Mixture of Ethanol, 2,2,2-trifluoro- + Water

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Ethanol, 2,2,2-trifluoro-

Name
Ethanol, 2,2,2-trifluoro-
InChI
InChI=1S/C2H3F3O/c3-2(4,5)1-6/h6H,1H2
InChI Key
RHQDFWAXVIIEBN-UHFFFAOYSA-N
Formula
C2H3F3O
SMILES
OCC(F)(F)F
Mol. Weight (g/mol)
100.04
CAS
75-89-8

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. Excess molar enthalpy (molar enthalpy (2)
  2. ρl - Mass density, kg/m3 (2)
  3. Binary diffusion coefficient, m2/s (2)

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0055 -0.0288
0.0109 -0.0543
0.0203 -0.0915
0.0306 -0.1055
0.0402 -0.1030
0.0498 -0.0940
0.0599 -0.0818
0.0700 -0.0666
0.0795 -0.0510
0.0899 -0.0331
0.0994 -0.0140
0.1100 0.0033
0.1193 0.0221
0.1299 0.0406
0.1385 0.0599
0.1486 0.0802
0.1983 0.1774
0.2988 0.3620
0.3988 0.5145
0.4955 0.6264
0.5989 0.6950
0.7078 0.6900
0.8079 0.5423
0.8980 0.3053
0.9054 0.2842
0.9202 0.2398
0.9301 0.2089
0.9387 0.1871
0.9528 0.1441
0.9646 0.1042
0.9732 0.0792
0.9880 0.0403
0.9952 0.0140

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0055 -0.0288
0.0109 -0.0543
0.0203 -0.0915
0.0306 -0.1055
0.0402 -0.1030
0.0498 -0.0940
0.0599 -0.0818
0.0700 -0.0666
0.0795 -0.0510
0.0899 -0.0331
0.0994 -0.0140
0.1100 0.0033
0.1193 0.0221
0.1299 0.0406
0.1385 0.0599
0.1486 0.0802
0.1983 0.1774
0.2988 0.3620
0.3988 0.5145
0.4955 0.6264
0.5989 0.6950
0.7078 0.6900
0.8079 0.5423
0.8980 0.3053
0.9054 0.2842
0.9202 0.2398
0.9301 0.2089
0.9387 0.1871
0.9528 0.1441
0.9646 0.1042
0.9732 0.0792
0.9880 0.0403
0.9952 0.0140

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 997.05
0.0048 1005.99
0.0103 1016.28
0.0186 1031.19
0.0223 1037.71
0.1002 1139.98
0.1985 1215.51
0.3000 1265.59
0.3983 1298.93
0.4965 1322.87
0.5995 1341.54
0.7303 1359.16
0.8390 1370.38
0.9062 1376.17
0.9696 1381.16
0.9800 1381.89
0.9899 1382.59
0.9950 1382.97
1.0000 1383.41

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 997.05
0.0048 1005.99
0.0103 1016.28
0.0186 1031.19
0.0223 1037.71
0.1002 1139.98
0.1985 1215.51
0.3000 1265.59
0.3983 1298.93
0.4965 1322.87
0.5995 1341.54
0.7303 1359.16
0.8390 1370.38
0.9062 1376.17
0.9696 1381.16
0.9800 1381.89
0.9899 1382.59
0.9950 1382.97
1.0000 1383.41

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Temperature, K - Liquid Binary diffusion coefficient, m2/s - Liquid
0.0005 283.20 0.0000
0.0005 288.20 0.0000
0.0005 293.20 0.0000
0.0005 298.20 0.0000
0.0005 303.20 0.0000
0.0005 308.20 0.0000
0.0005 313.20 0.0000
0.0010 283.20 0.0000
0.0010 288.20 0.0000
0.0010 293.20 0.0000
0.0010 298.20 0.0000
0.0010 303.20 0.0000
0.0010 308.20 0.0000
0.0010 313.20 0.0000
0.0050 283.20 0.0000
0.0050 288.20 0.0000
0.0050 293.20 0.0000
0.0050 298.20 0.0000
0.0050 303.20 0.0000
0.0050 308.20 0.0000
0.0050 313.20 0.0000
0.0093 283.20 0.0000
0.0093 288.20 0.0000
0.0093 293.20 0.0000
0.0093 298.20 0.0000
0.0093 303.20 0.0000
0.0093 308.20 0.0000
0.0093 313.20 0.0000
0.0101 283.20 0.0000
0.0101 288.20 0.0000
0.0101 293.20 0.0000
0.0101 298.20 0.0000
0.0101 303.20 0.0000
0.0101 308.20 0.0000
0.0101 313.20 0.0000
0.0496 283.20 0.0000
0.0496 288.20 0.0000
0.0496 293.20 0.0000
0.0496 298.20 0.0000
0.0496 303.20 0.0000
0.0496 308.20 0.0000
0.0496 313.20 0.0000

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Temperature, K - Liquid Binary diffusion coefficient, m2/s - Liquid
0.0005 283.20 0.0000
0.0005 288.20 0.0000
0.0005 293.20 0.0000
0.0005 298.20 0.0000
0.0005 303.20 0.0000
0.0005 308.20 0.0000
0.0005 313.20 0.0000
0.0010 283.20 0.0000
0.0010 288.20 0.0000
0.0010 293.20 0.0000
0.0010 298.20 0.0000
0.0010 303.20 0.0000
0.0010 308.20 0.0000
0.0010 313.20 0.0000
0.0050 283.20 0.0000
0.0050 288.20 0.0000
0.0050 293.20 0.0000
0.0050 298.20 0.0000
0.0050 303.20 0.0000
0.0050 308.20 0.0000
0.0050 313.20 0.0000
0.0093 283.20 0.0000
0.0093 288.20 0.0000
0.0093 293.20 0.0000
0.0093 298.20 0.0000
0.0093 303.20 0.0000
0.0093 308.20 0.0000
0.0093 313.20 0.0000
0.0101 283.20 0.0000
0.0101 288.20 0.0000
0.0101 293.20 0.0000
0.0101 298.20 0.0000
0.0101 303.20 0.0000
0.0101 308.20 0.0000
0.0101 313.20 0.0000
0.0496 283.20 0.0000
0.0496 288.20 0.0000
0.0496 293.20 0.0000
0.0496 298.20 0.0000
0.0496 303.20 0.0000
0.0496 308.20 0.0000
0.0496 313.20 0.0000

Sources