Water (3) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.0000 0.9789 313.15
0.0445 0.9341 303.15
0.0467 0.9305 313.15
0.0513 0.9259 303.15
0.0805 0.0494 303.15
0.1401 0.8333 303.15
0.1454 0.0895 313.15
0.1560 0.0958 303.15
0.1676 0.7916 313.15
0.1936 0.1347 313.15
0.2033 0.7580 303.15
0.2037 0.1454 303.15
0.2104 0.1586 313.15
0.2179 0.7391 303.15
0.2203 0.7399 303.15
0.2226 0.7067 313.15
0.2280 0.7180 303.15
0.2342 0.1963 303.15
0.2373 0.7118 303.15
0.2415 0.2292 313.15
0.2563 0.6388 313.15
0.2571 0.2448 303.15
0.2612 0.2943 313.15
0.2724 0.6430 303.15
0.2743 0.3635 313.15
0.2781 0.5704 313.15
0.2888 0.5787 303.15
0.2946 0.4353 303.15

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